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225-036
Originated: Delivered to:9-Oct-25Alaska Oil & Gas Conservation Commiss09Oct25-NR ! "# $$%$ !&$$'($)*%+ ($)*%,- .WELL NAME API #SERVICE ORDER #FIELD NAMESERVICE DESCRIPTIONDELIVERABLE DESCRIPTION DATA TYPE DATE LOGGED3T-613 50-103-20914-00-00 225-036 Kuparuk River WL TTiX-FSI FINAL FIELD 15-Sep-251D-30 50-029-22965-00-00 200-104 Kuparuk River WL Lee-LDL FINAL FIELD 21-Sep-253M-12 50-029-21719-00-00 187-050 Kuparuk River WL IPROF FINAL FIELD 28-Sep-252X-01 50-029-20963-00-00 183-084 Kuparuk River WL IPROF FINAL FIELD 30-Sep-25Transmittal Receipt//////////////////////////////// 0///////////////////////////////// + ! 1 Please return via courier or sign/scan and email a copy to Schlumberger. " 2"3 +45 %TRANSMITTAL DATETRANSMITTAL #1 67 8 " ! - +" 8 # !(3 . 8 ) "3 8 # !9 3 : 8" +8 6 8 8 " 8 # !;" " 3 - 3 " 3 ""+ 3 + < +3!% T40984T40985T40986T409873T-61350-103-20914-00-00225-036Kuparuk RiverWLTTiX-FSIFINAL FIELD15-Sep-25Gavin GluyasDigitally signed by Gavin Gluyas Date: 2025.10.10 08:21:47 -08'00' WELL NAME API #SERVICE ORDER #FIELD NAMESERVICE DESCRIPTION DELIVERABLE DESCRIPTION DATA TYPE DATE LOGGEDCOLOR PRINTS E-Delivery3S-721 50-103-20911-00-00 225-025 KUPARUK RIVER MWD/LWD/DD TOP OF CEMENT FINAL FIELD 7-May-25 13T-613 50-103-20914-00-00 225-036 KUPARUK RIVER MWD/LWD/DD TOP OF CEMENT FINAL FIELD 23-May-25 13T-605 50-103-20917-00-00 225-051 KUPARUK RIVER MWD/LWD/DD TOP OF CEMENT FINAL FIELD 21-Jun-25 13S-719 50-103-20919-00-00 225-058 KUPARUK RIVER MWD/LWD/DD TOP OF CEMENT FINAL FIELD 15-Jul-25 1Transmittal Receipt________________________________ X____________________________________________Print Name Signature DatePlease return via courier or sign/scan and email a copy to Schlumberger.aurana@slb.comSLB Auditor - A Transmittal Receipt signature confirms that a package (box, envelope, etc.) has been received and the contents of the package have been verified to match the media noted above. The specific content of the CDs and/or hardcopy prints may or may not have been verified for correctness or quality level at this point.# Schlumberger-PrivateT40687T40688T40689T406903T-61350-103-20914-00-00225-036KUPARUK RIVERMWD/LWD/DDTOP OF CEMENTFINAL FIELD23-May-251Gavin GluyasDigitally signed by Gavin Gluyas Date: 2025.07.28 08:43:18 -08'00' WELL NAME API #SERVICE ORDER #FIELD NAMESERVICE DESCRIPTION DELIVERABLE DESCRIPTION DATA TYPE DATE LOGGEDCOLOR PRINTS E-Delivery3T-613 50-103-20914-00-00 225-036 KUPARUK RIVER MWD/LWD/DD VISION Service FINAL FIELD 31-May-25 1Transmittal Receipt________________________________ X____________________________________________Print Name Signature DatePlease return via courier or sign/scan and email a copy to Schlumberger.aurana@slb.comSLB Auditor - A Transmittal Receipt signature confirms that a package (box, envelope, etc.) has been received and the contents of the package have been verified to match the media noted above. The specific content of the CDs and/or hardcopy prints may or may not have been verified for correctness or quality level at this point.# Schlumberger-Private225-036T40658Gavin GluyasDigitally signed by Gavin Gluyas Date: 2025.07.15 09:22:04 -08'00' 1. Operations Susp Well Insp Plug Perforations Fracture Stimulate Pull Tubing Operations shutdown Performed: Install Whipstock Perforate Other Stimulate Alter Casing Change Approved Program Mod Artificial Lift Perforate New Pool Repair Well Coiled Tubing Ops Other: ______________________ ConocoPhillips Alaska Inc. Development Exploratory 3. Address: Stratigraphic Service 6. API Number: P.O. Box 100360, Anchorage, Alaska 99510-0360 7. Property Designation (Lease Number): 8. Well Name and Number: 9. Logs (List logs and submit electronic data per 20AAC25.071): 10. Field/Pool(s): 11. Present Well Condition Summary: Total Depth measured 23631 feet feet true vertical 5031 feet feet Effective Depth measured 23618 feet 12349 / 12457 feet true vertical 5031 feet 4910 / 4936 feet Perforation depth Measured depth NA feet True Vertical depth NA feet Tubing (size, grade, measured and true vertical depth) 4-1/2" L-80 12469' MD 4939' TVD TNT Packer 12349' MD 4910' TVD Packers and SSSV (type, measured and true vertical depth) ZXP 12457' MD 4936' TVD 12. Stimulation or cement squeeze summary: Intervals treated (measured): Treatment descriptions including volumes used and final pressure: 13a. Prior to well operation: Subsequent to operation: 13b. Pools active after work:Torok Oil Pool 15. Well Class after work: Daily Report of Well Operations Exploratory Development Service Stratigraphic Copies of Logs and Surveys Run 16. Well Status after work: Oil Gas WDSPL Electronic Fracture Stimulation Data GSTOR GINJ SUSP SPLUG Sundry Number or N/A if C.O. Exempt: Authorized Name and Digital Signature with Date: Contact Name: Allen Eschete Contact Email:Allen.Eschete@ConocoPhillips.com Authorized Title: Senior Completions Engineer Contact Phone: 325-345 Sr Pet Eng: 9210 Sr Pet Geo: Sr Res Eng: WINJ WAG Water-BblOil-Bbl 17. I hereby certify that the foregoing is true and correct to the best of my knowledge. 907-265-6558 14. Attachments (required per 20 AAC 25.070, 25.071, & 25.283) measured true vertical Packer Representative Daily Average Production or Injection Data Casing Pressure Tubing PressureGas-Mcf MD 13361' MD - 23281' MD Size 119 52102695 7-5/8" 11590 7-5/8" 4790 7850 6890 10860 STATE OF ALASKA ALASKA OIL AND GAS CONSERVATION COMMISSION REPORT OF SUNDRY WELL OPERATIONS 225-036 50-103-20914-00-00 5. Permit to Drill Number:2. Operator Name 4. Well Class Before Work: ADL025528 / ADL393883 / ADL 393884 Kuparuk Field / Torok Oil Pool KRU 3T-613 Plugs Junk measured 3,743,524 pounds of Wanli 16/20 Ceramic. 63,000 pounds of 100 mesh, and avg treating pressure 4,000-5,500 psi. Length 80 2400 119Conductor Surface Intermediate 20" 10-3/4" measured TVD Intermediate Liner 11592 1034 11161 Casing Structural 4740 4982 4-1/2" 11630 12664 23618 5031 2437 Burst Collapse 2470 Development Service GINJ SUSP SPLUG Gas Form 10-404 Revised 10/2022 Due Within 30 days of Operations Submit in PDF format to aogcc.permitting@alaska.gov By Grace Christianson at 2:15 pm, Jul 10, 2025 Digitally signed by Allen Eschete DN: OU=ConocoPhillips Alaska, O=Completions Engineering, CN =Allen Eschete, E=Allen.Eschete@ConocoPhillips.com Reason: I am the author of this document Location: Date: 2025.07.10 07:20:25-08'00' Foxit PDF Editor Version: 13.1.6 Allen Eschete JJL 7/21/25 CDW 07/14/2025 RBDMS JSB 071025 DSR-7/21/24 Sales Order# Prepared By: Steven Sanders James Campbell Nannook Crew 910128224 Intervals 1-21 Moraine Notice: Although the information contained in this report is based on sound engineering practices, the copyright owner(s) does (do) not accept any responsibility whatsoever, in negligence or otherwise, for any loss or damage arising from the possession or use of the report whether in terms of correctness or otherwise. The application, therefore, by the user of this report or any part thereof, is solely at the user’s own risk. 3T-613 Conoco Phillips Harrison Bay County, AK Post Job Report Stimulation Treatment API: 50-103-20914 Prepared for: Chad Burkett June 22, 2025 Moraine Formation 30# Hybor G-i Table of Contents Section Page(s) Executive Summary Actual Design Wellbore Information Interval Summary Fluid System-Proppant Summary Interval 1 Plots Interval 2 Plots Interval 3 Plots Interval 4 Plots Interval 5 Plots Interval 6 Plots Interval 7 Plots Interval 8 Plots Interval 9 Plots Interval 10 Plots Interval 11 Plots Interval 12 Plots Interval 13 Plots Interval 14 Plots Interval 15 Plots Interval 16 Plots Interval 17 Plots Interval 18 Plots Interval 19 Plots Interval 20 Plots Interval 21 Plots Appendix Planned Design Well Summary Chemical Summary Prejob Break Test Water Analysis 6-15 Water Analysis 6-17 Water Analysis 6-18 Water Analysis 6-19 Water Analysis 6-20 Water Analysis 6-21 Water Straps 6-16 Water Straps 6-17 Water Straps 6-18 Water Straps 6-19 Water Straps 6-20 Water Straps 6-21 Real-Time QC Fann 15 Minute Interval 1 Fann 15 Minute Interval 2 Fann 15 Minute Interval 3 Fann 15 Minute Interval 4 Fann 15 Minute Interval 5 Fann 15 Minute Interval 6 Fann 15 Minute Interval 7 Fann 15 Minute Interval 8 Fann 15 Minute Interval 9 Fann 15 Minute Interval 10 Fann 15 Minute Interval 11 Fann 15 Minute Interval 12 Fann 15 Minute Interval 13 Fann 15 Minute Interval 14 Fann 15 Minute Interval 15 Fann 15 Minute Interval 16 Fann 15 Minute Interval 17 Fann 15 Minute Interval 18 Fann 15 Minute Interval 19 Fann 15 Minute Interval 20 Fann 15 Minute Interval 21 Sand Sieve Analysis Event Log 6.16.25 Event Log 6.17.25 Event Log 6.18.25 Event Log 6.19.25 Event Log 6.20.25 239 240 234 235 236 237 238 229 230 231 232 233 224 225 226 227 228 219 220 221 222 223 214 215 216 217 218 209 210 211 212 213 204 205 206 207 208 199 200 201 202 203 172 - 183 184 - 191 192 193 - 197 198 148 - 151 152 - 155 156 - 159 160 - 167 168 - 171 136 - 147 92 - 95 96 - 99 132 - 135 76 - 83 84 - 87 88 - 91 100 - 115 116 - 119 120 - 123 124 - 127 128 - 131 11 - 52 53 54 - 67 68 - 75 4 3 - 9 10 Conoco Phillips - 3T-613 TOC 2 Event Log 6.21.25 241 Conoco Phillips - 3T-613 TOC 3 220,805 gallons of 30# Linear 11,880 gallons of Freeze Protect 1,559,975 gallons of 30# Hybor G-i 3,781,700 pounds of Wanli 16/20 Ceramic 63,000 pounds of 100M 215,971 gallons of 30# Linear 6,609 gallons of Freeze Protect 1,599,139 gallons of 30# Hybor G-i 3,743,524 pounds of Wanli 16/20 Ceramic 63,000 pounds of 100M Thank you, Halliburton maintains a continuous quality improvement process and appreciates any comments or suggestions that you may have. Halliburton again thanks you for the opportunity to perform service work on this well. We hope to be your solutions provider for future projects. Engineering Executive Summary On June 16, 2025 a stimulation treatment was performed in the A-Sand formation on the 3T-613 well in Harrison Bay County, The actual treatment fully completed 21 of 21 stages. 0 stages were skipped, 0 stage screened out and 0 stages were cut short of design. The actual treatment consisted of: A more detailed description of the actual treatment can be found in the attached reports. The following comments were provided to summarize events and changes to the proposed treatment: The ResMetric tracer that was planned to run on intervals 2 - 21 had a delay in the shipment so the customer engineer made the call to not run it during this well. Patina tracer was run on interval 1 as per the design. During interval 2, three pumps went offline so the OSR called to stage into flush. After performing maintenance and swapping out a pump, the interval was restared with 6 pumps and completed with no further issues. On 6/17, due to a material shortage of breaker, 4 stages were pumped before shutting down for the day; operations resumed the afternoon of 6/18 once the material arrived to location. While pumping interval 8, two pumps went offline due to overheating and one pump went offline due to a leak on the suction manifold, the OSR called to shut down for the day once the dart was seated. After maintenancing all pumps during the night, operations resumed in the morning with 6 pumps. On interval 18, in order to give a third party more time to load proppant in the mover, the job was shut down after the dart seated and a DFIT was run. Pressure was monitored while proppant was being loaded; after two bins were filled, the interval resumed with no further issues. On interval 20, a sucton hose on a pump burst causing a spike in the blender discharge rate, the pump was shut in and the remainder of the interval pumped as per design. Halliburton is strongly committed to quality control on location. Before and after each job all chemicals, proppants, and fluid volumes are measured to assure the highest level of quality control. Tank fluid analysis, crosslink time, and break tests are performed before each job in order to optimize the performance of the treatment fluids. Steven Sanders Senior Technical Professional Conoco Phillips - 3T-613 Executive Summary 4 CUSTOMERConoco Phillips APIBFD (lb/gal)8.48LAT 70.42061242LEASE3T-613SALES ORDEBHST (°F)139LONG-150.266098FORMATIONMoraineDATE Max Pressure (psi)8500*Exceeds 80% of burst pressure*Prop Slurry Design Clean Actual Clean Actual Clean Calculated Slurry Design Prop Calculated Prop CL-28M BC-140X2 Losurf-300D MO-67 WG-36 OPTIFLO-III OPTIFLO-II BE-6Treatment Stage Fluid Stage Proppant Conc Rate Volume Volume Volume Volume Total TotalCrosslinker Crosslinker Surfactant Buffer Gel Breaker Breaker BiocideInterval Number Description Description Description(ppg) (bpm) (gal) (gal) (bbl) (bbl) (lbs) (lbs)(gpt) (gpt) (gpt) (gpt) (ppt) (ppt) (ppt) (ppt)1-1 Shut-In Shut-In-1-2 Freeze Protect Prime Up Pressure Test 5.0 1,000 571 14 141-3 Shut-In Shut-In-1-4 30# Linear Pre-Pad 10.0 2,100 859 20 201.00 30.00 2.00 2.00 0.151-5 30# Linear DFIT 10.0 1,680 2,740 65 651.00 30.00 2.00 2.00 0.151-6 Shut-In Shut-In-1-7 30# Linear Step Rate Test 15.0 8,400 9,565 228 2281.00 30.00 2.00 2.00 0.151-8 30# Hybor G-i Establish Stable Fluid 15.0 8,400 2,064 49 49 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.151-9 30# Hybor G-i Pad 37.0 16,030 16,096 383 383 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.151-10 30# Hybor G-i Conditioning Pad 100M 0.25 37.0 12,000 12,016 286 289 3,000 3,000 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.151-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37.0 10,200 10,244 244 253 10,200 8,786 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.151-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37.0 13,600 13,629 325 351 27,200 24,831 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.151-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37.0 13,600 13,609 324 365 40,800 38,713 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.151-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37.0 8,500 8,531 203 238 34,000 32,960 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.151-15 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37.0 6,800 6,800 162 191 30,600 27,436 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.151-16 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37.0 5,440 8,385 200 235 27,200 33,506 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.151-17 30# Linear Spacer and Dart Drop 37.0 2,041 2,324 55 551.00 30.00 2.00 2.00 0.152-1 30# Linear Pre-Pad 37.0 2,100 2,120 50 501.00 30.00 2.00 0.152-2 30# Hybor G-i Establish Stable Fluid 37.0 2,100 8,869 211 211 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.152-3 30# Hybor G-i Pad 37.0 15,500 15,859 378 378 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.152-4 30# Hybor G-i Conditioning Pad 100M 0.25 37.0 12,000 12,184 290 293 3,000 3,000 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.152-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37.0 10,200 13,382 319 331 10,200 11,453 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.152-6 30# Linear Flush 37.0 15,145 15,227 363 3631.00 30.00 2.00 2.00 0.152-7 30# Hybor G-i Establish Stable Fluid 37.0 2,100 1,552 37 37 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.152-8 30# Hybor G-i Pad 37.0 15,500 15,587 371 371 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.152-9 30# Hybor G-i Conditioning Pad 100M 0.25 37.0 12,000 12,036 287 290 3,000 3,000 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.152-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37.0 10,200 10,233 244 253 10,200 8,718 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.152-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37.0 12,750 12,755 304 329 25,500 24,272 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.152-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37.0 14,110 14,139 337 382 42,330 43,058 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.152-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37.0 6,375 6,392 152 179 25,500 25,548 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.152-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37.0 5,270 5,260 125 150 23,715 23,336 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.152-15 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37.0 4,437 4,411 105 128 22,185 21,806 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.152-16 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37.0 3,740 6,500 155 182 20,570 25,461 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.152-17 30# Linear Flush 37.0 15,145 15,336 365 3651.00 30.00 2.00 2.00 0.152-18 Freeze Protect Freeze Protect 10.0 1,470 1,470 35 352-19 Shut-In Shut-In-3-1 Shut-In Shut-In-3-2 Freeze Protect Prime Up Pressure Test 5.0 1,000 571 14 143-3 Shut-In Shut-In-3-4 30# Linear Spacer and Dart Drop 15.0 1,260 1,541 37 371.00 30.00 2.00 2.00 0.153-5 30# Linear Pre-Pad 37.0 8,400 2,069 49 491.00 30.00 2.00 2.00 0.153-6 30# Hybor G-i Establish Stable Fluid 37.0 2,100 3,346 80 80 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.153-7 30# Hybor G-i Pad 37.0 14,800 23,142 551 551 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.153-8 30# Hybor G-i Conditioning Pad 100M 0.25 37.0 12,000 30,373 723 726 3,000 3,000 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.153-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37.0 10,200 10,229 244 252 10,200 7,498 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.153-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37.0 12,750 12,802 305 328 25,500 22,070 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.153-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37.0 11,900 11,912 284 320 35,700 33,827 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.153-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37.0 8,500 8,506 203 238 34,000 33,831 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.153-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37.0 6,800 6,847 163 199 34,000 34,024 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.153-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37.0 5,100 7,318 174 215 30,600 38,507 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.153-15 30# Linear Spacer and Dart Drop 37.0 2,041 2,190 52 521.00 30.00 2.00 2.00 0.154-1 30# Linear Pre-Pad 37.0 2,100 2,114 50 501.00 30.00 2.00 2.00 0.154-2 30# Hybor G-i Establish Stable Fluid 37.0 8,400 3,282 78 78 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.154-3 30# Hybor G-i Pad 37.0 10,785 10,801 257 257 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.154-4 30# Hybor G-i Conditioning Pad 100M 0.25 37.0 12,000 12,064 287 290 3,000 3,000 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.154-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37.0 7,225 7,214 172 179 7,225 6,891 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.154-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37.0 7,225 7,285 173 188 14,450 13,930 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.154-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37.0 6,800 6,835 163 185 20,400 20,817 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.154-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37.0 7,650 7,660 182 215 30,600 30,964 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.154-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37.0 6,800 6,764 161 197 34,000 34,213 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.154-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37.0 5,950 5,931 141 179 35,700 35,793 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.154-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37.0 4,250 6,011 143 173 27,625 28,508 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.154-12 30# Linear Spacer and Dart Drop 37.0 2,041 2,660 63 631.00 30.00 2.00 2.00 0.155-1 30# Linear Pre-Pad 37.0 2,100 2,275 54 541.00 30.00 2.00 2.00 0.155-2 30# Hybor G-i Establish Stable Fluid 37.0 8,400 3,713 88 88 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.155-3 30# Hybor G-i Pad 37.0 6,450 6,602 157 157 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.155-4 30# Hybor G-i Conditioning Pad 100M 0.25 37.0 12,000 12,023 286 290 3,000 3,000 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.155-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37.0 1,700 1,746 42 43 1,700 1,587 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.155-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37.0 2,175 2,177 52 56 4,350 3,978 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.155-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37.0 3,400 3,412 81 92 10,200 10,084 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.155-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37.0 4,100 4,105 98 115 16,400 16,540 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.155-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37.0 4,240 4,285 102 123 19,080 19,627 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.155-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37.0 4,600 4,611 110 135 23,000 23,310 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.155-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37.0 4,680 4,688 112 139 25,740 25,699 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.155-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37.0 4,930 4,937 118 149 29,580 29,479 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.155-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37.0 3,400 3,453 82 106 22,100 22,226 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.155-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37.0 2,550 3,780 90 109 17,850 17,958 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.155-15 30# Linear Spacer and Dart Drop 37.0 2,041 2,102 50 501.00 30.00 2.00 2.00 0.15Interval 1Moraine@ 23276.81 - 23281.15 ft 137.3 °FInterval 2Moraine@ 22818.85 - 22823.19 ft 137.4 °FInterval 3Moraine@ 22324.92 - 22329.26 ft 137.6 °FInterval 4Moraine@ 21829.56 - 21833.9 ft 137.8 °FInterval 5Moraine@ 21331.62 - 21335.96 ft 138 °FLiquid AdditivesDry Additives50-103-20914910128224Conoco Phillips - 3T-613Actual Design5 CUSTOMERConoco Phillips APIBFD (lb/gal)8.48LAT 70.42061242LEASE3T-613SALES ORDEBHST (°F)139LONG-150.266098FORMATIONMoraineDATE Max Pressure (psi)8500*Exceeds 80% of burst pressure*Prop Slurry Design Clean Actual Clean Actual Clean Calculated Slurry Design Prop Calculated Prop CL-28M BC-140X2 Losurf-300D MO-67 WG-36 OPTIFLO-III OPTIFLO-II BE-6Treatment Stage Fluid Stage Proppant Conc Rate Volume Volume Volume Volume Total TotalCrosslinker Crosslinker Surfactant Buffer Gel Breaker Breaker BiocideInterval Number Description Description Description(ppg) (bpm) (gal) (gal) (bbl) (bbl) (lbs) (lbs)(gpt) (gpt) (gpt) (gpt) (ppt) (ppt) (ppt) (ppt)Liquid AdditivesDry Additives50-103-209149101282246-1 30# Linear Pre-Pad 37.0 2,100 2,165 52 521.00 30.00 2.00 0.156-2 30# Hybor G-i Establish Stable Fluid 37.0 8,400 4,800 114 114 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.156-3 30# Hybor G-i Pad 37.0 6,450 6,442 153 153 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.156-4 30# Hybor G-i Conditioning Pad 100M 0.25 37.0 12,000 11,996 286 289 3,000 3,000 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.156-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37.0 1,700 1,696 40 42 1,700 1,079 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.156-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37.0 2,175 2,223 53 57 4,350 3,733 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.156-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37.0 3,400 3,422 81 92 10,200 10,191 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.156-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37.0 4,100 4,108 98 116 16,400 16,842 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.156-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37.0 4,240 4,244 101 121 19,080 19,226 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.156-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37.0 4,600 4,621 110 135 23,000 23,074 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.156-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37.0 4,680 4,697 112 139 25,740 25,563 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.156-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37.0 4,930 4,972 118 150 29,580 29,909.00 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.156-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37.0 3,400 3,418 81 105 22,100 21,805 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.156-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37.0 2,550 4,647 111 131 17,850 19,309 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.156-15 30# Linear Flush 37.0 15,145 13,983 333 3331.00 30.00 2.00 2.00 0.156-16 Freeze Protect Freeze Protect 10.0 1,470 571 14 146-17 Shut-In Shut-In-7-1 Shut-In Shut-In-7-2 Freeze Protect Prime Up Pressure Test 5.0 1,000 571 14 147-3 Shut-In Shut-In-7-4 30# Linear Spacer and Dart Drop 20.0 2,100 1,291 31 311.00 30.00 2.00 2.00 0.157-5 30# Linear Pre-Pad 37.0 2,100 2,108 50 501.00 30.00 2.00 2.00 0.157-6 30# Hybor G-i Establish Stable Fluid 37.0 8,400 2,387 57 57 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.157-7 30# Hybor G-i Pad 37.0 6,450 6,444 153 153 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.157-8 30# Hybor G-i Conditioning Pad 100M 0.25 37.0 12,000 12,014 286 289 3,000 3,000 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.157-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37.0 1,700 1,698 40 42 1,700 1,128 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.157-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37.0 2,175 2,156 51 55 4,350 3,600 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.157-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37.0 3,400 3,427 82 92 10,200 9,817 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.157-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37.0 4,100 4,310 103 121 16,400 17,351 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.157-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37.0 4,240 4,235 101 121 19,080 19,108 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.157-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37.0 4,600 4,609 110 134 23,000 23,005 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.157-15 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37.0 4,680 4,686 112 139 25,740 25,691 1.00 0.25 1.00 0.70 30.00 2.00 2.00 0.157-16 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37.0 4,930 4,946 118 149 29,580 29,379 1.00 0.25 1.00 0.70 30.00 2.00 2.00 0.157-17 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37.0 3,400 3,430 82 105 22,100 22,343 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.157-18 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37.0 2,550 3,957 94 114 17,850 18,324 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.157-19 30# Linear Spacer and Dart Drop 37.0 2,041 2,052 49 491.00 30.00 2.00 2.00 0.158-1 30# Linear Pre-Pad 37.0 2,100 2,130 51 511.00 30.00 2.00 0.158-2 30# Hybor G-i Minifrac - Establish Fluid 37.0 2,100 3,028 72 72 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.158-3 30# Hybor G-i Displacement 37.0 13,224 11,158 266 266 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.158-4 30# Hybor G-i Minifrac - Treatment 37.0 6,300 6,267 149 149 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.158-5 30# Hybor G-i Minifrac - Flush 37.0 13,224 13,324 317 317 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.158-6 Shut-In Shut-In-8-7 Freeze Protect Prime Up Pressure Test 5.0 1,000 571 14 148-8 Shut-In Shut-In-8-9 30# Hybor G-i Establish Stable Fluid 37.0 8,400 2,017 48 48 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.158-10 30# Hybor G-i Pad 37.0 8,610 8,621 205 205 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.158-11 30# Hybor G-i Conditioning Pad 100M 0.25 37.0 12,000 12,040 287 290 3,000 3,000 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.158-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37.0 1,900 1,998 48 49 1,900 1,595 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.158-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37.0 2,375 2,370 56 61 4,750 3,935 1.00 0.25 1.00 0.55 30.00 2.00 2.00 0.158-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37.0 3,800 3,793 90 102 11,400 10,806 1.00 0.25 1.00 0.55 30.00 2.00 2.00 0.158-15 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37.0 4,570 4,566 109 128 18,280 18,027 1.00 0.25 1.00 0.55 30.00 2.00 2.00 0.158-16 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37.0 4,760 4,799 114 137 21,420 21,606 1.00 0.25 1.00 0.55 30.00 2.00 2.00 0.158-17 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37.0 5,140 5,146 123 150 25,700 25,618 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.158-18 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37.0 5,200 5,194 124 154 28,600 28,281 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.158-19 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37.0 5,550 5,570 133 168 33,300 33,439 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.158-20 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37.0 3,800 3,824 91 117 24,700 24,013 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.158-21 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37.0 2,850 4,494 107 131 19,950 22,151 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.158-22 30# Linear Spacer and Dart Drop 37.0 2,041 2,157 51 511.00 30.00 2.00 2.00 0.159-1 30# Linear Pre-Pad 37.0 2,100 2,242 53 531.00 30.00 2.00 2.00 0.159-2 30# Hybor G-i Establish Stable Fluid 37.0 2,100 2,758 66 66 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.159-3 30# Hybor G-i Pad 37.0 8,610 8,623 205 205 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.159-4 30# Hybor G-i Conditioning Pad 100M 0.25 37.0 12,000 12,037 287 290 3,000 3,000 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.159-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37.0 1,900 1,949 46 48 1,900 1,565 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.159-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37.0 2,375 2,402 57 61 4,750 4,031 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.159-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37.0 3,800 3,800 90 102 11,400 10,767 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.159-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37.0 4,570 4,592 109 129 18,280 18,159 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.159-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37.0 4,760 4,843 115 138 21,420 21,469 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.159-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37.0 5,140 5,157 123 150 25,700 25,394 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.159-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37.0 5,200 5,253 125 156 28,600 28,677 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.159-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37.0 5,550 5,546 132 167 33,300 33,186 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.159-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37.0 3,800 3,798 90 117 24,700 24,779 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.159-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37.0 2,850 4,255 101 124 19,950 21,666 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.159-15 30# Linear Spacer and Dart Drop 37.0 2,041 2,138 51 511.00 30.00 2.00 2.00 0.15Interval 6Moraine@ 20834.19 - 20838.53 ft 138.3 °FInterval 7Moraine@ 20336.33 - 20340.67 ft 138.5 °FInterval 8Moraine@ 19795.42 - 19799.76 ft 138.3 °FInterval 9Moraine@ 19337.07 - 19341.41 ft 137.9 °FConoco Phillips - 3T-613Actual Design6 CUSTOMERConoco Phillips APIBFD (lb/gal)8.48LAT 70.42061242LEASE3T-613SALES ORDEBHST (°F)139LONG-150.266098FORMATIONMoraineDATE Max Pressure (psi)8500*Exceeds 80% of burst pressure*Prop Slurry Design Clean Actual Clean Actual Clean Calculated Slurry Design Prop Calculated Prop CL-28M BC-140X2 Losurf-300D MO-67 WG-36 OPTIFLO-III OPTIFLO-II BE-6Treatment Stage Fluid Stage Proppant Conc Rate Volume Volume Volume Volume Total TotalCrosslinker Crosslinker Surfactant Buffer Gel Breaker Breaker BiocideInterval Number Description Description Description(ppg) (bpm) (gal) (gal) (bbl) (bbl) (lbs) (lbs)(gpt) (gpt) (gpt) (gpt) (ppt) (ppt) (ppt) (ppt)Liquid AdditivesDry Additives50-103-2091491012822410-1 30# Linear Pre-Pad 37.0 2,100 2,089 50 501.00 30.00 2.00 2.00 0.1510-2 30# Hybor G-i Establish Stable Fluid 37.0 2,100 2,543 61 61 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.1510-3 30# Hybor G-i Pad 37.0 8,610 8,629 205 205 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.1510-4 30# Hybor G-i Conditioning Pad 100M 0.25 37.0 12,000 12,020 286 289 3,000 3,000 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.1510-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37.0 1,900 1,908 45 47 1,900 1,439 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.1510-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37.0 2,375 2,455 58 63 4,750 4,215 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.1510-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37.0 3,800 3,796 90 102 11,400 10,967 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.1510-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37.0 4,570 4,582 109 128 18,280 18,175 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.1510-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37.0 4,760 4,773 114 137 21,420 21,531 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.1510-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37.0 5,140 5,209 124 152 25,700 26,274 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.1510-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37.0 5,200 5,201 124 154 28,600 28,358 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.1510-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37.0 5,550 5,554 132 167 33,300 32,705 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.1510-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37.0 3,800 3,819 91 117 24,700 24,594 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.1510-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37.0 2,850 4,152 99 121 19,950 20,942 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.1510-15 30# Linear Spacer and Dart Drop 37.0 2,041 2,112 50 501.00 30.00 2.00 2.00 0.1511-1 30# Linear Pre-Pad 37.0 2,100 2,193 52 521.00 30.00 2.00 0.1511-2 30# Hybor G-i Establish Stable Fluid 37.0 2,100 2,465 59 59 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.1511-3 30# Hybor G-i Pad 37.0 8,610 8,566 204 204 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.1511-4 30# Hybor G-i Conditioning Pad 100M 0.25 37.0 12,000 11,992 286 289 3,000 3,000 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.1511-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37.0 1,900 1,932 46 47 1,900 1,377 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.1511-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37.0 2,375 2,419 58 62 4,750 3,754 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.1511-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37.0 3,800 3,805 91 102 11,400 10,604 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.1511-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37.0 4,570 4,628 110 130 18,280 18,206 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.1511-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37.0 4,760 4,807 114 137 21,420 21,269 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.1511-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37.0 5,140 5,272 126 153 25,700 26,007 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.1511-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37.0 5,200 5,216 124 155 28,600 28,597 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.1511-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37.0 5,550 5,702 136 172 33,300 33,918 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.1511-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37.0 3,800 3,792 90 116 24,700 24,422 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.1511-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37.0 2,850 4,515 108 131 19,950 22,328 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.1511-15 30# Linear Spacer and Dart Drop 37.0 1,260 2,085 50 501.00 30.00 2.00 2.00 0.1512-1 30# Linear Pre-Pad 37.0 2,100 2,217 53 531.00 30.00 2.00 0.1512-2 30# Hybor G-i Establish Stable Fluid 37.0 2,100 2,490 59 59 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.1512-3 30# Hybor G-i Pad 37.0 8,610 8,566 204 204 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.1512-4 30# Hybor G-i Conditioning Pad 100M 0.25 37.0 12,000 12,067 287 291 3,000 3,000 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.1512-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37.0 1,900 1,921 46 47 1,900 1,552 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.1512-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37.0 2,375 2,371 56 61 4,750 4,171 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.1512-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37.0 3,800 3,853 92 104 11,400 11,466 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.1512-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37.0 4,570 4,620 110 130 18,280 18,921 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.1512-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37.0 4,760 4,764 113 137 21,420 22,374 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.1512-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37.0 5,140 5,121 122 150 25,700 26,337 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.1512-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37.0 5,200 5,167 123 153 28,600 28,671 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.1512-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37.0 5,550 5,538 132 167 33,300 33,220 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.1512-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37.0 3,800 3,668 87 113 24,700 23,727 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.1512-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37.0 2,850 4,390 105 125 19,950 19,071 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.1512-15 30# Linear Spacer and Dart Drop 37.0 2,041 2,096 50 501.00 30.00 2.00 2.00 0.1513-1 30# Linear Pre-Pad 37.0 2,100 2,176 52 521.00 30.00 2.00 0.1513-2 30# Hybor G-i Establish Stable Fluid 37.0 8,400 2,424 58 58 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.1513-3 30# Hybor G-i Pad 37.0 8,610 8,603 205 205 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.1513-4 30# Hybor G-i Conditioning Pad 100M 0.25 37.0 12,000 12,061 287 290 3,000 3,000 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.1513-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37.0 1,900 1,922 46 47 1,900 1,331 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.1513-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37.0 2,375 2,442 58 63 4,750 4,171 1.00 0.25 1.00 0.45 30.00 2.00 2.00 0.1513-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37.0 3,800 3,835 91 103 11,400 10,827 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1513-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37.0 4,570 4,573 109 128 18,280 17,782 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1513-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37.0 4,760 4,782 114 136 21,420 21,254 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1513-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37.0 5,140 5,141 122 149 25,700 25,464 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1513-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37.0 5,200 5,241 125 155 28,600 28,148 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1513-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37.0 5,550 5,600 133 168 33,300 32,237 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1513-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37.0 3,800 3,859 92 118 24,700 24,163 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1513-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37.0 2,850 5,016 119 145 19,950 24,354 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1513-15 30# Linear Flush 37.0 11,655 11,730 279 2791.00 30.00 2.00 2.00 0.1513-16 Freeze Protect Freeze Protect 10.0 1,470 571 14 1413-17 Shut-In Shut-In-14-1 Shut-In Shut-In-14-2 Freeze Protect Prime Up Pressure Test 5.0 1,000 571 14 1414-3 Shut-In Shut-In-14-4 30# Linear Spacer and Dart Drop 15.0 2,100 1,043 25 251.00 30.00 2.00 2.00 0.1514-5 30# Linear Displacement 20.0 11,337 10,797 257 2571.00 30.00 2.00 2.00 0.1514-6 30# Linear DFIT 10.0 1,680 1,676 40 401.00 30.00 2.00 2.00 0.1514-7 Shut-In Shut-In-14-8 30# Hybor G-i Establish Stable Fluid 20.0 8,400 1,852 44 44 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1514-9 30# Hybor G-i Pad 37.0 8,610 8,613 205 205 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1514-10 30# Hybor G-i Conditioning Pad 100M 0.25 37.0 12,000 12,203 291 294 3,000 3,000 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1514-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37.0 1,900 1,926 46 48 1,900 1,605 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1514-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37.0 2,375 2,374 57 61 4,750 4,188 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1514-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37.0 3,800 3,801 91 102 11,400 11,058 1.00 0.25 1.00 0.40 30.00 2.00 2.00 0.1514-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37.0 4,570 4,575 109 129 18,280 18,476 1.00 0.25 1.00 0.40 30.00 2.00 2.00 0.1514-15 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37.0 4,760 4,792 114 137 21,420 21,655 1.00 0.25 1.00 0.40 30.00 2.00 2.00 0.1514-16 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37.0 5,140 5,170 123 151 25,700 25,922 1.00 0.25 1.00 0.40 30.00 2.00 2.00 0.1514-17 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37.0 5,200 5,212 124 154 28,600 28,561 1.00 0.25 1.00 0.40 30.00 2.00 2.00 0.1514-18 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37.0 5,550 5,881 140 178 33,300 35,313 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1514-19 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37.0 3,800 3,714 88 114 24,700 23,640 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1514-20 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37.0 2,850 3,989 95 115 19,950 18,662 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1514-21 30# Linear Spacer and Dart Drop 37.0 2,041 2,051 49 491.00 30.00 2.00 2.00 0.15Interval 10Moraine@ 18837.88 - 18842.22 ft 137.9 °FInterval 11Moraine@ 18339.06 - 18343.4 ft 138.1 °FInterval 12Moraine@ 17840.76 - 17845.1 ft 138.5 °FInterval 13Moraine@ 17341.75 - 17346.09 ft 139 °FInterval 14Moraine@ 16843.15 - 16847.49 ft 138.9 °FConoco Phillips - 3T-613Actual Design7 CUSTOMERConoco Phillips APIBFD (lb/gal)8.48LAT 70.42061242LEASE3T-613SALES ORDEBHST (°F)139LONG-150.266098FORMATIONMoraineDATE Max Pressure (psi)8500*Exceeds 80% of burst pressure*Prop Slurry Design Clean Actual Clean Actual Clean Calculated Slurry Design Prop Calculated Prop CL-28M BC-140X2 Losurf-300D MO-67 WG-36 OPTIFLO-III OPTIFLO-II BE-6Treatment Stage Fluid Stage Proppant Conc Rate Volume Volume Volume Volume Total TotalCrosslinker Crosslinker Surfactant Buffer Gel Breaker Breaker BiocideInterval Number Description Description Description(ppg) (bpm) (gal) (gal) (bbl) (bbl) (lbs) (lbs)(gpt) (gpt) (gpt) (gpt) (ppt) (ppt) (ppt) (ppt)Liquid AdditivesDry Additives50-103-2091491012822415-1 30# Linear Pre-Pad 37.0 2,100 2,186 52 521.00 30.00 2.00 2.00 0.1515-2 30# Hybor G-i Establish Stable Fluid 37.0 2,100 3,217 77 77 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1515-3 30# Hybor G-i Pad 37.0 9,710 9,647 230 230 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1515-4 30# Hybor G-i Conditioning Pad 100M 0.25 37.0 12,000 12,085 288 291 3,000 3,000 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1515-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37.0 2,000 1,957 47 48 2,000 1,517 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1515-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37.0 2,500 2,547 61 65 5,000 4,351 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1515-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37.0 4,000 3,983 95 107 12,000 11,535 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1515-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37.0 4,850 4,872 116 137 19,400 19,523 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1515-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37.0 5,000 5,008 119 143 22,500 22,603 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1515-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37.0 5,410 5,471 130 159 27,050 27,467 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1515-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37.0 5,500 5,532 132 164 30,250 30,434 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1515-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37.0 5,800 5,820 139 176 34,800 35,157 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1515-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37.0 4,000 3,968 94 122 26,000 25,973 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1515-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37.0 3,000 4,848 115 140 21,000 23,301 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1515-15 30# Linear Spacer and Dart Drop 37.0 2,041 2,116 50 501.00 30.00 2.00 2.00 0.1516-1 30# Linear Pre-Pad 37.0 2,100 2,153 51 511.00 30.00 2.00 0.1516-2 30# Hybor G-i Establish Stable Fluid 37.0 2,100 3,887 93 93 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1516-3 30# Hybor G-i Pad 37.0 9,710 9,726 232 232 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1516-4 30# Hybor G-i Conditioning Pad 100M 0.25 37.0 12,000 11,927 284 287 3,000 3,000 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1516-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37.0 2,000 2,019 48 50 2,000 1,575 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1516-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37.0 2,500 2,497 59 64 5,000 4,187 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1516-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37.0 4,000 3,997 95 107 12,000 11,470 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1516-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37.0 4,850 4,898 117 137 19,400 19,333 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1516-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37.0 5,000 5,010 119 143 22,500 22,745 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1516-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37.0 5,410 5,410 129 158 27,050 27,032 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1516-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37.0 5,500 5,569 133 165 30,250 30,451 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1516-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37.0 5,800 5,803 138 175 34,800 34,983 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1516-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37.0 4,000 4,041 96 124 26,000 26,340 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1516-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37.0 3,000 4,639 110 132 21,000 20,585 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1516-15 30# Linear Spacer and Dart Drop 37.0 2,041 2,054 49 491.00 30.00 2.00 2.00 0.1517-1 30# Linear Pre-Pad 37.0 2,100 2,189 52 521.00 30.00 2.00 0.1517-2 30# Hybor G-i Establish Stable Fluid 37.0 2,100 3,118 74 74 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1517-3 30# Hybor G-i Pad 37.0 9,710 9,800 233 233 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1517-4 30# Hybor G-i Conditioning Pad 100M 0.25 37.0 12,000 11,988 285 289 3,000 3,000 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1517-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37.0 2,000 2,055 49 51 2,000 1,501 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1517-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37.0 2,500 2,551 61 65 5,000 4,282 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1517-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37.0 4,000 4,005 95 107 12,000 11,398 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1517-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37.0 4,850 4,851 116 136 19,400 19,450 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1517-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37.0 5,000 5,021 120 143 22,500 22,073 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1517-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37.0 5,410 5,429 129 158 27,050 27,009 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1517-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37.0 5,500 5,510 131 163 30,250 29,809 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1517-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37.0 5,800 5,810 138 174 34,800 34,005 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1517-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37.0 4,000 4,092 97 125 26,000 26,037 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1517-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37.0 3,000 4,832 115 140 21,000 23,128 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1517-15 30# Linear Spacer and Dart Drop 37.0 2,041 2,168 52 521.00 30.00 2.00 2.00 0.1518-1 30# Linear Displacement 20.0 11,337 9,883 235 2351.00 30.00 2.00 2.00 0.1518-2 30# Linear DFIT 10.0 1,680 1,658 39 391.00 30.00 2.00 2.00 0.1518-3 30# Hybor G-i Establish Stable Fluid 37.0 2,100 2,095 50 50 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1518-4 30# Hybor G-i Pad 37.0 9,710 9,688 231 231 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1518-5 30# Hybor G-i Conditioning Pad 100M 0.25 37.0 12,000 11,931 284 287 3,000 3,000 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1518-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37.0 2,000 2,010 48 50 2,000 1,666 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1518-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37.0 2,500 2,884 69 74 5,000 5,204 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1518-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37.0 4,000 4,084 97 110 12,000 11,993 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1518-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37.0 4,850 5,610 134 158 19,400 22,958 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1518-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37.0 5,000 4,271 102 122 22,500 19,275 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1518-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37.0 5,410 5,416 129 158 27,050 26,887 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1518-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37.0 5,500 5,486 131 162 30,250 29,663 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1518-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37.0 5,800 5,797 138 175 34,800 34,629 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1518-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37.0 4,000 3,992 95 122 26,000 25,692 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1518-15 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37.0 3,000 4,460 106 128 21,000 20,966 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1518-16 30# Linear Spacer and Dart Drop 37.0 2,041 2,064 49 491.00 30.00 2.00 2.00 0.1519-1 30# Linear Pre-Pad 37.0 2,100 2,248 54 541.00 30.00 2.00 2.00 0.1519-2 30# Hybor G-i Establish Stable Fluid 37.0 2,100 3,336 79 79 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1519-3 30# Hybor G-i Pad 37.0 9,710 9,741 232 232 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1519-4 30# Hybor G-i Conditioning Pad 100M 0.25 37.0 12,000 12,016 286 289 3,000 3,000 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1519-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37.0 2,000 2,045 49 50 2,000 1,678 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1519-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37.0 2,500 2,529 60 65 5,000 4,060 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1519-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37.0 4,000 4,006 95 108 12,000 11,567 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1519-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37.0 4,850 4,859 116 136 19,400 19,360 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1519-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37.0 5,000 5,007 119 143 22,500 22,504 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1519-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37.0 5,410 5,393 128 157 27,050 26,569 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1519-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37.0 5,500 5,500 131 163 30,250 29,783 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1519-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37.0 5,800 5,816 138 175 34,800 34,544 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1519-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37.0 4,000 3,994 95 122 26,000 25,615 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1519-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37.0 3,000 4,773 114 138 21,000 22,895 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1519-15 30# Linear Flush 37.0 9,747 9,844 234 2341.00 30.00 2.00 2.00 0.1519-16 Freeze Protect Freeze Protect 10.0 1,470 571 14 1419-17 Shut-In Shut-In-Interval 17Moraine@ 15352.19 - 15356.53 ft 138.5 °FInterval 16Moraine@ 15850.53 - 15854.87 ft 138.7 °FInterval 18Moraine@ 14854.27 - 14858.61 ft 138.3 °FInterval 19Moraine@ 14356.39 - 14360.73 ft 138.1 °FInterval 15Moraine@ 16349.44 - 16353.78 ft 138.9 °FConoco Phillips - 3T-613Actual Design8 CUSTOMERConoco Phillips APIBFD (lb/gal)8.48LAT 70.42061242LEASE3T-613SALES ORDEBHST (°F)139LONG-150.266098FORMATIONMoraineDATE Max Pressure (psi)8500*Exceeds 80% of burst pressure*Prop Slurry Design Clean Actual Clean Actual Clean Calculated Slurry Design Prop Calculated Prop CL-28M BC-140X2 Losurf-300D MO-67 WG-36 OPTIFLO-III OPTIFLO-II BE-6Treatment Stage Fluid Stage Proppant Conc Rate Volume Volume Volume Volume Total TotalCrosslinker Crosslinker Surfactant Buffer Gel Breaker Breaker BiocideInterval Number Description Description Description(ppg) (bpm) (gal) (gal) (bbl) (bbl) (lbs) (lbs)(gpt) (gpt) (gpt) (gpt) (ppt) (ppt) (ppt) (ppt)Liquid AdditivesDry Additives50-103-2091491012822420-1 Shut-In Shut-In-20-2 Freeze Protect Prime Up Pressure Test 5.0 1,000 571 14 1420-3 Shut-In Shut-In-20-4 30# Linear Spacer and Dart Drop 15.0 1,260 876 21 211.00 30.00 2.00 2.00 0.1520-5 30# Linear Displacement 15.0 8,859 8,731 208 2081.00 30.00 2.00 2.00 0.1520-6 30# Hybor G-i Minifrac - Establish Fluid 15.0 8,400 4,566 109 109 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1520-7 30# Hybor G-i Minifrac - Treatment 37.0 16,500 16,491 393 393 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1520-8 30# Linear Minifrac - Flush 37.0 9,430 9,481 226 2261.00 30.00 2.00 2.00 0.1520-9 Shut-In Shut-In-20-10 30# Hybor G-i Establish Stable Fluid 37.0 8,400 3,402 81 81 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1520-11 30# Hybor G-i Pad 37.0 21,000 20,921 498 498 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1520-12 30# Hybor G-i Conditioning Pad 100M 0.25 37.0 12,000 12,020 286 289 3,000 3,000 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1520-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37.0 12,000 12,016 286 297 12,000 10,478 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1520-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37.0 16,000 16,003 381 413 32,000 30,540 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1520-15 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37.0 16,000 15,949 380 430 48,000 47,213 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1520-16 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37.0 10,000 9,999 238 280 40,000 39,744 1.00 0.25 1.00 0.35 30.00 2.00 2.00 0.1520-17 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37.0 8,000 8,187 195 234 36,000 36,663 1.00 0.25 1.00 0.30 30.00 2.00 2.00 0.1520-18 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37.0 6,400 8,601 205 242 32,000 35,361 1.00 0.25 1.00 0.30 30.00 2.00 2.00 0.1520-19 30# Linear Spacer and Dart Drop 37.0 1,260 2,125 51 511.00 30.00 2.00 2.00 0.1521-1 30# Linear Pre-Pad 37.0 2,100 2,213 53 531.00 30.00 2.00 0.1521-2 30# Hybor G-i Minifrac - Establish Fluid 37.0 2,100 3,300 79 79 1.00 0.25 1.00 0.30 30.00 2.00 2.00 0.1521-3 30# Hybor G-i Minifrac - Treatment 37.0 4,110 8,433 201 201 1.00 0.25 1.00 0.30 30.00 2.00 2.00 0.1521-4 30# Linear Minifrac - Flush 37.0 8,540 9,204 219 2191.00 30.00 2.00 2.00 0.1521-5 Shut-In Shut-In-21-6 30# Hybor G-i Establish Stable Fluid 37.0 2,100 1,287 31 31 1.00 0.25 1.00 0.30 30.00 2.00 2.00 0.1521-7 30# Hybor G-i Pad 37.0 2,220 2,234 53 53 1.00 0.25 1.00 0.30 30.00 2.00 2.00 0.1521-8 30# Hybor G-i Conditioning Pad Wanli 16/20 Ceramic 0.25 37.0 6,000 5,962 142 143 1,500 926 1.00 0.25 1.00 0.30 30.00 2.00 2.00 0.1521-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37.0 3,000 3,010 72 74 3,000 2,540 1.00 0.25 1.00 0.30 30.00 2.00 2.00 0.1521-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37.0 4,000 4,007 95 103 8,000 7,432 1.00 0.25 1.00 0.30 30.00 2.00 2.00 0.1521-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37.0 4,000 4,009 95 108 12,000 11,903 1.00 0.25 1.00 0.30 30.00 2.00 2.00 0.1521-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37.0 2,500 2,492 59 70 10,000 10,019 1.00 0.25 1.00 0.30 30.00 2.00 2.00 0.1521-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37.0 2,000 2,010 48 58 9,000 9,091 1.00 0.25 1.00 0.30 30.00 2.00 2.00 0.1521-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37.0 1,600 4,978 119 136 8,000 16,285 1.00 0.25 1.00 0.30 30.00 2.00 2.00 0.1521-15 30# Linear Flush 37.0 9,111 9,125 217 2171.00 30.00 2.00 2.00 0.1521-16 Shut-In Shut-In-1,792,660 1,821,719 43,374 47,461 3,844,700 3,846,846Design Total (gal)Actual Total (gal)Design Total (lbs)Calculated Total (lbs)Ticket Total (lbs)CL-28M BC-140X2 Losurf-300D MO-67 WG-36 OPTIFLO-III OPTIFLO-II BE-6- - 3,781,700 3,783,846 3,743,524(gal) (gal) (gal) (gal) (lbs) (lbs) (lbs) (lbs)220,805 215,971 63,000 63,000 63,000 Initial Design Material Volume 1,560.0 390.0 1,780.8 1,032.2 53,423.4 3,561.6 3,561.6 267.1- - - Actual Design Material Volume 1,599.1 399.8 1,815.1 855.7 54,453.3 3,630.2 3,591.1 272.311,880 6,609 - - - Physical Material Volume Pumped 1,655 391 1890 879 53776 3,661 3,636 2751,559,975 1,599,139 - - - Physical Material Volume Deviance 3% -2% 4% 3% -1% 1% 1% 1%--** IFS numbers for proppant are taken from software calculations based on multiple variablesMicroMotion Volume Pumped 1,615 406 1,855 872 55,797 3,651 3,648 ---** Proppant is billed from Weight Ticket volumesMicroMotion Volume Deviance 1% 2% 2% 2% 2% 1% 2% ------Interval 20Moraine@ 13859.35 - 13863.69 ft 138.1 °FInterval 21Moraine@ 13361.01 - 13365.35 ft 137.9 °F-Fluid Type-30# LinearSeawaterFreeze Protect30# Hybor G-iProppant TypeWanli 16/20 Ceramic100M--Conoco Phillips - 3T-613Actual Design9 Conoco Phillips Moraine3T-61350-103-20914*Exceeds 80% of burst pressure*Description OD (in) ID (in) Wt (#)MD Top (ft)MD Btm (ft) Volume (gal)Tubular Burst Pressure (psi)Tubing4.5 3.958 12.6 0 8,148 5,208 8,430Tubing4.5 3.958 12.6 8,148 22,000 8,854 8,430Total22,00014,0621.55139.01.55139.0Top MD (ft)Btm MD (ft)Average TVD (ft)Interval # Formation DescriptorAverage Interval Temperature (F)Ball Drop Time (HH:MM)Ball Hit Time (HH:MM)JSV Drop (bbl)JSV Slow Down (bbl)JSV Hit (bbl)Early (bbl)Surface Seat Pressure (psi)Surface Peak Pressure (psi)Surface Differential (psi)BH Seat Pressure (psi)BH Peak Pressure (psi)BH Differential (psi)Rate at Shift (bpm)23,27723,281 4,9871Moraine137.3N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A22,819 22,823 4,9972Moraine137.412:12:13 PM 12:21:46 PM 2,727 3,0243,05519.33,147 6,471 3,324 4,263 7,458 3,195 15.122,325 22,329 5,0063Moraine137.69:48:52 AM 10:00:25 AM 27 317 3606.82,924 4,173 1,249 4,048 5,306 1,258 15.121,83021,8345,0174Moraine137.811:42:03 AM 11:51:43 AM 3,052 3,3343,36618.23,158 6,484 3,326 4,336 7,572 3,236 14.721,332 21,3365,0305Moraine138.012:40:17 PM 12:49:30 PM 5,105 5,3805,41019.62,829 5,889 3,060 4,035 6,723 2,688 15.120,83420,839 5,0536Moraine138.31:29:36 PM 1:38:49 PM 6,8307,097 7,12918.12,652 6,223 3,571 3,954 7,115 3,161 15.020,33620,341 5,0647Moraine138.55:08:18 PM 5:18:54 PM 22 281 31912.52,740 5,825 3,085 3,883 6,437 2,554 15.119,795 19,8005,0508Moraine138.36:00:18 PM 6:09:27 PM 1,709 1,9601,99119.32,869 6,191 3,322 3,916 7,136 3,220 15.119,33719,341 5,0259Moraine137.910:54:12 AM 11:02:58 AM 1,7962,0402,07911.32,661 5,916 3,255 3,856 7,142 3,286 15.518,83818,842 5,02310Moraine137.911:47:00 AM 11:55:33 AM 3,662 3,899 3,93612.72,412 5,609 3,197 3,724 7,019 3,295 15.718,339 18,343 5,04111Moraine138.112:39:22 PM 12:47:47 PM 5,513 5,742 5,78210.12,509 5,633 3,124 3,772 6,700 2,928 15.517,841 17,845 5,06712Moraine138.51:32:21 PM 1:40:32 PM 7,378 7,6007,63811.52,394 5,031 2,637 3,691 6,602 2,911 15.517,342 17,3465,09613Moraine139.02:24:37 PM 2:32:43 PM 9,2309,4449,4867.92,302 5,220 2,918 3,672 6,616 2,944 15.916,843 16,8475,09114Moraine138.99:33:03 AM 9:46:08 AM 15 221 26011.31,934 4,652 2,718 3,660 6,229 2,569 15.316,349 16,3545,08915Moraine138.911:39:11 AM 11:46:52 AM 2,108 2,307 2,34610.82,554 5,865 3,311 3,782 6,514 2,732 15.315,851 15,855 5,07516Moraine138.712:34:46 PM 12:42:19 PM 4,078 4,269 4,3118.22,379 5,015 2,636 3,711 6,502 2,791 15.515,352 15,3575,06517Moraine138.51:30:41 PM 1:38:01 PM 6,0546,238 6,2789.62,415 5,541 3,126 3,643 6,295 2,652 15.314,85414,859 5,04918Moraine138.32:26:15 PM 2:33:17 PM 8,0248,2008,2419.11,855 5,572 3,717 3,594 6,761 3,167 15.614,35614,361 5,03919Moraine138.14:03:58 PM 4:11:00 PM 10,182 10,35010,3928.52,316 5,354 3,038 3,638 6,196 2,558 15.213,859 13,8645,04020Moraine138.19:17:35 AM 9:27:10 AM 16 177 21412.91,794 4,668 2,874 3,495 6,136 2,641 15.413,361 13,365 5,02921Moraine137.91:25:12 PM 1:32:04 PM 3,778 3,931 3,9783.32,322 5,449 3,127 3,625 6,248 2,623 15.29,8139,4959,1778,8598,54011,40411,08510,76610,45110,13212,99912,65312,36012,04111,72214,27013,95313,63513,317Displacement to Top Sleeve/Perf (gal)14,87914,586Interval #1Max Pressure (psi)8,500Isolation TypeCemented LinerTreatment TubularsCustomerFormationLeaseAPIDateTemperature DataTemp. Gradient (°F/100 ft)BHST (°F)Directional Data5,0372,23722,000Directional Data2,2376/16/2025KOPTemperature DataSleeve/Perf DepthSleeves78910112345617181920211213141516Temp. Gradient (°F/100 ft)BHST (°F)TVD at Bottom PerfMD at Bottom Perf5,09623,281KOPAvg. TVDTotal MDConoco Phillips - 3T-613 Wellbore Information1 6/16/25 9:40 6/16/25 12:12 152 min N/A bpm N/A psi N/A psi 38.7 bpm 5,893 psi 6,206 psi 36.0 bpm 4,055 psi 4,074 psi 5,542 psi 3,579 hhp 537 psi 18 psi 765 psi 5.00 ppg 6 5 30 % 29 % 26 cP 94.5 F 9.2 DFIT 10.400 bpm 2670 psi 4341 psi 10.4 bpm 2777 psi 4464 psi 3235 psi 0.649 psi/ft 166,232 lbs 3,000 lbs 169,232 lbs 169,232 lbs Pad Percentage Actual Wanli 16/20 Ceramic Pumped: Diagnostic method Average Missile Pressure: Minifrac Max Rate: Open Well Pressure: Initial OA Pressure: Average Missile HHP: Initial BH Pressure (Breakdown): Average BH Pressure: Pumps Ending Stage: Max Proppant Concentration: Pump Time: ISDP: Final Fracture Gradient: Minifrac Max Surface Pressure: 100M Pumped: Proppant in Formation: Minifrac Max DH Pressure: Average pH: Minifrac Average Rate: Proppant Summary Minifrac Average Pressure: Minifrac Average DH Pressure: Average Visc: Average Temp: Initial Rate (Breakdown): Initial Surface Pressure (Breakdown): Max Rate: Max Surface Pressure: Max BH Pressure: Interval Summary 3T-613 - Moraine - Interval 1 Interval Summary Start Date/Time: End Date/Time: Average Surface Pressure: Average Rate: Max OA Pressure: Pumps Starting Stage: Pad Percentage Design Total Proppant Pumped* : Conoco Phillips - 3T-613 Interval Summary 11 15,488 gal 369 bbls 571 gal 14 bbls 91,374 gal 2,176 bbls 571 gal 14 bbls 859 gal 20 bbls 16,096 gal 383 bbls 12,016 gal 286 bbls 61,198 gal 1,457 bbls 2,324 gal 55 bbls 9,565 gal 228 bbls 2,064 gal 49 bbls 2,740 gal 65 bbls 114,984 gal 2,738 bbls 107,433 gal 2,558 bbls Completed Comments: Engineer: Treater: Supervisor: Customer Engineer: Customer Rep: Conditioning Pad Volume: Proppant Laden Fluid Volume: Pre-Pad Volume: Pad Volume: 30# Linear Volume: A DFIT was pumped and closure pressure was determined to be 3142 psi. During the stage pump 670 shut off three times causing rate to drop; Pump 177 had a preload issue causing rate to drop. During 4ppg, there was an issues getting one of the gates on bin 2 to open causing a dip in concentration; a different bin was swapped to and concentration recovered. DFIT Volume: Freeze Protect Volume: Allen Eschete Dan Faur Steven Sanders Treatment Slurry Volume (Calculated): Total Clean Fluid Volume: Prime Up Pressure Test Fluid Summary (by fluid description) Fluid Summary (by stage description) 30# Hybor G-i Volume: Establish Stable Fluid Volume: *Values for proppant are taken from software calculations based on multiple variables. Proppant is billed off of weight ticket volumes and may vary slightly from this number. Step Rate Test Volume: Spacer and Dart Drop Volume: Interval Status: Craig Karpinski James Campbell Conoco Phillips - 3T-613 Interval Summary 12 6/16/25 12:12 6/16/25 18:08 356 min 15.1 bpm 6,471 psi 7,458 psi 19 bbl 37.6 bpm 5,688 psi 6,041 psi 35.9 bpm 4,962 psi 4,969 psi 5,530 psi 4,366 hhp 1059 psi 760 psi 774 psi 5.50 ppg 5 6 42 % 41 % 26 cP 94.6 F 9.2 3725 psi 0.746 psi/ft 3553 psi 3533 psi 3519 psi 183,652 lbs 6,000 lbs 189,652 lbs 189,652 lbs Pad Percentage Design Pad Percentage Actual ISDP: Final Fracture Gradient: Final 5 min: Final 10 min: Proppant in Formation: Interval Summary Start Date/Time: End Date/Time: Pump Time: Initial Rate (Breakdown): Initial Surface Pressure (Breakdown): Initial BH Pressure (Breakdown): Dart/Ball Early : Max Rate: Max Surface Pressure: Max BH Pressure: Average Rate: Average Missile Pressure: Average Surface Pressure: 3T-613 - Moraine - Interval 2 Average BH Pressure: Average Missile HHP: Open Well Pressure: Initial OA Pressure: Max OA Pressure: Max Proppant Concentration: Pumps Starting Stage: Pumps Ending Stage: Average Visc: Average Temp: Average pH: Final 15 min: Proppant Summary Wanli 16/20 Ceramic Pumped: 100M Pumped: Total Proppant Pumped* : Conoco Phillips - 3T-613 Interval Summary 13 32,683 gal 778 bbls 1,470 gal 35 bbls 139,159 gal 3,313 bbls 2,120 gal 50 bbls 31,446 gal 749 bbls 24,220 gal 577 bbls 73,072 gal 1,740 bbls 30,563 gal 728 bbls 1,470 gal 35 bbls 10,421 gal 248 bbls 181,776 gal 4,328 bbls 173,312 gal 4,126 bbls Completed Comments: Engineer: Treater: Supervisor: Customer Engineer: Customer Rep: Pad Volume: Pre-Pad Volume: Fluid Summary (by fluid description) Fluid Summary (by stage description) 30# Linear Volume: Freeze Protect Volume: Conditioning Pad Volume: Proppant Laden Fluid Volume: Flush Volume: Freeze Protect Volume: Establish Stable Fluid Volume: 30# Hybor G-i Volume: Interval Status: During the first attempt at the stage, pump 670 shut off, pump 621 radiator cap blew, and pump 584 shut off. With these pumps down, rate was only able to be pumped at 23 bpm, so the OSR called to flush the well. Pump 670 was swapped out, pump 177 had valves changed, and pump 584 was fueled up. The stage was resumed with 6 pumps. *Values for proppant are taken from software calculations based on multiple variables. Proppant is billed off of weight ticket volumes and may vary slightly from this number.Dan Faur Treatment Slurry Volume (Calculated): Total Clean Fluid Volume: Steven Sanders Craig Karpinski James Campbell Allen Eschete Conoco Phillips - 3T-613 Interval Summary 14 6/17/25 9:45 6/17/25 11:42 116 min 15.1 bpm 4,173 psi 5,306 psi 7 bbl 37.8 bpm 6,119 psi 6,939 psi 26.5 bpm 5,278 psi 5,146 psi 5,944 psi 3,428 hhp 693 psi 497 psi 750 psi 5.00 ppg 6 6 30 % 45 % 27 cP 97.4 F 9.2 169,757 lbs 3,000 lbs 172,757 lbs 172,757 lbs Proppant Summary Wanli 16/20 Ceramic Pumped: Interval Summary Average Missile HHP: Average Temp: Average Missile Pressure: Average Surface Pressure: Average BH Pressure: Pumps Starting Stage: Pumps Ending Stage: Average pH: 100M Pumped: Max OA Pressure: Max Proppant Concentration: Open Well Pressure: Pad Percentage Design Pad Percentage Actual Average Visc: Initial OA Pressure: Initial Surface Pressure (Breakdown): Start Date/Time: 3T-613 - Moraine - Interval 3 End Date/Time: Max BH Pressure: Average Rate: Initial BH Pressure (Breakdown): Dart/Ball Early : Max Rate: Max Surface Pressure: Pump Time: Initial Rate (Breakdown): Total Proppant Pumped* : Proppant in Formation: Conoco Phillips - 3T-613 Interval Summary 15 5,800 gal 138 bbls 571 gal 14 bbls 114,475 gal 2,726 bbls 571 gal 14 bbls 2,069 gal 49 bbls 23,142 gal 551 bbls 30,373 gal 723 bbls 57,614 gal 1,372 bbls 3,731 gal 89 bbls 3,346 gal 80 bbls 128,554 gal 3,061 bbls 120,846 gal 2,877 bbls Completed Comments: Engineer: Treater: Supervisor: Customer Engineer: Customer Rep: Spacer and Dart Drop Volume: Pad Volume: Total Clean Fluid Volume: 30# Linear Volume: 30# Hybor G-i Volume: Freeze Protect Volume: Fluid Summary (by stage description) Pre-Pad Volume: Conditioning Pad Volume: Establish Stable Fluid Volume: Steven Sanders Craig Karpinski James Campbell Treatment Slurry Volume (Calculated): Interval Status: Due to high pressure after the dart seat, the pad was extended. The 100 mesh sand scour was then run and the stage was extended until the scour reached the formation. Pressure then started to trend down the job continued as per the design. *Values for proppant are taken from software calculations based on multiple variables. Proppant is billed off of weight ticket volumes and may vary slightly from this number. Fluid Summary (by fluid description) Proppant Laden Fluid Volume: Prime Up Pressure Test Allen Eschete Dan Faur Conoco Phillips - 3T-613 Interval Summary 16 6/17/25 11:42 6/17/25 12:40 59 min 14.7 bpm 6,484 psi 7,572 psi 18 bbl 37.3 bpm 6,498 psi 6,583 psi 36.1 bpm 5,377 psi 5,240 psi 5,647 psi 4,758 hhp 749 psi 762 psi 6.64 ppg 6 ppg 6 ppg 30 % 29 % 27 cP 97.4 F 9.28 171,116 lbs 3,000 lbs 174,116 lbs 174,116 lbs Initial Rate (Breakdown): Proppant in Formation: Max Surface Pressure: Average Rate: Average Missile Pressure: Average BH Pressure: Average Missile HHP: Pumps Ending Stage: Pad Percentage Actual Initial BH Pressure (Breakdown): Dart/Ball Early : Max Rate: Interval Summary Start Date/Time: Initial Surface Pressure (Breakdown): End Date/Time: Pump Time: 3T-613 - Moraine - Interval 4 Max BH Pressure: Proppant Summary Wanli 16/20 Ceramic Pumped: Total Proppant Pumped* : Pad Percentage Design Average Surface Pressure: Pumps Starting Stage: 100M Pumped: Max OA Pressure: Max Proppant Concentration: Average Visc: Average Temp: Average pH: Initial OA Pressure: Conoco Phillips - 3T-613 Interval Summary 17 4,774 gal 114 bbls 73,847 gal 1,758 bbls 2,114 gal 50 bbls 10,801 gal 257 bbls 12,064 gal 287 bbls 47,700 gal 1,136 bbls 2,660 gal 63 bbls 3,282 gal 78 bbls 86,390 gal 2,057 bbls 78,621 gal 1,872 bbls Completed Comments: Engineer: Treater: Supervisor: Customer Engineer: Customer Rep: Spacer and Dart Drop Volume: Fluid Summary (by fluid description) *Values for proppant are taken from software calculations based on multiple variables. Proppant is billed off of weight ticket volumes and may vary slightly from this number. 30# Hybor G-i Volume: 30# Linear Volume: Interval completed as per design. James Campbell Pre-Pad Volume: Pad Volume: Conditioning Pad Volume: Treatment Slurry Volume (Calculated): Proppant Laden Fluid Volume: Fluid Summary (by stage description) Establish Stable Fluid Volume: Total Clean Fluid Volume: Interval Status: Allen Eschete Dan Faur Steven Sanders Craig Karpinski Conoco Phillips - 3T-613 Interval Summary 18 6/17/25 12:40 6/17/25 13:29 49 min 15.1 bpm 5,889 psi 6,723 psi 20 bbl 37.2 bpm 6,983 psi 6,832 psi 35.9 bpm 5,744 psi 5,604 psi 5,849 psi 5,054 hhp 715 psi 727 psi 7.20 ppg 6 6 30 % 30 % 27 cP 96.17 F 9.28 170,488 lbs 3,000 lbs 173,488 lbs 173,488 lbs Total Proppant Pumped* : Initial Rate (Breakdown): Average Missile Pressure: Max OA Pressure: Initial BH Pressure (Breakdown): Dart/Ball Early : Average Temp: Initial Surface Pressure (Breakdown): Max Rate: Pumps Starting Stage: Pumps Ending Stage: Pump Time: Average pH: Pad Percentage Actual 3T-613 - Moraine - Interval 5 Average BH Pressure: Initial OA Pressure: Max Proppant Concentration: Start Date/Time: Pad Percentage Design Average Rate: Proppant in Formation: Average Missile HHP: Average Visc: Max Surface Pressure: Interval Summary Proppant Summary Wanli 16/20 Ceramic Pumped: 100M Pumped: End Date/Time: Max BH Pressure: Average Surface Pressure: Conoco Phillips - 3T-613 Interval Summary 19 4,377 gal 104 bbls 59,532 gal 1,417 bbls 2,275 gal 54 bbls 6,602 gal 157 bbls 12,023 gal 286 bbls 37,194 gal 886 bbls 2,102 gal 50 bbls 3,713 gal 88 bbls 71,650 gal 1,706 bbls 63,909 gal 1,522 bbls Completed Comments: Engineer: Treater: Supervisor: Customer Engineer: Customer Rep: Pre-Pad Volume: Proppant Laden Fluid Volume: Interval Status: Establish Stable Fluid Volume: Spacer and Dart Drop Volume: Craig Karpinski Interval completed as per design. Total Clean Fluid Volume: Allen Eschete Dan Faur James Campbell *Values for proppant are taken from software calculations based on multiple variables. Proppant is billed off of weight ticket volumes and may vary slightly from this number. Pad Volume: 30# Hybor G-i Volume: Steven Sanders Fluid Summary (by fluid description) Fluid Summary (by stage description) Treatment Slurry Volume (Calculated): Conditioning Pad Volume: 30# Linear Volume: Conoco Phillips - 3T-613 Interval Summary 20 6/17/25 13:29 6/17/25 14:27 57 min 15.0 bpm 6,223 psi 7,115 psi 18 bbl 37.4 bpm 6,174 psi 6,206 psi 36.4 bpm 5,255 psi 5,114 psi 5,527 psi 4,688 hhp 708 psi 727 psi 6.90 ppg 6 6 30 % 29 % 28 cP 94.58 F 9.3 3367 psi 0.666 psi/ft 3420 psi 3403 psi 3390 psi 170,731 lbs 3,000 lbs 173,731 lbs 173,731 lbs Start Date/Time: Max Proppant Concentration: Pad Percentage Actual Initial OA Pressure: Max OA Pressure: End Date/Time: Max Surface Pressure: Max BH Pressure: Wanli 16/20 Ceramic Pumped: Pad Percentage Design Average Temp: Total Proppant Pumped* : Final Fracture Gradient: Initial Surface Pressure (Breakdown): Initial BH Pressure (Breakdown): Dart/Ball Early : Final 15 min: Average Surface Pressure: Average BH Pressure: 100M Pumped: Pumps Ending Stage: Average Visc: Proppant in Formation: 3T-613 - Moraine - Interval 6 Interval Summary Average pH: Final 5 min: Final 10 min: Proppant Summary Pumps Starting Stage: Max Rate: Average Missile Pressure: ISDP: Average Rate: Pump Time: Initial Rate (Breakdown): Average Missile HHP: Conoco Phillips - 3T-613 Interval Summary 21 16,148 gal 384 bbls 571 gal 14 bbls 61,286 gal 1,459 bbls 2,165 gal 52 bbls 6,442 gal 153 bbls 11,996 gal 286 bbls 38,048 gal 906 bbls 13,983 gal 333 bbls 571 gal 14 bbls 4,800 gal 114 bbls 85,756 gal 2,042 bbls 78,005 gal 1,857 bbls Completed Comments: Engineer: Treater: Supervisor: Customer Engineer: Customer Rep: Total Clean Fluid Volume: 30# Linear Volume: Proppant Laden Fluid Volume: Freeze Protect Volume: 30# Hybor G-i Volume: Flush Volume: Pad Volume: Interval completed as per design.Steven Sanders Craig Karpinski James Campbell *Values for proppant are taken from software calculations based on multiple variables. Proppant is billed off of weight ticket volumes and may vary slightly from this number. Allen Eschete Dan Faur Pre-Pad Volume: Conditioning Pad Volume: Interval Status: Treatment Slurry Volume (Calculated): Fluid Summary (by fluid description) Fluid Summary (by stage description) Establish Stable Fluid Volume: Freeze Protect Volume: Conoco Phillips - 3T-613 Interval Summary 22 6/18/25 17:05 6/18/25 18:00 55 min 15.1 bpm 5,825 psi 6,437 psi 12 bbl 37.3 bpm 6,532 psi 6,238 psi 34.4 bpm 5,730 psi 5,739 psi 5,829 psi 4,831 hhp 1016 psi 488 psi 704 psi 7.19 ppg 6 4 30 % 29 % 29 cP 92.2 F 9.4 169,746 lbs 3,000 lbs 172,746 lbs 172,746 lbs Average Temp: Average Missile HHP: 3T-613 - Moraine - Interval 7 End Date/Time: Total Proppant Pumped* : Average BH Pressure: Average Surface Pressure: Wanli 16/20 Ceramic Pumped: Average Visc: Max Surface Pressure: Max BH Pressure: Average Rate: Average Missile Pressure: Initial Rate (Breakdown): Initial Surface Pressure (Breakdown): Max OA Pressure: Proppant in Formation: Dart/Ball Early : Pad Percentage Actual Initial OA Pressure: Pad Percentage Design Pumps Starting Stage: Proppant Summary Open Well Pressure: Pumps Ending Stage: 100M Pumped: Average pH: Max Proppant Concentration: Pump Time: Max Rate: Initial BH Pressure (Breakdown): Start Date/Time: Interval Summary Conoco Phillips - 3T-613 Interval Summary 23 5,451 gal 130 bbls 571 gal 14 bbls 58,299 gal 1,388 bbls 571 gal 14 bbls 2,108 gal 50 bbls 6,444 gal 153 bbls 12,014 gal 286 bbls 37,454 gal 892 bbls 3,343 gal 80 bbls 2,387 gal 57 bbls 72,028 gal 1,715 bbls 64,321 gal 1,531 bbls Completed Comments: Engineer: Treater: Supervisor: Customer Engineer: Customer Rep: Conditioning Pad Volume: *Values for proppant are taken from software calculations based on multiple variables. Proppant is billed off of weight ticket volumes and may vary slightly from this number. Proppant Laden Fluid Volume: Pre-Pad Volume: Pad Volume: 30# Hybor G-i Volume: Treatment Slurry Volume (Calculated): Total Clean Fluid Volume: Interval Status: During the interval, pump 621 and pump 670 shut off due to intake issues. The remainder of the interval was completed as per design. Fluid Summary (by fluid description) Allen Eschete Dan Faur Prime Up Pressure Test Establish Stable Fluid Volume: Freeze Protect Volume: Steven Sanders James Campbell Fluid Summary (by stage description) Craig Karpinski 30# Linear Volume: Spacer and Dart Drop Volume: Conoco Phillips - 3T-613 Interval Summary 24 6/18/25 18:00 6/19/25 10:54 1014 min 15.1 bpm 6,191 psi 7,136 psi 19 bbl 37.9 bpm 5,733 psi 5,826 psi 35.2 bpm 4,976 psi 4,961 psi 5,339 psi 4,292 hhp 956 psi 489 psi 708 psi 7.05 ppg 5 6 30 % 29 % 28 cP 93 F 9.45 Minifrac 36.000 bpm 4729 psi 5211 psi 38.2 bpm 5304 psi 5681 psi 3207 psi 0.635 psi/ft 3343 psi 3336 psi 3324 psi 189,471 lbs 3,000 lbs 192,471 lbs 192,471 lbs Minifrac Max Rate: Max BH Pressure: Dart/Ball Early : End Date/Time: Pump Time: Average Rate: Max Proppant Concentration: Average BH Pressure: Minifrac Max DH Pressure: Max OA Pressure: Open Well Pressure: Initial OA Pressure: Average Missile Pressure: Initial Rate (Breakdown): Max Surface Pressure: Pumps Ending Stage: Pumps Starting Stage: ISDP: Proppant in Formation: Final 10 min: Average Temp: Average pH: Minifrac Max Surface Pressure: Average Surface Pressure: Max Rate: Initial Surface Pressure (Breakdown): Start Date/Time: Initial BH Pressure (Breakdown): Average Visc: Total Proppant Pumped* : Final 5 min: Final Fracture Gradient: Final 15 min: Average Missile HHP: Pad Percentage Actual Pad Percentage Design Interval Summary 3T-613 - Moraine - Interval 8 Minifrac Average Pressure: Minifrac Average DH Pressure: Diagnostic method Wanli 16/20 Ceramic Pumped: 100M Pumped: Proppant Summary Minifrac Average Rate: Conoco Phillips - 3T-613 Interval Summary 25 4,287 gal 102 bbls 571 gal 14 bbls 98,209 gal 2,338 bbls 571 gal 14 bbls 2,130 gal 51 bbls 8,621 gal 205 bbls 12,040 gal 287 bbls 41,754 gal 994 bbls 11,158 gal 266 bbls 2,157 gal 51 bbls 2,017 gal 48 bbls 3,028 gal 72 bbls 6,267 gal 149 bbls 13,324 gal 317 bbls 111,654 gal 2,658 bbls 103,067 gal 2,454 bbls Completed Comments: Engineer: Treater: Supervisor: Customer Engineer: Customer Rep: Total Clean Fluid Volume: Minifrac - Flush Volume: Displacement Volume: Establish Stable Fluid Volume: Minifrac - Treatment Volume: *Values for proppant are taken from software calculations based on multiple variables. Proppant is billed off of weight ticket volumes and may vary slightly from this number. Spacer and Dart Drop Volume: Pre-Pad Volume: Minifrac - Establish Fluid Volume: Prime Up Pressure Test Fluid Summary (by fluid description) Pad Volume: 30# Linear Volume: Conditioning Pad Volume: Fluid Summary (by stage description) Interval Status: Pumps 621 and 670 had issues with overheating and had to be taken offline. Pump 579 had a leak on the suction manifold and had to be taken offline. Due to losing three pumps, the OSR called to not continue with the stage. The dart was seated and a minifrac was pumped before shutting down for the day. No closure was identified duirng the minifrac. The interval was resumed the next day and during pad, pump 579 needed to be restarted in order to turn on the fan. The interval was then completed with no further issues. Treatment Slurry Volume (Calculated): Proppant Laden Fluid Volume: Freeze Protect Volume: 30# Hybor G-i Volume: Steven Sanders Chad Burkett Craig Karpinski James Campbell Allen Eschete Conoco Phillips - 3T-613 Interval Summary 26 6/19/25 10:54 6/19/25 11:47 53 min 15.5 bpm 5,916 psi 7,142 psi 11 bbl 38.9 bpm 5,565 psi 6,246 psi 36.4 bpm 4,405 psi 4,390 psi 5,016 psi 3,930 hhp 708 psi 739 psi 7.20 ppg 6 6 30 % 29 % 26 cP 93.2 F 9.34 189,693 lbs 3,000 lbs 192,693 lbs 192,693 lbs Average BH Pressure: Average Missile HHP: Proppant in Formation: Initial OA Pressure: Average Rate: 100M Pumped: Pad Percentage Actual Interval Summary Dart/Ball Early : Average Visc: Pad Percentage Design Max OA Pressure: Total Proppant Pumped* : Max Surface Pressure: Max BH Pressure: Initial Rate (Breakdown): Max Rate: Pumps Ending Stage: Initial Surface Pressure (Breakdown): Proppant Summary Wanli 16/20 Ceramic Pumped: Average Missile Pressure: 3T-613 - Moraine - Interval 9 Initial BH Pressure (Breakdown): Average pH: Start Date/Time: End Date/Time: Pump Time: Average Temp: Max Proppant Concentration: Pumps Starting Stage: Average Surface Pressure: Conoco Phillips - 3T-613 Interval Summary 27 4,380 gal 104 bbls 65,013 gal 1,548 bbls 2,242 gal 53 bbls 8,623 gal 205 bbls 12,037 gal 287 bbls 41,595 gal 990 bbls 2,138 gal 51 bbls 2,758 gal 66 bbls 77,990 gal 1,857 bbls 69,393 gal 1,652 bbls Completed Comments: Engineer: Treater: Supervisor: Customer Engineer: Customer Rep: Total Clean Fluid Volume: Interval completed as per design. Interval Status: Pad Volume: James Campbell 30# Hybor G-i Volume: Pre-Pad Volume: Establish Stable Fluid Volume: Spacer and Dart Drop Volume: 30# Linear Volume: Conditioning Pad Volume: Proppant Laden Fluid Volume: Fluid Summary (by stage description) Fluid Summary (by fluid description) *Values for proppant are taken from software calculations based on multiple variables. Proppant is billed off of weight ticket volumes and may vary slightly from this number. Steven Sanders Craig Karpinski Treatment Slurry Volume (Calculated): Allen Eschete Chad Burkett Conoco Phillips - 3T-613 Interval Summary 28 6/19/25 11:47 6/19/25 12:39 52 min 15.7 bpm 5,609 psi 7,019 psi 13 bbl 37.8 bpm 5,193 psi 5,413 psi 36.6 bpm 4,206 psi 4,186 psi 4,835 psi 3,770 hhp 738 psi 752 psi 7.30 ppg 6 6 30 % 29 % 25 cP 91.6 F 9.35 189,200 lbs 3,000 lbs 192,200 lbs 192,200 lbs Initial Rate (Breakdown): Total Proppant Pumped* : Proppant in Formation: Max Surface Pressure: Max BH Pressure: Pumps Ending Stage: Max Rate: Initial Surface Pressure (Breakdown): Proppant Summary Average Missile Pressure: Average Rate: Average Missile HHP: Wanli 16/20 Ceramic Pumped: Initial OA Pressure: Max Proppant Concentration: 100M Pumped: Average Temp: Interval Summary Pump Time: Start Date/Time: 3T-613 - Moraine - Interval 10 End Date/Time: Initial BH Pressure (Breakdown): Pad Percentage Actual Pumps Starting Stage: Dart/Ball Early : Average Visc: Pad Percentage Design Max OA Pressure: Average pH: Average BH Pressure: Average Surface Pressure: Conoco Phillips - 3T-613 Interval Summary 29 4,201 gal 100 bbls 64,641 gal 1,539 bbls 2,089 gal 50 bbls 8,629 gal 205 bbls 12,020 gal 286 bbls 41,449 gal 987 bbls 2,112 gal 50 bbls 2,543 gal 61 bbls 77,417 gal 1,843 bbls 68,842 gal 1,639 bbls Completed Comments: Engineer: Treater: Supervisor: Customer Engineer: Customer Rep: 30# Hybor G-i Volume: Fluid Summary (by stage description) Steven Sanders Interval Status: Fluid Summary (by fluid description) 30# Linear Volume: Proppant Laden Fluid Volume: Pre-Pad Volume: Pad Volume: Conditioning Pad Volume: Establish Stable Fluid Volume: Spacer and Dart Drop Volume: Treatment Slurry Volume (Calculated): Total Clean Fluid Volume: Interval completed as per design. Craig Karpinski James Campbell *Values for proppant are taken from software calculations based on multiple variables. Proppant is billed off of weight ticket volumes and may vary slightly from this number.Allen Eschete Chad Burkett Conoco Phillips - 3T-613 Interval Summary 30 6/19/25 12:39 6/19/25 13:32 53 min 15.5 bpm 5,633 psi 6,700 psi 10 bbl 37.7 bpm 5,160 psi 5,265 psi 36.3 bpm 4,250 psi 4,226 psi 4,794 psi 3,777 hhp 723 psi 754 psi 7.06 ppg 6 6 30 % 29 % 26 cP 93.2 F 9.32 190,482 lbs 3,000 lbs 193,482 lbs 193,482 lbs Max Surface Pressure: Average Missile Pressure: Initial Surface Pressure (Breakdown): Initial Rate (Breakdown): Start Date/Time: Average Missile HHP: Pumps Starting Stage: 100M Pumped: Interval Summary Proppant Summary Total Proppant Pumped* : Proppant in Formation: Pumps Ending Stage: Pump Time: Initial BH Pressure (Breakdown): Dart/Ball Early : 3T-613 - Moraine - Interval 11 End Date/Time: Max Proppant Concentration: Average Visc: Average Temp: Max Rate: Wanli 16/20 Ceramic Pumped: Average pH: Pad Percentage Actual Initial OA Pressure: Pad Percentage Design Average Surface Pressure: Max OA Pressure: Max BH Pressure: Average Rate: Average BH Pressure: Conoco Phillips - 3T-613 Interval Summary 31 4,278 gal 102 bbls 65,111 gal 1,550 bbls 2,193 gal 52 bbls 8,566 gal 204 bbls 11,992 gal 286 bbls 42,088 gal 1,002 bbls 2,085 gal 50 bbls 2,465 gal 59 bbls 78,021 gal 1,858 bbls 69,389 gal 1,652 bbls Completed Comments: Engineer: Treater: Supervisor: Customer Engineer: Customer Rep: Interval Status: 30# Linear Volume: Conditioning Pad Volume: 30# Hybor G-i Volume: Proppant Laden Fluid Volume: Steven Sanders Fluid Summary (by fluid description) Craig Karpinski James Campbell *Values for proppant are taken from software calculations based on multiple variables. Proppant is billed off of weight ticket volumes and may vary slightly from this number. Fluid Summary (by stage description) Establish Stable Fluid Volume: Pre-Pad Volume: Pad Volume: Spacer and Dart Drop Volume: Treatment Slurry Volume (Calculated): Total Clean Fluid Volume: Interval completed as per design. Allen Eschete Chad Burkett Conoco Phillips - 3T-613 Interval Summary 32 6/19/25 13:32 6/19/25 14:24 52 min 15.5 bpm 5,031 psi 6,602 psi 12 bbl 37.6 bpm 4,813 psi 5,032 psi 36.7 bpm 4,111 psi 4,086 psi 4,649 psi 3,695 hhp 744 psi 749 psi 7.07 ppg 6 6 30 % 29 % 26 cP 93 F 9.32 189,510 lbs 3,000 lbs 192,510 lbs 192,510 lbs Wanli 16/20 Ceramic Pumped: Pumps Ending Stage: Pad Percentage Design Proppant in Formation: Average Temp: Total Proppant Pumped* : Max Surface Pressure: 100M Pumped: Proppant Summary Start Date/Time: Average Rate: Average Missile Pressure: Pad Percentage Actual Initial Rate (Breakdown): Average BH Pressure: Average Surface Pressure: Dart/Ball Early : Max BH Pressure: Average Visc: Max OA Pressure: Average pH: Max Rate: Initial OA Pressure: End Date/Time: Pumps Starting Stage: Max Proppant Concentration: Pump Time: 3T-613 - Moraine - Interval 12 Interval Summary Initial BH Pressure (Breakdown): Average Missile HHP: Initial Surface Pressure (Breakdown): Conoco Phillips - 3T-613 Interval Summary 33 4,313 gal 103 bbls 64,536 gal 1,537 bbls 2,217 gal 53 bbls 8,566 gal 204 bbls 12,067 gal 287 bbls 41,413 gal 986 bbls 2,096 gal 50 bbls 2,490 gal 59 bbls 77,438 gal 1,844 bbls 68,849 gal 1,639 bbls Completed Comments: Engineer: Treater: Supervisor: Customer Engineer: Customer Rep: Treatment Slurry Volume (Calculated): Pre-Pad Volume: Proppant Laden Fluid Volume: Interval Status: Pad Volume: Conditioning Pad Volume: Spacer and Dart Drop Volume: James Campbell *Values for proppant are taken from software calculations based on multiple variables. Proppant is billed off of weight ticket volumes and may vary slightly from this number.Allen Eschete 30# Linear Volume: 30# Hybor G-i Volume: Fluid Summary (by fluid description) Fluid Summary (by stage description) Total Clean Fluid Volume: Interval completed as per design.Steven Sanders Establish Stable Fluid Volume: Craig Karpinski Chad Burkett Conoco Phillips - 3T-613 Interval Summary 34 6/19/25 14:24 6/19/25 15:23 59 min 15.9 bpm 5,220 psi 6,616 psi 8 bbl 37.9 bpm 4,927 psi 5,073 psi 36.9 bpm 3,788 psi 3,759 psi 4,498 psi 3,426 hhp 694 psi 699 psi 6.89 ppg 6 6 30 % 29 % 25 cP 92.3 F 9.2 3371 psi 0.662 psi/ft 3339 psi 3316 psi 3293 psi 189,731 lbs 3,000 lbs 192,731 lbs 192,731 lbs 100M Pumped: Proppant in Formation: Max Rate: Wanli 16/20 Ceramic Pumped: Average BH Pressure: Average Temp: Start Date/Time: Pumps Starting Stage: Average Rate: Proppant Summary Dart/Ball Early : Max OA Pressure: Average pH: Pumps Ending Stage: Max BH Pressure: Initial BH Pressure (Breakdown): Average Missile Pressure: Pump Time: 3T-613 - Moraine - Interval 13 Total Proppant Pumped* : Average Visc: Initial OA Pressure: Average Surface Pressure: Final 5 min: Final 10 min: Pad Percentage Design Initial Rate (Breakdown): Initial Surface Pressure (Breakdown): Max Surface Pressure: Max Proppant Concentration: Pad Percentage Actual ISDP: Final Fracture Gradient: Average Missile HHP: Interval Summary End Date/Time: Final 15 min: Conoco Phillips - 3T-613 Interval Summary 35 13,906 gal 331 bbls 571 gal 14 bbls 65,499 gal 1,560 bbls 2,176 gal 52 bbls 8,603 gal 205 bbls 12,061 gal 287 bbls 42,411 gal 1,010 bbls 11,730 gal 279 bbls 571 gal 14 bbls 2,424 gal 58 bbls 88,575 gal 2,109 bbls 79,976 gal 1,904 bbls Completed Comments: Engineer: Treater: Supervisor: Customer Engineer: Customer Rep: Establish Stable Fluid Volume: Interval Status: Pre-Pad Volume: Pad Volume: 30# Hybor G-i Volume: Freeze Protect Volume: Flush Volume: *Values for proppant are taken from software calculations based on multiple variables. Proppant is billed off of weight ticket volumes and may vary slightly from this number. Total Clean Fluid Volume: Conditioning Pad Volume: Proppant Laden Fluid Volume: Fluid Summary (by stage description) Freeze Protect Volume: Treatment Slurry Volume (Calculated): Interval completed as per design.Steven Sanders Craig Karpinski James Campbell Fluid Summary (by fluid description) 30# Linear Volume: Allen Eschete Chad Burkett Conoco Phillips - 3T-613 Interval Summary 36 6/20/25 9:30 6/20/25 11:39 128 min 15.3 bpm 4,652 psi 6,229 psi 11 bbl 37.3 bpm 4,927 psi 4,984 psi 34.9 bpm 4,247 psi 4,138 psi 4,607 psi 3,633 hhp 347 psi 534 psi 764 psi 7.11 ppg 6 6 30 % 30 % 25 cP 96.1 F 9.45 DFIT 10.300 bpm 1597 psi 3487 psi 10.6 bpm 1616 psi 3503 psi 3290 psi 0.646 psi/ft 189,080 lbs 3,000 lbs 192,080 lbs 192,080 lbs Average Rate: Average Missile Pressure: Pumps Ending Stage: Minifrac Max DH Pressure: Initial BH Pressure (Breakdown): Average Surface Pressure: Pad Percentage Design Pad Percentage Actual ISDP: Final Fracture Gradient: Proppant Summary Max OA Pressure: Max Proppant Concentration: Initial Rate (Breakdown): Minifrac Average DH Pressure: Minifrac Average Rate: Minifrac Average Pressure: Average Visc: Initial OA Pressure: End Date/Time: Average Temp: Dart/Ball Early : Max Surface Pressure: Minifrac Max Surface Pressure: Average Missile HHP: Open Well Pressure: Pumps Starting Stage: Average BH Pressure: 100M Pumped: Minifrac Max Rate: Pump Time: Average pH: Wanli 16/20 Ceramic Pumped: Max Rate: Max BH Pressure: Interval Summary Start Date/Time: 3T-613 - Moraine - Interval 14 Diagnostic method Initial Surface Pressure (Breakdown): Total Proppant Pumped* : Proppant in Formation: Conoco Phillips - 3T-613 Interval Summary 37 15,567 gal 371 bbls 571 gal 14 bbls 64,102 gal 1,526 bbls 571 gal 14 bbls 8,613 gal 205 bbls 12,203 gal 291 bbls 41,434 gal 987 bbls 3,094 gal 74 bbls 1,852 gal 44 bbls 1,676 gal 40 bbls 0 gal 0 bbls 88,810 gal 2,115 bbls 80,240 gal 1,910 bbls Completed Comments: Engineer: Treater: Supervisor: Customer Engineer: Customer Rep: DFIT Volume: Treatment Slurry Volume (Calculated): Total Clean Fluid Volume: Interval Status: Establish Stable Fluid Volume: Steven Sanders Allen Eschete Chad Burkett 30# Linear Volume: 30# Hybor G-i Volume: Proppant Laden Fluid Volume: Prime Up Pressure Test Pad Volume: Fluid Summary (by fluid description) Freeze Protect Volume: Spacer and Dart Drop Volume: Conditioning Pad Volume: - A DFIT was pumped prior to the stage, closure was determined to 2854 psi BHGP. Interval completed as per design. Fluid Summary (by stage description) Craig Karpinski James Campbell *Values for proppant are taken from software calculations based on multiple variables. Proppant is billed off of weight ticket volumes and may vary slightly from this number. Conoco Phillips - 3T-613 Interval Summary 38 6/20/25 11:39 6/20/25 12:34 56 min 15.3 bpm 5,865 psi 6,514 psi 11 bbl 38.2 bpm 4,758 psi 4,807 psi 36.6 bpm 4,049 psi 3,939 psi 4,465 psi 3,632 hhp 763 psi 780 psi 7.15 ppg 6 6 30 % 29 % 25 cP 92.8 F 9.36 201,861 lbs 3,000 lbs 204,861 lbs 204,861 lbs Average Rate: Start Date/Time: Pumps Starting Stage: 100M Pumped: Wanli 16/20 Ceramic Pumped: Proppant Summary Total Proppant Pumped* : Proppant in Formation: Average Temp: Initial OA Pressure: Max OA Pressure: Max Proppant Concentration: Average Surface Pressure: Average Visc: Average pH: Max Surface Pressure: Average Missile HHP: Initial BH Pressure (Breakdown): Average BH Pressure: Pump Time: Dart/Ball Early : 3T-613 - Moraine - Interval 15 Interval Summary Average Missile Pressure: Pad Percentage Actual Pumps Ending Stage: Pad Percentage Design End Date/Time: Max BH Pressure: Max Rate: Initial Surface Pressure (Breakdown): Initial Rate (Breakdown): Conoco Phillips - 3T-613 Interval Summary 39 4,302 gal 102 bbls 68,955 gal 1,642 bbls 2,186 gal 52 bbls 9,647 gal 230 bbls 12,085 gal 288 bbls 44,006 gal 1,048 bbls 2,116 gal 50 bbls 3,217 gal 77 bbls 82,397 gal 1,962 bbls 73,257 gal 1,744 bbls Completed Comments: Engineer: Treater: Supervisor: Customer Engineer: Customer Rep: Pre-Pad Volume: Allen Eschete Chad Burkett *Values for proppant are taken from software calculations based on multiple variables. Proppant is billed off of weight ticket volumes and may vary slightly from this number. Establish Stable Fluid Volume: Proppant Laden Fluid Volume: 30# Linear Volume: Spacer and Dart Drop Volume: Steven Sanders Fluid Summary (by stage description) Fluid Summary (by fluid description) Treatment Slurry Volume (Calculated): Total Clean Fluid Volume: Interval Status: Craig Karpinski James Campbell Pad Volume: Conditioning Pad Volume: Pump 329 went offline do to a preload. Rate was brought up with the other pumps and later on pump 329 was brought back online. 30# Hybor G-i Volume: Conoco Phillips - 3T-613 Interval Summary 40 6/20/25 12:34 6/20/25 13:30 56 min 15.5 bpm 5,015 psi 6,502 psi 8 bbl 37.6 bpm 4,537 psi 4,631 psi 36.4 bpm 3,954 psi 3,840 psi 4,317 psi 3,528 hhp 776 psi 793 psi 7.02 ppg 6 6 30 % 29 % 25 cP 94.8 F 9.35 198,701 lbs 3,000 lbs 201,701 lbs 201,701 lbs Total Proppant Pumped* : Max Rate: 3T-613 - Moraine - Interval 16 Average Missile Pressure: Proppant Summary Initial Rate (Breakdown): Initial Surface Pressure (Breakdown): 100M Pumped: Wanli 16/20 Ceramic Pumped: Pumps Ending Stage: Max Surface Pressure: Interval Summary Pad Percentage Actual Initial OA Pressure: Initial BH Pressure (Breakdown): Dart/Ball Early : Average Missile HHP: Max OA Pressure: Average Temp: Proppant in Formation: Average pH: Pumps Starting Stage: Start Date/Time: Average BH Pressure: Average Rate: End Date/Time: Max BH Pressure: Max Proppant Concentration: Pad Percentage Design Average Visc: Pump Time: Average Surface Pressure: Conoco Phillips - 3T-613 Interval Summary 41 4,207 gal 100 bbls 69,423 gal 1,653 bbls 2,153 gal 51 bbls 9,726 gal 232 bbls 11,927 gal 284 bbls 43,883 gal 1,045 bbls 2,054 gal 49 bbls 3,887 gal 93 bbls 82,629 gal 1,967 bbls 73,630 gal 1,753 bbls Completed Comments: Engineer: Treater: Supervisor: Customer Engineer: Customer Rep: 30# Hybor G-i Volume: Fluid Summary (by stage description) Interval Status: Interval completed as per design. Treatment Slurry Volume (Calculated): 30# Linear Volume: Pre-Pad Volume: Pad Volume: Conditioning Pad Volume: Proppant Laden Fluid Volume: Total Clean Fluid Volume: Fluid Summary (by fluid description) Spacer and Dart Drop Volume: Establish Stable Fluid Volume: Steven Sanders Craig Karpinski James Campbell *Values for proppant are taken from software calculations based on multiple variables. Proppant is billed off of weight ticket volumes and may vary slightly from this number.Allen Eschete Chad Burkett Conoco Phillips - 3T-613 Interval Summary 42 6/20/25 13:30 6/20/25 14:26 56 min 15.3 bpm 5,541 psi 6,295 psi 10 bbl 37.6 bpm 4,281 psi 4,412 psi 36.5 bpm 3,744 psi 3,621 psi 4,151 psi 3,349 hhp 778 psi 797 psi 7.09 ppg 6 6 30 % 29 % 25 cP 102.4 F 9.29 198,692 lbs 3,000 lbs 201,692 lbs 201,692 lbs Average Visc: Average Temp: Max OA Pressure: Average Surface Pressure: Max Rate: Initial OA Pressure: Max BH Pressure: Initial Surface Pressure (Breakdown): Pumps Starting Stage: Average Missile HHP: Pump Time: Max Surface Pressure: Initial BH Pressure (Breakdown): Pumps Ending Stage: Pad Percentage Design Pad Percentage Actual Average BH Pressure: Start Date/Time: End Date/Time: Max Proppant Concentration: Wanli 16/20 Ceramic Pumped: 100M Pumped: Total Proppant Pumped* : Average Missile Pressure: Initial Rate (Breakdown): Dart/Ball Early : 3T-613 - Moraine - Interval 17 Interval Summary Average pH: Proppant Summary Average Rate: Proppant in Formation: Conoco Phillips - 3T-613 Interval Summary 43 4,357 gal 104 bbls 69,062 gal 1,644 bbls 2,189 gal 52 bbls 9,800 gal 233 bbls 11,988 gal 285 bbls 44,156 gal 1,051 bbls 2,168 gal 52 bbls 3,118 gal 74 bbls 82,417 gal 1,962 bbls 73,419 gal 1,748 bbls Completed Comments: Engineer: Treater: Supervisor: Customer Engineer: Customer Rep: Interval Status: Pre-Pad Volume: Fluid Summary (by stage description) Interval completed as per design.Steven Sanders Craig Karpinski James Campbell Total Clean Fluid Volume: Establish Stable Fluid Volume: Treatment Slurry Volume (Calculated): *Values for proppant are taken from software calculations based on multiple variables. Proppant is billed off of weight ticket volumes and may vary slightly from this number. 30# Linear Volume: Allen Eschete Chad Burkett Conditioning Pad Volume: Proppant Laden Fluid Volume: Fluid Summary (by fluid description) 30# Hybor G-i Volume: Pad Volume: Spacer and Dart Drop Volume: Conoco Phillips - 3T-613 Interval Summary 44 6/20/25 14:26 6/20/25 16:04 98 min 15.6 bpm 5,572 psi 6,761 psi 9 bbl 37.5 bpm 4,119 psi 4,507 psi 35.5 bpm 3,718 psi 3,589 psi 4,167 psi 3,235 hhp 774 psi 783 psi 7.14 ppg 6 6 30 % 29 % 25 cP 96.7 F 9.2 DFIT 10.500 bpm 1742 psi 3654 psi 10.6 bpm 1758 psi 1884 psi 3323 psi 0.658 psi/ft 198,933 lbs 3,000 lbs 201,933 lbs 201,933 lbs Minifrac Max Rate: Average Visc: Total Proppant Pumped* : Proppant in Formation: Initial OA Pressure: Max OA Pressure: Max Surface Pressure: Diagnostic method Minifrac Average Rate: Wanli 16/20 Ceramic Pumped: End Date/Time: Initial Rate (Breakdown): Average Rate: 3T-613 - Moraine - Interval 18 Pump Time: Average BH Pressure: Minifrac Average Pressure: Minifrac Average DH Pressure: Pumps Starting Stage: Pumps Ending Stage: Final Fracture Gradient: Start Date/Time: Average Surface Pressure: Dart/Ball Early : Initial BH Pressure (Breakdown): Pad Percentage Design Max Proppant Concentration: Pad Percentage Actual Average Missile Pressure: ISDP: Max Rate: Average Missile HHP: Max BH Pressure: Initial Surface Pressure (Breakdown): Interval Summary Average Temp: Average pH: Minifrac Max DH Pressure: Minifrac Max Surface Pressure: Proppant Summary 100M Pumped: Conoco Phillips - 3T-613 Interval Summary 45 13,605 gal 324 bbls 67,724 gal 1,612 bbls 9,688 gal 231 bbls 11,931 gal 284 bbls 44,010 gal 1,048 bbls 9,883 gal 235 bbls 2,064 gal 49 bbls 2,095 gal 50 bbls 1,658 gal 39 bbls 90,338 gal 2,151 bbls 81,329 gal 1,936 bbls Completed Comments: Engineer: Treater: Supervisor: Customer Engineer: Customer Rep: Fluid Summary (by stage description) 30# Linear Volume: Fluid Summary (by fluid description) DFIT Volume: Proppant Laden Fluid Volume: *Values for proppant are taken from software calculations based on multiple variables. Proppant is billed off of weight ticket volumes and may vary slightly from this number. Treatment Slurry Volume (Calculated): Pad Volume: Allen Eschete Establish Stable Fluid Volume: Displacement Volume: Conditioning Pad Volume: Interval Status: Due to third party proppant loading falling behind, the OSR called to seat the dart and shut down while the mover was loaded. An unplanned DFIT was pumped after the dart seated and closure was not able to be identified. Once two bins were filled with proppant, the remainder of the interval was pumped as per design.James Campbell Chad Burkett Spacer and Dart Drop Volume: Steven Sanders Total Clean Fluid Volume: 30# Hybor G-i Volume: Craig Karpinski Conoco Phillips - 3T-613 Interval Summary 46 6/20/25 16:04 6/20/25 17:05 61 min 15.2 bpm 5,354 psi 6,196 psi 8 bbl 37.6 bpm 4,304 psi 4,284 psi 36.4 bpm 3,681 psi 3,551 psi 4,030 psi 3,284 hhp 734 psi 769 psi 7.14 ppg 6 6 30 % 29 % 25 cP 97.9 F 9.3 3346 psi 0.664 psi/ft 3413 psi 3394 psi 3377 psi 198,575 lbs 3,000 lbs 201,575 lbs 201,575 lbs Pad Percentage Design Proppant Summary Average Surface Pressure: 3T-613 - Moraine - Interval 19 Initial Surface Pressure (Breakdown): Max Proppant Concentration: Pumps Ending Stage: Proppant in Formation: 100M Pumped: Average Missile HHP: Interval Summary Average Visc: Start Date/Time: End Date/Time: Dart/Ball Early : Pumps Starting Stage: Max Rate: Initial Rate (Breakdown): Max BH Pressure: Average Rate: Pad Percentage Actual Max Surface Pressure: Pump Time: Initial OA Pressure: Initial BH Pressure (Breakdown): Max OA Pressure: Wanli 16/20 Ceramic Pumped: Average Temp: Final 10 min: Final 15 min: Average Missile Pressure: Average pH: Average BH Pressure: Total Proppant Pumped* : Final Fracture Gradient: Final 5 min: ISDP: Conoco Phillips - 3T-613 Interval Summary 47 12,092 gal 288 bbls 571 gal 14 bbls 69,015 gal 1,643 bbls 2,248 gal 54 bbls 9,741 gal 232 bbls 12,016 gal 286 bbls 43,922 gal 1,046 bbls 9,844 gal 234 bbls 571 gal 14 bbls 3,336 gal 79 bbls 90,671 gal 2,159 bbls 81,678 gal 1,945 bbls Completed Comments: Engineer: Treater: Supervisor: Customer Engineer: Customer Rep: Interval completed as per design.Steven Sanders Craig Karpinski Flush Volume: Conditioning Pad Volume: Fluid Summary (by fluid description) Freeze Protect Volume: Pad Volume: Freeze Protect Volume: Allen Eschete Chad Burkett 30# Linear Volume: Proppant Laden Fluid Volume: Pre-Pad Volume: Fluid Summary (by stage description) James Campbell Total Clean Fluid Volume: 30# Hybor G-i Volume: Treatment Slurry Volume (Calculated): *Values for proppant are taken from software calculations based on multiple variables. Proppant is billed off of weight ticket volumes and may vary slightly from this number. Establish Stable Fluid Volume: Interval Status: Conoco Phillips - 3T-613 Interval Summary 48 6/21/25 9:15 6/21/25 13:25 250 min 15.4 bpm 4,668 psi 6,136 psi 13 bbl 37.6 bpm 3,787 psi 4,093 psi 35.9 bpm 3,598 psi 3,482 psi 3,973 psi 3,166 hhp 463 psi 522 psi 790 psi 5.11 ppg 6 6 30 % 29 % 25 cP 95.9 F 9.4 Minifrac 37.170 bpm 3647 psi 3991 psi 37.3 bpm 3922 psi 4187 psi 3222 psi 0.639 psi/ft 199,999 lbs 3,000 lbs 202,999 lbs 202,999 lbs Initial Rate (Breakdown): Pumps Starting Stage: Minifrac Average Pressure: Max Proppant Concentration: Average Visc: Max Surface Pressure: 3T-613 - Moraine - Interval 20 Minifrac Average DH Pressure: Average Temp: Minifrac Max DH Pressure: Max OA Pressure: Pad Percentage Actual Minifrac Max Surface Pressure: ISDP: Average Missile HHP: Minifrac Max Rate: Open Well Pressure: Initial OA Pressure: Interval Summary Start Date/Time: End Date/Time: Final Fracture Gradient: Max BH Pressure: Average Rate: Average Missile Pressure: Average Surface Pressure: Average pH: Initial Surface Pressure (Breakdown): Initial BH Pressure (Breakdown): Dart/Ball Early : Max Rate: Diagnostic method Proppant Summary Wanli 16/20 Ceramic Pumped: 100M Pumped: Pumps Ending Stage: Minifrac Average Rate: Average BH Pressure: Pump Time: Pad Percentage Design Total Proppant Pumped* : Proppant in Formation: Conoco Phillips - 3T-613 Interval Summary 49 21,213 gal 505 bbls 571 gal 14 bbls 128,155 gal 3,051 bbls 571 gal 14 bbls 20,921 gal 498 bbls 12,020 gal 286 bbls 70,755 gal 1,685 bbls 8,731 gal 208 bbls 3,001 gal 71 bbls 3,402 gal 81 bbls 4,566 gal 109 bbls 16,491 gal 393 bbls 9,481 gal 226 bbls 158,996 gal 3,786 bbls 149,939 gal 3,570 bbls Completed Comments: Engineer: Treater: Supervisor: Customer Engineer: Customer Rep: A minifrac was pumped prior to the stage and closure pressure was determined to 3010 psi on the BHG. While pumping the pad, a suction hose burst cause the blender discharge rate to increase to 42 bpm. Remainder of the interval was pumped as per design. Treatment Slurry Volume (Calculated): Establish Stable Fluid Volume: Minifrac - Establish Fluid Volume: Minifrac - Treatment Volume: Minifrac - Flush Volume: Total Clean Fluid Volume: Freeze Protect Volume: Interval Status: Steven Sanders Craig Karpinski Proppant Laden Fluid Volume: James Campbell *Values for proppant are taken from software calculations based on multiple variables. Proppant is billed off of weight ticket volumes and may vary slightly from this number.Allen Eschete Chad Burkett Fluid Summary (by fluid description) Fluid Summary (by stage description) 30# Hybor G-i Volume: Pad Volume: Prime Up Pressure Test 30# Linear Volume: Displacement Volume: Conditioning Pad Volume: Spacer and Dart Drop Volume: Conoco Phillips - 3T-613 Interval Summary 50 6/21/25 13:25 6/21/25 15:18 114 min 15.2 bpm 5,449 psi 6,248 psi 3 bbl 37.8 bpm 3,941 psi 3,969 psi 35.2 bpm 3,333 psi 3,203 psi 3,858 psi 2,875 hhp 887 psi 790 psi 812 psi 5.05 ppg 6 6 30 % 26 % 25 cP 91.4 F 9.3 Minifrac 37.500 bpm 3073 psi 3788 psi 37.6 bpm 3247 psi 3819 psi 3406 psi 0.677 psi/ft 3534 psi 3515 psi 3502 psi 58,196 lbs 58,196 lbs 58,196 lbs Total Proppant Pumped* : Max Surface Pressure: Final Fracture Gradient: 3T-613 - Moraine - Interval 21 Minifrac Average Pressure: Average BH Pressure: Pumps Starting Stage: Average Temp: Average Missile Pressure: Average Surface Pressure: Pad Percentage Actual Average Rate: Minifrac Average Rate: Max Proppant Concentration: Pad Percentage Design Minifrac Max Surface Pressure: Final 15 min: Average pH: Max BH Pressure: Average Missile HHP: Final 5 min: Pumps Ending Stage: Average Visc: Initial Rate (Breakdown): Initial Surface Pressure (Breakdown): Initial BH Pressure (Breakdown): Dart/Ball Early : Max Rate: Initial OA Pressure: Open Well Pressure: Max OA Pressure: Proppant in Formation: Minifrac Max DH Pressure: ISDP: Interval Summary Minifrac Average DH Pressure: Minifrac Max Rate: Proppant Summary Wanli 16/20 Ceramic Pumped: Final 10 min: Start Date/Time: End Date/Time: Pump Time: Diagnostic method Conoco Phillips - 3T-613 Interval Summary 51 20,542 gal 489 bbls 41,722 gal 993 bbls 2,213 gal 53 bbls 2,234 gal 53 bbls 5,962 gal 142 bbls 20,506 gal 488 bbls 9,125 gal 217 bbls 1,287 gal 31 bbls 3,300 gal 79 bbls 8,433 gal 201 bbls 9,204 gal 219 bbls 64,860 gal 1,544 bbls 62,264 gal 1,482 bbls Completed Comments: Engineer: Treater: Supervisor: Customer Engineer: Customer Rep: Establish Stable Fluid Volume: Minifrac - Establish Fluid Volume: A minifrac was pumped prior to the stage and closure pressure was determined to 3082 psi on the BHG. Interval was pumped as per design.Craig Karpinski James Campbell Allen Eschete Chad Burkett Interval Status: Minifrac - Flush Volume: Minifrac - Treatment Volume: Treatment Slurry Volume (Calculated): Steven Sanders *Values for proppant are taken from software calculations based on multiple variables. Proppant is billed off of weight ticket volumes and may vary slightly from this number. Pad Volume: Fluid Summary (by fluid description) Fluid Summary (by stage description) Conditioning Pad Volume: Flush Volume: Proppant Laden Fluid Volume: Pre-Pad Volume: 30# Linear Volume: 30# Hybor G-i Volume: Total Clean Fluid Volume: Conoco Phillips - 3T-613 Interval Summary 52 CustomerFormationLeaseAPIDateWell SummaryWanli 16/20 Ceramic 100MTotal ProppantSurface Pressure Rate Visc Temp pHrface PressRate gal bbl gal bbl gal bbl lbs lbs lbs14074 36.0 26 94.5 9.2 5893 38.7 15,488 369 571 14 107,433 2,558 166,232 3,000 169,232 24969 35.9 26 95 9.2 5688 37.6 32,683 778 1,470 35 173,312 4,126 183,652 6,000 189,652 35146 26.5 27 97 9.2 6119 37.8 5,800 138 571 14 120,846 2,877 169,757 3,000 172,757 45240 36.1 27 97 9.3 6498 37.3 4,774 114 78,621 1,872 171,116 3,000 174,116 55604 35.9 27 96 9.3 6983 37.2 4,377 104 63,909 1,522 170,488 3,000 173,488 65114 36.4 28 95 9.3 6174 37.4 16,148 384 571 14 78,005 1,857 170,731 3,000 173,731 75739 34.4 29 92 9.4 6532 37.3 5,451 130 571 14 64,321 1,531 169,746 3,000 172,746 84961 35.2 28 93 9.5 5733 37.9 4,287 102 571 14 103,067 2,454 189,471 3,000 192,471 94390 36.4 26 93 9.3 5565 38.9 4,380 104 69,393 1,652 189,693 3,000 192,693 104186 36.6 25 92 9.4 5193 37.8 4,201 100 68,842 1,639 189,200 3,000 192,200 114226 36.3 26 93 9.3 5160 37.7 4,278 102 69,389 1,652 190,482 3,000 193,482 124086 36.7 26 93 9.3 4813 37.6 4,313 103 68,849 1,639 189,510 3,000 192,510 133759 36.9 25 92 9.2 4927 37.9 13,906 331 571 14 79,976 1,904 189,731 3,000 192,731 144138 34.9 25 96 9.5 4927 37.3 15,567 371 571 14 80,240 1,910 189,080 3,000 192,080 153939 36.6 25 93 9.4 4758 38.2 4,302 102 73,257 1,744 201,861 3,000 204,861 163840 36.4 25 95 9.4 4537 37.6 4,207 100 73,630 1,753 198,701 3,000 201,701 173621 36.5 25 102 9.3 4281 37.6 4,357 104 73,419 1,748 198,692 3,000 201,692 183589 35.5 25 97 9.2 4119 37.5 13,605 324 81,329 1,936 198,933 3,000 201,933 193551 36.4 25 98 9.3 4304 37.6 12,092 288 571 14 81,678 1,945 198,575 3,000 201,575 203482 35.9 25 96 9.4 3787 37.6 21,213 505 571 14 149,939 3,570 199,999 3,000 202,999 213203 35.2 25 91 9.3 3941 37.8 20,542 489 62,264 1,482 58,196 58,196 Minimum4201 100 571 14 62264 1482 58196 3000 58196 Average10284 245 661 16 86749 2065 180183 3150 183183 Maximum32683 778 1470 35 173312 4126 201861 6000 204861 Wanli 16/20 Ceramic 100M Total ProppantPressure Rate Visc Temp pH Pressure Rate gal bbl gal bbl gal bbl lbs lbs TotalPlanned220,805 5,257 11,880 283 1,792,660 42,682 3,781,700 63,000 3,844,700Recorded4811 35.2 27 94 9.30 6983 38.9 215,971 5,142 6,609 157 1,821,719 43,374 3,783,846 63,000 3,846,846Weight Tickets3,743,524 63,000 3,806,524** Proppant is billed from Weight Ticket volumesJune 16, 202550-103-209143T-613MoraineConoco Phillips IntervalAverage MaxAverage Max30# Linear30# Linearmultiple variablesTotal FluidFluidsProppantsFluidsProppantsTotal FluidFreeze ProtectFreeze ProtectConoco Phillips - 3T-613 Fluid System-Proppant Summary53 <-Paste Interval 1 Plots HereTreatment Plot - Arsenal Burst Disk6/14/202510:5010:556/14/202511:00Time010002000300040005000600070008000900010000A0102030405060708090100B012345678910C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD2Global Event Log2IntersectionArsenal Burst Disk 10:58:40SBP7022Conoco Phillips - 3T-613 Interval 1 Plots54 <-Paste Interval 1 Plots HereTreatment Plot - Shift Alpha Sleeve6/14/202511:0011:0111:0211:0311:0411:056/14/202511:06Time010002000300040005000600070008000900010000A0102030405060708090100B012345678910C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD3Global Event Log3IntersectionAlpha Sleeve 11:05:43SBP8115Conoco Phillips - 3T-613 Interval 1 Plots55 <-Paste Interval 1 Plots HereADP Chemical Plots - Bucket Test 6.16.256/16/202507:2707:2807:2907:3007:3107:3207:336/16/202507:34Time010203040A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)AB2Conoco Phillips - 3T-613 Interval 1 Plots56 <-Paste Interval 1 Plots HereBlender Chemical Plot - Bucket Test 6.16.256/16/202507:2807:3007:3207:3407:3607:3807:4007:426/16/202507:44Time0.00.51.01.52.02.53.0A0.00.51.01.52.02.5BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-II Conc (lb/Mgal)Optiflo-III Conc (lb/Mgal)MO-67 Conc (gal/Mgal)CL-28M BU Conc (gal/Mgal)BABBAA2Conoco Phillips - 3T-613 Interval 1 Plots57 ePRV Test - 6.16.256/16/202507:5007:5508:0008:056/16/202508:10Time01000200030004000500060007000Treating Pressure (psi)Treating Pressure @Pump (psi)I1 Global Kickout Pressure (psi)P2 Kickout Pressure (psi)Pop-off (psi)6543Global Event Log3456Intersection IntersectionePRV - Primary Tubing ePRV - Primary IAePRV - Secondary Tubing ePRV - Secondary IA07:52:20 07:54:3808:08:38 08:10:02TP TP930.9 20511501 1320TPP TPP974.9 20911054 745.6IGKP IGKP1500 15002000 2000Conoco Phillips - 3T-613 Interval 1 Plots58 Pressure Test - 6.16. 256/16/202516:2516:3016:3516:406/16/202516:45Time010002000300040005000600070008000900010000Treating Pressure (psi)Treating Pressure @Pump (psi)I1 Global Kickout Pressure (psi)P2 Kickout Pressure (psi)Pop-off (psi)7170Global Event Log7071Intersection IntersectionPressure Test - Max Pressure Test - Pass16:38:49 16:44:35TP TP9493 9194TPP TPP9510 9194IGKP IGKP9500 9500PKP PKP9500 9500Customer: CONOCOPHILLIPS NORTH SLOPE - EBUSJob Date: 16-Jun-2025Sales Order #: 0910128224Well Description: 3T-613 3T-613UWI: 50-103-20914-00Conoco Phillips - 3T-613 Interval 1 Plots59 Treatment Plot - Interval 1 - DFIT6/16/202509:3509:4009:456/16/202509:50Time010002000300040005000600070008000900010000A0102030405060708090100B012345678910C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD54Conoco Phillips - 3T-613 Interval 1 Plots60 ADP Chemical Plots - Interval 1 - DFIT6/16/202509:4209:4409:4609:486/16/202509:50Time0102030405060A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)AB5Conoco Phillips - 3T-613 Interval 1 Plots61 Blender Chemical Plot - Interval 1 - DFIT6/16/202509:4209:4409:4609:486/16/202509:50Time0.00.51.01.52.02.53.0A0.00.51.01.52.02.5BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-II Conc (lb/Mgal)Optiflo-III Conc (lb/Mgal)MO-67 Conc (gal/Mgal)CL-28M BU Conc (gal/Mgal)BAABAA5Conoco Phillips - 3T-613 Interval 1 Plots62 Treatment Plot - Interval 1 - Step Rate Test6/16/202510:3010:3510:4010:4510:5010:556/16/202511:00Time0200040006000800010000A020406080100B0246810C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD8730292827262524232221201918171615Global Event Log15161718192021222324252627282930Intersection IntersectionOpen Well Step Rate Test - 1 bpmStep Rate Test - 2 bpm Step Rate Test - 3 bpmStep Rate Test - 4 bpm Step Rate Test - 5 bpmStep Rate Test - 6 bpm Step Rate Test - 7 bpmStep Rate Test - 8 bpm Step Rate Test - 9 bpmStep Rate Test - 10 bpm Step Rate Test - 11 bpmStep Rate Test - 12 bpm Step Rate Test - 13 bpmStep Rate Test - 14 bpm Step Rate Test - 15 bpm10:32:53 10:35:0210:37:39 10:39:4010:41:24 10:43:3210:45:28 10:47:1910:49:11 10:50:1610:52:26 10:54:1210:56:06 10:57:5510:59:54 11:01:53TP TP667.0 13821599 17101830 19572074 23532444 26362740 27412755 28702900 2874SR SR0.000 0.9122.160 2.9013.872 4.8745.941 7.1078.130 8.90210.03 10.9811.93 12.7713.81 14.87GBP GBP2707 35193674 37523828 39294045 42214267 44604484 45104517 46354600 4567Conoco Phillips - 3T-613 Interval 1 Plots63 Treatment Plot - Interval 16/16/202510:4011:0011:2011:4012:006/16/202512:20Time010002000300040005000600070008000A0102030405060708090100B012345678910C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD32117161514131211109872Conoco Phillips - 3T-613 Interval 1 Plots64 ADP Chemical Plots - Interval 16/16/202510:4011:0011:2011:406/16/202512:00Time0102030405060A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)AB2117161514131211109872Conoco Phillips - 3T-613 Interval 1 Plots65 Blender Chemical Plot - Interval 16/16/202510:4011:0011:2011:406/16/202512:00Time0.00.51.01.52.02.53.0A0.00.51.01.52.02.5BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-II Conc (lb/Mgal)Optiflo-III Conc (lb/Mgal)MO-67 Conc (gal/Mgal)CL-28M BU Conc (gal/Mgal)BABBAA2117161514131211109872Conoco Phillips - 3T-613 Interval 1 Plots66 Net Pressure Plot - Interval 123Time (min)2345678923456789100100010000A-5-4-3-2-1012345CNet Gauge BH Pres (psi)A Closure Pressure = 3142 psi 0 Time = 06/16/25 07:26:00 1-9.030.0000.000Customer: CONOCOPHILLIPS NORTH SLOPE - EBUSJob Date: 16-Jun-2025Sales Order #: 0910128224Well Description: 3T-613 3T-613UWI: 50-103-20914-00Conoco Phillips - 3T-613 Interval 1 Plots67 <-Paste Interval 1 Plots HereTreatment Plot - Interval 2 Attempt 16/16/202512:1012:2012:3012:4012:5013:006/16/202513:10Time010002000300040005000600070008000A0102030405060708090100B012345678910C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD654321172Conoco Phillips - 3T-613 Interval 2 Plots68 <-Paste Interval 1 Plots HereADP Chemical Plots - Interval 2 Attempt 16/16/202512:1012:2012:3012:4012:5013:006/16/202513:10Time0102030405060A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)AB654321172Conoco Phillips - 3T-613 Interval 2 Plots69 <-Paste Interval 1 Plots HereBlender Chemical Plot - Interval 2 Attempt 16/16/202512:1012:2012:3012:4012:5013:006/16/202513:10Time0.00.51.01.52.02.53.0A0.00.51.01.52.02.5BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-II Conc (lb/Mgal)Optiflo-III Conc (lb/Mgal)MO-67 Conc (gal/Mgal)CL-28M BU Conc (gal/Mgal)BABBAA654321172Conoco Phillips - 3T-613 Interval 2 Plots70 <-Paste Interval 1 Plots HereNet Pressure Plot - Interval 2 Attempt 13Time (min)2345678923456789100100010000A-5-4-3-2-1012345CNet Gauge BH Pres (psi)A Closure Pressure = 3142 psi 0 Time = 06/16/25 07:26:00 1-9.030.0000.000Customer: CONOCOPHILLIPS NORTH SLOPE - EBUSJob Date: 16-Jun-2025Sales Order #: 0910128224Well Description: 3T-613 3T-613UWI: 50-103-20914-00Conoco Phillips - 3T-613 Interval 2 Plots71 Treatment Plot - Interval 2 Attempt 26/16/202517:0017:2017:406/16/202518:00Time010002000300040005000600070008000A0102030405060708090100B012345678910C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD1716151413121110987Conoco Phillips - 3T-613 Interval 2 Plots72 ADP Chemical Plots - Interval 2 Attempt 26/16/202517:0017:2017:406/16/202518:00Time0102030405060A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)AB1716151413121110987Conoco Phillips - 3T-613 Interval 2 Plots73 Blender Chemical Plot - Interval 2 Attempt 26/16/202517:0017:2017:4018:006/16/202518:20Time0.00.51.01.52.02.53.0A0.00.51.01.52.02.5BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-II Conc (lb/Mgal)Optiflo-III Conc (lb/Mgal)MO-67 Conc (gal/Mgal)CL-28M BU Conc (gal/Mgal)BABBAA1716151413121110987Conoco Phillips - 3T-613 Interval 2 Plots74 Net Pressure Plot - Interval 2 Attempt 26Time (min)2345678923456789100100010000A-5-4-3-2-1012345CNet Gauge BH Pres (psi)A Closure Pressure = 3142 psi 0 Time = 06/16/25 07:26:00 1-9.030.0000.000Customer: CONOCOPHILLIPS NORTH SLOPE - EBUSJob Date: 16-Jun-2025Sales Order #: 0910128224Well Description: 3T-613 3T-613UWI: 50-103-20914-00Conoco Phillips - 3T-613 Interval 2 Plots75 <-Paste Interval 1 Plots HereADP Chemical Plots - Bucket Test 6.17.256/17/202506:5606:5706:5806:596/17/202507:00Time010203040A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)ABConoco Phillips - 3T-613 Interval 3 Plots76 <-Paste Interval 1 Plots HereBlender Chemical Plot - Bucket Test 6.17.256/17/202506:5206:5406:5606:5807:006/17/202507:02Time0.00.51.01.52.02.53.0A0.00.51.01.52.02.5BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-II Conc (lb/Mgal)Optiflo-III Conc (lb/Mgal)MO-67 Conc (gal/Mgal)CL-28M BU Conc (gal/Mgal)BABBAAConoco Phillips - 3T-613 Interval 3 Plots77 <-Paste Interval 1 Plots HereePRV Test - 6.17.256/17/202509:1109:1209:1309:1409:1509:1609:176/17/202509:18Time01000200030004000500060007000Treating Pressure (psi)Treating Pressure @Pump (psi)I1 Global Kickout Pressure (psi)P2 Kickout Pressure (psi)Pop-off (psi)8765Global Event Log5678Intersection IntersectionePRV - Primary Tubing ePRV - Primary IAePRV - Secondary Tubing ePRV - Secondary IA09:12:55 09:14:4609:16:18 09:17:48TP TP854.0 551.2606.5 775.5TPP TPP979.9 715.1782.1 955.7IGKP IGKP1500 15001500 1500Conoco Phillips - 3T-613 Interval 3 Plots78 <-Paste Interval 1 Plots HerePressure Test - 6.17.256/17/202509:2009:2209:2409:2609:286/17/202509:30Time010002000300040005000600070008000900010000Treating Pressure (psi)Treating Pressure @Pump (psi)I1 Global Kickout Pressure (psi)P2 Kickout Pressure (psi)Pop-off (psi)1211109Global Event Log9101112Intersection IntersectionTesting Globals Testing LocalsPressure Test - Max Pressure Test - Pass09:19:59 09:20:0609:23:07 09:29:53TP TP1112 11169532 9293TPP TPP1256 12549703 9426IGKP IGKP1500 95009500 9500PKP PKP500.4 500.49500 9500Customer: CONOCOPHILLIPS NORTH SLOPE - EBUSJob Date: 17-Jun-2025Sales Order #: 0910128224Well Description: 3T-613 3T-613UWI: 50-103-20914-00Conoco Phillips - 3T-613 Interval 3 Plots79 Treatment Plot - Interval 36/17/202509:4010:0010:2010:4011:0011:2011:406/17/202512:00Time010002000300040005000600070008000A0102030405060708090100B012345678910C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD43211514131211109876544Conoco Phillips - 3T-613 Interval 3 Plots80 ADP Chemical Plots - Interval 36/17/202510:0010:2010:4011:0011:206/17/202511:40Time010203040A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)AB3211514131211109876544Conoco Phillips - 3T-613 Interval 3 Plots81 Blender Chemical Plot - Interval 36/17/202509:4010:0010:2010:4011:0011:206/17/202511:40Time0.00.51.01.52.02.53.0A0.00.51.01.52.02.5BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-II Conc (lb/Mgal)Optiflo-III Conc (lb/Mgal)MO-67 Conc (gal/Mgal)CL-28M BU Conc (gal/Mgal)BABAAA3211514131211109876544Conoco Phillips - 3T-613 Interval 3 Plots82 Net Pressure Plot - Interval 32Time (min)2345678923456789100100010000A-5-4-3-2-1012345CNet Gauge BH Pres (psi)A Closure Pressure = 3142 psi 0 Time = 06/17/25 07:10:15 111.000.0000.000Customer: CONOCOPHILLIPS NORTH SLOPE - EBUSJob Date: 17-Jun-2025Sales Order #: 0910128224Well Description: 3T-613 3T-613UWI: 50-103-20914-00Conoco Phillips - 3T-613 Interval 3 Plots83 <-Paste Interval 1 Plots HereTreatment Plot - Interval 46/17/202511:4011:5012:0012:1012:2012:3012:406/17/202512:50Time010002000300040005000600070008000A0102030405060708090100B012345678910C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD43211211109876543211554Conoco Phillips - 3T-613 Interval 4 Plots84 <-Paste Interval 1 Plots HereADP Chemical Plots - Interval 46/17/202511:4011:5012:0012:1012:2012:306/17/202512:40Time010203040A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)AB211211109876543211554Conoco Phillips - 3T-613 Interval 4 Plots85 <-Paste Interval 1 Plots HereBlender Chemical Plot - Interval 46/17/202511:5012:0012:1012:2012:306/17/202512:40Time0.00.51.01.52.02.53.0A0.00.51.01.52.02.5BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-II Conc (lb/Mgal)Optiflo-III Conc (lb/Mgal)MO-67 Conc (gal/Mgal)CL-28M BU Conc (gal/Mgal)BABAAA211211109876543211554Conoco Phillips - 3T-613 Interval 4 Plots86 <-Paste Interval 1 Plots HereNet Pressure Plot - Interval 43Time (min)2345678923456789100100010000A-5-4-3-2-1012345CNet Gauge BH Pres (psi)A Closure Pressure = 3142 psi 0 Time = 06/17/25 07:10:15 111.000.0000.000Customer: CONOCOPHILLIPS NORTH SLOPE - EBUSJob Date: 17-Jun-2025Sales Order #: 0910128224Well Description: 3T-613 3T-613UWI: 50-103-20914-00Conoco Phillips - 3T-613 Interval 4 Plots87 <-Paste Interval 1 Plots HereTreatment Plot - Interval 56/17/202512:4012:5013:0013:1013:2013:306/17/202513:40Time010002000300040005000600070008000A0102030405060708090100B012345678910C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD43211514131211109876543211265Conoco Phillips - 3T-613 Interval 5 Plots88 <-Paste Interval 1 Plots HereADP Chemical Plots - Interval 56/17/202512:4012:5013:0013:1013:206/17/202513:30Time010203040A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)AB2115141312111098765432165Conoco Phillips - 3T-613 Interval 5 Plots89 <-Paste Interval 1 Plots HereBlender Chemical Plot - Interval 56/17/202512:4012:5013:0013:1013:206/17/202513:30Time0.00.51.01.52.02.53.0A0.00.51.01.52.02.5BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-II Conc (lb/Mgal)Optiflo-III Conc (lb/Mgal)MO-67 Conc (gal/Mgal)CL-28M BU Conc (gal/Mgal)BABAAA211514131211109876543211265Conoco Phillips - 3T-613 Interval 5 Plots90 <-Paste Interval 1 Plots HereNet Pressure Plot - Interval 5Time (min)2345678923456789100100010000A-5-4-3-2-1012345CNet Gauge BH Pres (psi)A Closure Pressure = 3142 psi 0 Time = 06/17/25 07:10:15 111.000.0000.000Customer: CONOCOPHILLIPS NORTH SLOPE - EBUSJob Date: 17-Jun-2025Sales Order #: 0910128224Well Description: 3T-613 3T-613UWI: 50-103-20914-00Conoco Phillips - 3T-613 Interval 5 Plots91 <-Paste Interval 1 Plots HereTreatment Plot - Interval 66/17/202513:3013:4013:5014:0014:1014:206/17/202514:30Time010002000300040005000600070008000A0102030405060708090100B012345678910C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD151413121110987654321156Conoco Phillips - 3T-613 Interval 6 Plots92 <-Paste Interval 1 Plots HereADP Chemical Plots - Interval 66/17/202513:3013:4013:5014:0014:106/17/202514:20Time010203040A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)AB1514131211109876543216Conoco Phillips - 3T-613 Interval 6 Plots93 <-Paste Interval 1 Plots HereBlender Chemical Plot - Interval 66/17/202513:3013:4013:5014:0014:106/17/202514:20Time0.00.51.01.52.02.53.0A0.00.51.01.52.02.5BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-II Conc (lb/Mgal)Optiflo-III Conc (lb/Mgal)MO-67 Conc (gal/Mgal)CL-28M BU Conc (gal/Mgal)BABAAA151413121110987654321156Conoco Phillips - 3T-613 Interval 6 Plots94 <-Paste Interval 1 Plots HereNet Pressure Plot - Interval 64Time (min)2345678923456789100100010000A-5-4-3-2-1012345CNet Gauge BH Pres (psi)A Closure Pressure = 3142 psi 0 Time = 06/17/25 07:10:15 111.000.0000.000Customer: CONOCOPHILLIPS NORTH SLOPE - EBUSJob Date: 17-Jun-2025Sales Order #: 0910128224Well Description: 3T-613 3T-613UWI: 50-103-20914-00Conoco Phillips - 3T-613 Interval 6 Plots95 <-Paste Interval 1 Plots HereTreatment Plot - Interval 76/18/202517:1017:2017:3017:4017:5018:006/18/202518:10Time010002000300040005000600070008000A0102030405060708090100B012345678910C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD321191817161514131211109876543187Conoco Phillips - 3T-613 Interval 7 Plots96 <-Paste Interval 1 Plots HereADP Chemical Plots - Interval 76/18/202517:1017:2017:3017:4017:506/18/202518:00Time010203040A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)AB21191817161514131211109876543187Conoco Phillips - 3T-613 Interval 7 Plots97 <-Paste Interval 1 Plots HereBlender Chemical Plot - Interval 76/18/202517:1017:2017:3017:4017:506/18/202518:00Time0.00.51.01.52.02.53.0A0.00.51.01.52.02.5BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-II Conc (lb/Mgal)Optiflo-III Conc (lb/Mgal)MO-67 Conc (gal/Mgal)CL-28M BU Conc (gal/Mgal)BABBAA1191817161514131211109876543187Conoco Phillips - 3T-613 Interval 7 Plots98 <-Paste Interval 1 Plots HereNet Pressure Plot - Interval 7Time (min)2345678923456789100100010000A-5-4-3-2-1012345CNet Gauge BH Pres (psi)A Closure Pressure = 3142 psi 0 Time = 06/18/25 14:59:58 150.950.0000.000Customer: CONOCOPHILLIPS NORTH SLOPE - EBUSJob Date: 18-Jun-2025Sales Order #: 0910128224Well Description: 3T-613 3T-613UWI: 50-103-20914-00Conoco Phillips - 3T-613 Interval 7 Plots99 <-Paste Interval 1 Plots HereADP Chemical Plots - Bucket Test 6.18.256/18/202515:2515:2615:2715:286/18/202515:29Time010203040A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)ABConoco Phillips - 3T-613 Interval 8 Plots100 <-Paste Interval 1 Plots HereBlender Chemical Plot - Bucket Test 6.18.256/18/202515:0215:0415:0615:0815:1015:126/18/202515:14Time0.00.51.01.52.02.53.0A0.00.51.01.52.02.5BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-II Conc (lb/Mgal)Optiflo-III Conc (lb/Mgal)MO-67 Conc (gal/Mgal)CL-28M BU Conc (gal/Mgal)BABBAAConoco Phillips - 3T-613 Interval 8 Plots101 <-Paste Interval 1 Plots HereePRV Test - 6.18.256/18/202515:5715:5815:5916:0016:0116:0216:036/18/202516:04Time01000200030004000500060007000Treating Pressure (psi)Treating Pressure @Pump (psi)I1 Global Kickout Pressure (psi)P2 Kickout Pressure (psi)Pop-off (psi)6543Global Event Log3456Intersection IntersectionePRV - Primary Tubing ePRV - Primary IAePRV - Secondary Tubing ePRV - Secondary IA15:57:43 16:00:4816:02:04 16:03:15TP TP1311 11442010 899.4TPP TPP1408 12172092 987.9IGKP IGKP1500 15002500 2500Conoco Phillips - 3T-613 Interval 8 Plots102 <-Paste Interval 1 Plots HerePressure Test - 6.18.256/18/202516:2616:2816:3016:3216:3416:366/18/202516:38Time010002000300040005000600070008000900010000Treating Pressure (psi)Treating Pressure @Pump (psi)I1 Global Kickout Pressure (psi)P2 Kickout Pressure (psi)Pop-off (psi)10987Global Event Log78910Intersection IntersectionTesting Globals Testing LocalsPressure Test - Max Pressure Test - Pass16:27:54 16:28:0116:29:35 16:34:55TP TP967.6 10019556 9511TPP TPP1024 10539604 9513IGKP IGKP25.00 95009500 9500PKP PKP500.4 509.39500 9500Customer: CONOCOPHILLIPS NORTH SLOPE - EBUSJob Date: 18-Jun-2025Sales Order #: 0910128224Well Description: 3T-613 3T-613UWI: 50-103-20914-00Conoco Phillips - 3T-613 Interval 8 Plots103 Treatment Plot - Interval 8 Attempt 16/18/202518:0018:0518:1018:1518:206/18/202518:25Time010002000300040005000600070008000A0102030405060708090100B012345678910C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD54321198Conoco Phillips - 3T-613 Interval 8 Plots104 ADP Chemical Plots - Interval 8 Attempt 16/18/202518:0018:0518:1018:1518:206/18/202518:25Time010203040A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)AB54321198Conoco Phillips - 3T-613 Interval 8 Plots105 Blender Chemical Plot - Interval 8 Attempt 16/18/202518:0018:0518:1018:1518:206/18/202518:25Time0.00.51.01.52.02.53.0A0.00.51.01.52.02.5BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-II Conc (lb/Mgal)Optiflo-III Conc (lb/Mgal)MO-67 Conc (gal/Mgal)CL-28M BU Conc (gal/Mgal)BABBAA543218Conoco Phillips - 3T-613 Interval 8 Plots106 Net Pressure Plot - Interval 8 Attempt 12Time (min)2345678923456789100100010000A-5-4-3-2-1012345CNet Gauge BH Pres (psi)A Closure Pressure = 3142 psi 0 Time = 06/18/25 14:59:58 150.950.0000.000Customer: CONOCOPHILLIPS NORTH SLOPE - EBUSJob Date: 18-Jun-2025Sales Order #: 0910128224Well Description: 3T-613 3T-613UWI: 50-103-20914-00Conoco Phillips - 3T-613 Interval 8 Plots107 ADP Chemical Plots - Bucket Test 6.19.256/19/202507:54:2007:54:3007:54:4007:54:5007:55:0007:55:1007:55:2007:55:306/19/202507:55:40Time010203040A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)ABConoco Phillips - 3T-613 Interval 8 Plots108 Blender Chemical Plot - Bucket Test 6.19.256/19/202508:1508:1608:1708:1808:1908:2008:216/19/202508:22Time0.00.51.01.52.02.53.0A0.00.51.01.52.02.5BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-II Conc (lb/Mgal)Optiflo-III Conc (lb/Mgal)MO-67 Conc (gal/Mgal)CL-28M BU Conc (gal/Mgal)BABBAAConoco Phillips - 3T-613 Interval 8 Plots109 ePRV Test - 6.19.256/19/202508:4208:4308:4408:4508:4608:4708:486/19/202508:49Time01000200030004000500060007000Treating Pressure (psi)Treating Pressure @Pump (psi)I1 Global Kickout Pressure (psi)P2 Kickout Pressure (psi)Pop-off (psi)6543Global Event Log3456Intersection IntersectionePRV - Primary Tubing ePRV - Primary IAePRV - Secondary Tubing ePRV - Secondary IA08:43:50 08:45:4008:47:25 08:48:43TP TP1636 10851135 1064TPP TPP1655 902.01187 1108IGKP IGKP2000 20002000 2000Conoco Phillips - 3T-613 Interval 8 Plots110 Pressure Test - 6.19.256/19/202508:5008:5208:5408:5608:586/19/202509:00Time010002000300040005000600070008000900010000Treating Pressure (psi)Treating Pressure @Pump (psi)I1 Global Kickout Pressure (psi)P2 Kickout Pressure (psi)Pop-off (psi)10987Global Event Log78910Intersection IntersectionTesting Globals Testing LocalsPressure Test - Max Pressure Test - Pass08:50:36 08:50:4108:52:53 08:58:17TP TP1101 11249521 9511TPP TPP1155 11809556 9528IGKP IGKP25.00 95009500 9500PKP PKP500.4 960.09500 9500Customer: CONOCOPHILLIPS NORTH SLOPE - EBUSJob Date: 19-Jun-2025Sales Order #: 0910128224Well Description: 3T-613 3T-613UWI: 50-103-20914-00Conoco Phillips - 3T-613 Interval 8 Plots111 Treatment Plot - Interval 8 Attempt 26/19/202510:0010:1010:2010:3010:4010:506/19/202511:00Time010002000300040005000600070008000A0102030405060708090100B012345678910C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD43211716151413121110987654198Conoco Phillips - 3T-613 Interval 8 Plots112 ADP Chemical Plots - Interval 8 Attempt 26/19/202510:1010:2010:3010:406/19/202510:50Time010203040A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)AB2117161514131211109876549Conoco Phillips - 3T-613 Interval 8 Plots113 Blender Chemical Plot - Interval 2 Attempt 26/16/202517:0017:2017:4018:006/16/202518:20Time0.00.51.01.52.02.53.0A0.00.51.01.52.02.5BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-II Conc (lb/Mgal)Optiflo-III Conc (lb/Mgal)MO-67 Conc (gal/Mgal)CL-28M BU Conc (gal/Mgal)BABBAA1716151413121110987Conoco Phillips - 3T-613 Interval 8 Plots114 Net Pressure Plot - Interval 8 Attempt 22Time (min)2345678923456789100100010000A-5-4-3-2-1012345CNet Gauge BH Pres (psi)A Closure Pressure = 3265 psi 0 Time = 06/19/25 07:30:28 150.950.0000.000Customer: CONOCOPHILLIPS NORTH SLOPE - EBUSJob Date: 19-Jun-2025Sales Order #: 0910128224Well Description: 3T-613 3T-613UWI: 50-103-20914-00Conoco Phillips - 3T-613 Interval 8 Plots115 <-Paste Interval 1 Plots HereTreatment Plot - Interval 96/19/202511:0011:1011:2011:3011:4011:506/19/202512:00Time010002000300040005000600070008000A0102030405060708090100B012345678910C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD432115141312111098765432117109Conoco Phillips - 3T-613 Interval 9 Plots116 <-Paste Interval 1 Plots HereADP Chemical Plots - Interval 96/19/202511:0011:1011:2011:3011:406/19/202511:50Time010203040A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)AB321151413121110987654321109Conoco Phillips - 3T-613 Interval 9 Plots117 <-Paste Interval 1 Plots HereBlender Chemical Plot - Interval 96/19/202510:5011:0011:1011:2011:3011:406/19/202511:50Time0.00.51.01.52.02.53.0A0.00.51.01.52.02.5BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-II Conc (lb/Mgal)Optiflo-III Conc (lb/Mgal)MO-67 Conc (gal/Mgal)CL-28M BU Conc (gal/Mgal)BAABAA43211514131211109876543211716109Conoco Phillips - 3T-613 Interval 9 Plots118 <-Paste Interval 1 Plots HereNet Pressure Plot - Interval 9Time (min)2345678923456789100100010000A-5-4-3-2-1012345CNet Gauge BH Pres (psi)A Closure Pressure = 3265 psi 0 Time = 06/19/25 07:30:28 150.950.0000.000Customer: CONOCOPHILLIPS NORTH SLOPE - EBUSJob Date: 19-Jun-2025Sales Order #: 0910128224Well Description: 3T-613 3T-613UWI: 50-103-20914-00Conoco Phillips - 3T-613 Interval 9 Plots119 <-Paste Interval 1 Plots HereTreatment Plot - Interval 106/19/202511:5012:0012:1012:2012:3012:406/19/202512:50Time010002000300040005000600070008000A0102030405060708090100B012345678910C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD4321151413121110987654321151110Conoco Phillips - 3T-613 Interval 10 Plots120 <-Paste Interval 1 Plots HereADP Chemical Plots - Interval 106/19/202511:5012:0012:1012:2012:306/19/202512:40Time010203040A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)AB21151413121110987654321151110Conoco Phillips - 3T-613 Interval 10 Plots121 <-Paste Interval 1 Plots HereBlender Chemical Plot - Interval 106/19/202511:5012:0012:1012:2012:306/19/202512:40Time0.00.51.01.52.02.53.0A0.00.51.01.52.02.5BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-II Conc (lb/Mgal)Optiflo-III Conc (lb/Mgal)MO-67 Conc (gal/Mgal)CL-28M BU Conc (gal/Mgal)BAABAA321151413121110987654321151110Conoco Phillips - 3T-613 Interval 10 Plots122 <-Paste Interval 1 Plots HereNet Pressure Plot - Interval 103Time (min)2345678923456789100100010000A-5-4-3-2-1012345CNet Gauge BH Pres (psi)A Closure Pressure = 3265 psi 0 Time = 06/19/25 07:30:28 150.950.0000.000Customer: CONOCOPHILLIPS NORTH SLOPE - EBUSJob Date: 19-Jun-2025Sales Order #: 0910128224Well Description: 3T-613 3T-613UWI: 50-103-20914-00Conoco Phillips - 3T-613 Interval 10 Plots123 <-Paste Interval 1 Plots HereTreatment Plot - Interval 116/19/202512:4012:5013:0013:1013:2013:306/19/202513:40Time010002000300040005000600070008000A0102030405060708090100B012345678910C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD4321151413121110987654321151211Conoco Phillips - 3T-613 Interval 11 Plots124 <-Paste Interval 1 Plots HereADP Chemical Plots - Interval 116/19/202512:4012:5013:0013:1013:206/19/202513:30Time010203040A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)AB21151413121110987654321151211Conoco Phillips - 3T-613 Interval 11 Plots125 <-Paste Interval 1 Plots HereBlender Chemical Plot - Interval 116/19/202512:4012:5013:0013:1013:206/19/202513:30Time0.00.51.01.52.02.53.0A0.00.51.01.52.02.5BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-II Conc (lb/Mgal)Optiflo-III Conc (lb/Mgal)MO-67 Conc (gal/Mgal)CL-28M BU Conc (gal/Mgal)BAABAA21151413121110987654321151211Conoco Phillips - 3T-613 Interval 11 Plots126 <-Paste Interval 1 Plots HereNet Pressure Plot - Interval 11Time (min)2345678923456789100100010000A-5-4-3-2-1012345CNet Gauge BH Pres (psi)A Closure Pressure = 3265 psi 0 Time = 06/19/25 07:30:28 150.950.0000.000Customer: CONOCOPHILLIPS NORTH SLOPE - EBUSJob Date: 19-Jun-2025Sales Order #: 0910128224Well Description: 3T-613 3T-613UWI: 50-103-20914-00Conoco Phillips - 3T-613 Interval 11 Plots127 <-Paste Interval 1 Plots HereTreatment Plot - Interval 126/19/202513:3013:4013:5014:0014:1014:206/19/202514:30Time010002000300040005000600070008000A0102030405060708090100B012345678910C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD4321151413121110987654321151312Conoco Phillips - 3T-613 Interval 12 Plots128 <-Paste Interval 1 Plots HereADP Chemical Plots - Interval 126/19/202513:4013:5014:0014:106/19/202514:20Time010203040A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)AB11514131211109876543211312Conoco Phillips - 3T-613 Interval 12 Plots129 <-Paste Interval 1 Plots HereBlender Chemical Plot - Interval 126/19/202513:4013:5014:0014:106/19/202514:20Time0.00.51.01.52.02.53.0A0.00.51.01.52.02.5BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-II Conc (lb/Mgal)Optiflo-III Conc (lb/Mgal)MO-67 Conc (gal/Mgal)CL-28M BU Conc (gal/Mgal)BAABAA21151413121110987654321151312Conoco Phillips - 3T-613 Interval 12 Plots130 <-Paste Interval 1 Plots HereNet Pressure Plot - Interval 124Time (min)2345678923456789100100010000A-5-4-3-2-1012345CNet Gauge BH Pres (psi)A Closure Pressure = 3265 psi 0 Time = 06/19/25 07:30:28 150.950.0000.000Customer: CONOCOPHILLIPS NORTH SLOPE - EBUSJob Date: 19-Jun-2025Sales Order #: 0910128224Well Description: 3T-613 3T-613UWI: 50-103-20914-00Conoco Phillips - 3T-613 Interval 12 Plots131 <-Paste Interval 1 Plots HereTreatment Plot - Interval 136/19/202514:3014:4014:5015:0015:106/19/202515:20Time010002000300040005000600070008000A0102030405060708090100B012345678910C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD1514131211109876543211513Conoco Phillips - 3T-613 Interval 13 Plots132 <-Paste Interval 1 Plots HereADP Chemical Plots - Interval 136/19/202514:3014:4014:5015:0015:106/19/202515:20Time010203040A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)AB15141312111098765432113Conoco Phillips - 3T-613 Interval 13 Plots133 <-Paste Interval 1 Plots HereBlender Chemical Plot - Interval 136/19/202514:3014:4014:5015:0015:106/19/202515:20Time0.00.51.01.52.02.53.0A0.00.51.01.52.02.5BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-II Conc (lb/Mgal)Optiflo-III Conc (lb/Mgal)MO-67 Conc (gal/Mgal)CL-28M BU Conc (gal/Mgal)BAABAA1514131211109876543211513Conoco Phillips - 3T-613 Interval 13 Plots134 <-Paste Interval 1 Plots HereNet Pressure Plot - Interval 13Time (min)2345678923456789100100010000A-5-4-3-2-1012345CNet Gauge BH Pres (psi)A Closure Pressure = 3265 psi 0 Time = 06/19/25 07:30:28 150.950.0000.000Customer: CONOCOPHILLIPS NORTH SLOPE - EBUSJob Date: 19-Jun-2025Sales Order #: 0910128224Well Description: 3T-613 3T-613UWI: 50-103-20914-00Conoco Phillips - 3T-613 Interval 13 Plots135 <-Paste Interval 1 Plots HereADP Chemical Plots - Bucket Test 6.20.256/20/202506:5206:5306:5406:5506:566/20/202506:57Time010203040A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)ABConoco Phillips - 3T-613 Interval 14 Plots136 <-Paste Interval 1 Plots HereBlender Chemical Plot - Bucket Test 6.20.256/20/202506:5006:5507:006/20/202507:05Time0.00.51.01.52.02.53.0A0.00.51.01.52.02.5BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-II Conc (lb/Mgal)Optiflo-III Conc (lb/Mgal)MO-67 Conc (gal/Mgal)CL-28M BU Conc (gal/Mgal)BAABAA2Conoco Phillips - 3T-613 Interval 14 Plots137 <-Paste Interval 1 Plots HereePRV Test - 6.20.256/20/202508:5608:5708:5808:5909:0009:016/20/202509:02Time01000200030004000500060007000Treating Pressure (psi)Treating Pressure @Pump (psi)I1 Global Kickout Pressure (psi)P2 Kickout Pressure (psi)Pop-off (psi)7654Global Event Log4567Intersection IntersectionePRV - Primary Tubing ePRV - Primary IAePRV - Secondary Tubing ePRV - Secondary IA08:56:44 08:58:0908:59:52 09:01:12TP TP995.5 698.91108 988.8TPP TPP1137 849.61258 1069IGKP IGKP1500 15001500 1500Conoco Phillips - 3T-613 Interval 14 Plots138 <-Paste Interval 1 Plots HerePressure Test - 6.20.256/20/202509:0409:0609:0809:106/20/202509:12Time010002000300040005000600070008000900010000Treating Pressure (psi)Treating Pressure @Pump (psi)I1 Global Kickout Pressure (psi)P2 Kickout Pressure (psi)Pop-off (psi)111098Global Event Log891011Intersection IntersectionTesting Globals Testing LocalsPressure Test - Max Pressure Test - Pass09:03:54 09:04:0109:06:04 09:12:28TP TP871.7 870.49535 9478TPP TPP719.7 735.59657 9587IGKP IGKP25.00 95009500 9500PKP PKP500.4 712.09500 9500Customer: CONOCOPHILLIPS NORTH SLOPE - EBUSJob Date: 20-Jun-2025Sales Order #: 0910128224Well Description: 3T-613 3T-613UWI: 50-103-20914-00Conoco Phillips - 3T-613 Interval 14 Plots139 Treatment Plot - Interval 14 - DFIT6/20/202509:3009:3509:4009:4509:506/20/202509:55Time010002000300040005000600070008000A0102030405060708090100B012345678910C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD6542114Conoco Phillips - 3T-613 Interval 14 Plots140 ADP Chemical Plots - Interval 14 - DFIT6/20/202509:3509:4009:456/20/202509:50Time010203040A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)AB65Conoco Phillips - 3T-613 Interval 14 Plots141 Blender Chemical Plot - Interval 14 - DFIT6/20/202509:3509:4009:456/20/202509:50Time0.00.51.01.52.02.53.0A0.00.51.01.52.02.5BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-II Conc (lb/Mgal)Optiflo-III Conc (lb/Mgal)MO-67 Conc (gal/Mgal)CL-28M BU Conc (gal/Mgal)BAABAA65Conoco Phillips - 3T-613 Interval 14 Plots142 Net Pressure Plot - Interval 14 - DFITTime (min)2345678923456789100100010000A-5-4-3-2-1012345CNet Gauge BH Pres (psi)A Closure Pressure = 2854 psi 0 Time = 06/20/25 06:43:54 150.950.0000.000Customer: CONOCOPHILLIPS NORTH SLOPE - EBUSJob Date: 20-Jun-2025Sales Order #: 0910128224Well Description: 3T-613 3T-613UWI: 50-103-20914-00Conoco Phillips - 3T-613 Interval 14 Plots143 Treatment Plot - Interval 146/20/202510:5011:0011:1011:2011:3011:406/20/202511:50Time010002000300040005000600070008000A0102030405060708090100B012345678910C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD32121201918171615141312111098715Conoco Phillips - 3T-613 Interval 14 Plots144 ADP Chemical Plots - Interval 146/20/202510:5011:0011:1011:2011:306/20/202511:40Time010203040A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)AB1212019181716151413121110915Conoco Phillips - 3T-613 Interval 14 Plots145 Blender Chemical Plot - Interval 146/20/202510:5011:0011:1011:2011:306/20/202511:40Time0.00.51.01.52.02.53.0A0.00.51.01.52.02.5BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-II Conc (lb/Mgal)Optiflo-III Conc (lb/Mgal)MO-67 Conc (gal/Mgal)CL-28M BU Conc (gal/Mgal)BAABAA21212019181716151413121110915Conoco Phillips - 3T-613 Interval 14 Plots146 Net Pressure Plot - Interval 143Time (min)2345678923456789100100010000A-5-4-3-2-1012345CNet Gauge BH Pres (psi)A Closure Pressure = 2854 psi 0 Time = 06/20/25 06:43:54 150.950.0000.000Customer: CONOCOPHILLIPS NORTH SLOPE - EBUSJob Date: 20-Jun-2025Sales Order #: 0910128224Well Description: 3T-613 3T-613UWI: 50-103-20914-00Conoco Phillips - 3T-613 Interval 14 Plots147 <-Paste Interval 1 Plots HereTreatment Plot - Interval 156/20/202511:4011:5012:0012:1012:2012:306/20/202512:40Time010002000300040005000600070008000A0102030405060708090100B012345678910C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD321151413121110987654321211615Conoco Phillips - 3T-613 Interval 15 Plots148 <-Paste Interval 1 Plots HereADP Chemical Plots - Interval 156/20/202511:4011:5012:0012:1012:206/20/202512:30Time010203040A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)AB211514131211109876543211615Conoco Phillips - 3T-613 Interval 15 Plots149 <-Paste Interval 1 Plots HereBlender Chemical Plot - Interval 156/20/202511:4011:5012:0012:1012:206/20/202512:30Time0.00.51.01.52.02.53.0A0.00.51.01.52.02.5BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-II Conc (lb/Mgal)Optiflo-III Conc (lb/Mgal)MO-67 Conc (gal/Mgal)CL-28M BU Conc (gal/Mgal)BAABAA211514131211109876543211615Conoco Phillips - 3T-613 Interval 15 Plots150 <-Paste Interval 1 Plots HereNet Pressure Plot - Interval 153Time (min)2345678923456789100100010000A-5-4-3-2-1012345CNet Gauge BH Pres (psi)A Closure Pressure = 2854 psi 0 Time = 06/20/25 06:43:54 150.950.0000.000Customer: CONOCOPHILLIPS NORTH SLOPE - EBUSJob Date: 20-Jun-2025Sales Order #: 0910128224Well Description: 3T-613 3T-613UWI: 50-103-20914-00Conoco Phillips - 3T-613 Interval 15 Plots151 <-Paste Interval 1 Plots HereTreatment Plot - Interval 166/20/202512:4012:5013:0013:1013:2013:306/20/202513:40Time010002000300040005000600070008000A0102030405060708090100B012345678910C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD321151413121110987654321151716Conoco Phillips - 3T-613 Interval 16 Plots152 <-Paste Interval 1 Plots HereADP Chemical Plots - Interval 166/20/202512:4012:5013:0013:1013:206/20/202513:30Time010203040A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)AB211514131211109876543211716Conoco Phillips - 3T-613 Interval 16 Plots153 <-Paste Interval 1 Plots HereBlender Chemical Plot - Interval 166/20/202512:4012:5013:0013:1013:206/20/202513:30Time0.00.51.01.52.02.53.0A0.00.51.01.52.02.5BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-II Conc (lb/Mgal)Optiflo-III Conc (lb/Mgal)MO-67 Conc (gal/Mgal)CL-28M BU Conc (gal/Mgal)BAABAA21151413121110987654321151716Conoco Phillips - 3T-613 Interval 16 Plots154 <-Paste Interval 1 Plots HereNet Pressure Plot - Interval 164Time (min)2345678923456789100100010000A-5-4-3-2-1012345CNet Gauge BH Pres (psi)A Closure Pressure = 2854 psi 0 Time = 06/20/25 06:43:54 150.950.0000.000Customer: CONOCOPHILLIPS NORTH SLOPE - EBUSJob Date: 20-Jun-2025Sales Order #: 0910128224Well Description: 3T-613 3T-613UWI: 50-103-20914-00Conoco Phillips - 3T-613 Interval 16 Plots155 <-Paste Interval 1 Plots HereTreatment Plot - Interval 176/20/202513:3013:4013:5014:0014:1014:206/20/202514:30Time010002000300040005000600070008000A0102030405060708090100B012345678910C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD21151413121110987654321151817Conoco Phillips - 3T-613 Interval 17 Plots156 <-Paste Interval 1 Plots HereADP Chemical Plots - Interval 176/20/202513:3013:4013:5014:0014:106/20/202514:20Time010203040A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)AB11514131211109876543211817Conoco Phillips - 3T-613 Interval 17 Plots157 <-Paste Interval 1 Plots HereBlender Chemical Plot - Interval 176/20/202513:3013:4013:5014:0014:106/20/202514:20Time0.00.51.01.52.02.53.0A0.00.51.01.52.02.5BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-II Conc (lb/Mgal)Optiflo-III Conc (lb/Mgal)MO-67 Conc (gal/Mgal)CL-28M BU Conc (gal/Mgal)BAABAA1151413121110987654321151817Conoco Phillips - 3T-613 Interval 17 Plots158 <-Paste Interval 1 Plots HereNet Pressure Plot - Interval 17Time (min)2345678923456789100100010000A-5-4-3-2-1012345CNet Gauge BH Pres (psi)A Closure Pressure = 2854 psi 0 Time = 06/20/25 06:43:54 150.950.0000.000Customer: CONOCOPHILLIPS NORTH SLOPE - EBUSJob Date: 20-Jun-2025Sales Order #: 0910128224Well Description: 3T-613 3T-613UWI: 50-103-20914-00Conoco Phillips - 3T-613 Interval 17 Plots159 <-Paste Interval 1 Plots HereTreatment Plot - Interval 18 - DFIT6/20/202514:3214:3414:3614:3814:4014:426/20/202514:44Time010002000300040005000600070008000A0102030405060708090100B012345678910C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD2Conoco Phillips - 3T-613 Interval 18 Plots160 <-Paste Interval 1 Plots HereADP Chemical Plots - Interval 18 - DFIT6/20/202514:2614:2814:3014:3214:3414:366/20/202514:38Time010203040A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)AB2118Conoco Phillips - 3T-613 Interval 18 Plots161 <-Paste Interval 1 Plots HereBlender Chemical Plot - Interval 18 - DFIT6/20/202514:2614:2814:3014:3214:3414:366/20/202514:38Time0.00.51.01.52.02.53.0A0.00.51.01.52.02.5BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-II Conc (lb/Mgal)Optiflo-III Conc (lb/Mgal)MO-67 Conc (gal/Mgal)CL-28M BU Conc (gal/Mgal)BAABAA211518Conoco Phillips - 3T-613 Interval 18 Plots162 <-Paste Interval 1 Plots HereNet Pressure Plot - Interval 18 - DFITTime (min)2345678923456789100100010000A-5-4-3-2-1012345CNet Gauge BH Pres (psi)A Closure Pressure = 2854 psi 0 Time = 06/20/25 06:43:54 150.950.0000.000Customer: CONOCOPHILLIPS NORTH SLOPE - EBUSJob Date: 20-Jun-2025Sales Order #: 0910128224Well Description: 3T-613 3T-613UWI: 50-103-20914-00Conoco Phillips - 3T-613 Interval 18 Plots163 Treatment Plot - Interval 186/20/202515:1015:2015:3015:4015:5016:006/20/202516:10Time010002000300040005000600070008000A0102030405060708090100B012345678910C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD321171615141312111098765419Conoco Phillips - 3T-613 Interval 18 Plots164 ADP Chemical Plots - Interval 186/20/202515:1015:2015:3015:4015:506/20/202516:00Time010203040A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)AB21171615141312111098765419Conoco Phillips - 3T-613 Interval 18 Plots165 Blender Chemical Plot - Interval 186/20/202515:1015:2015:3015:4015:506/20/202516:00Time0.00.51.01.52.02.53.0A0.00.51.01.52.02.5BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-II Conc (lb/Mgal)Optiflo-III Conc (lb/Mgal)MO-67 Conc (gal/Mgal)CL-28M BU Conc (gal/Mgal)BAABAA21171615141312111098765419Conoco Phillips - 3T-613 Interval 18 Plots166 Net Pressure Plot - Interval 18Time (min)2345678923456789100100010000A-5-4-3-2-1012345CNet Gauge BH Pres (psi)A Closure Pressure = 2854 psi 0 Time = 06/20/25 06:43:54 150.950.0000.000Customer: CONOCOPHILLIPS NORTH SLOPE - EBUSJob Date: 20-Jun-2025Sales Order #: 0910128224Well Description: 3T-613 3T-613UWI: 50-103-20914-00Conoco Phillips - 3T-613 Interval 18 Plots167 <-Paste Interval 1 Plots HereTreatment Plot - Interval 196/20/202516:1016:2016:3016:4016:506/20/202517:00Time010002000300040005000600070008000A0102030405060708090100B012345678910C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD1514131211109876543211719Conoco Phillips - 3T-613 Interval 19 Plots168 <-Paste Interval 1 Plots HereADP Chemical Plots - Interval 196/20/202516:1016:2016:3016:4016:506/20/202517:00Time010203040A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)AB15141312111098765432119Conoco Phillips - 3T-613 Interval 19 Plots169 <-Paste Interval 1 Plots HereBlender Chemical Plot - Interval 196/20/202516:1016:2016:3016:4016:506/20/202517:00Time0.00.51.01.52.02.53.0A0.00.51.01.52.02.5BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-II Conc (lb/Mgal)Optiflo-III Conc (lb/Mgal)MO-67 Conc (gal/Mgal)CL-28M BU Conc (gal/Mgal)BAABAA1514131211109876543211719Conoco Phillips - 3T-613 Interval 19 Plots170 <-Paste Interval 1 Plots HereNet Pressure Plot - Interval 196Time (min)2345678923456789100100010000A-5-4-3-2-1012345CNet Gauge BH Pres (psi)A Closure Pressure = 2854 psi 0 Time = 06/20/25 06:43:54 150.950.0000.000Customer: CONOCOPHILLIPS NORTH SLOPE - EBUSJob Date: 20-Jun-2025Sales Order #: 0910128224Well Description: 3T-613 3T-613UWI: 50-103-20914-00Conoco Phillips - 3T-613 Interval 19 Plots171 <-Paste Interval 1 Plots HereADP Chemical Plots - Bucket Test 6.21.256/21/202506:5306:5406:5506:566/21/202506:57Time010203040A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)ABConoco Phillips - 3T-613 Interval 20 Plots172 <-Paste Interval 1 Plots HereBlender Chemical Plot - Bucket Test 6.21.256/21/202506:4506:5006:5507:0007:0507:106/21/202507:15Time0.00.51.01.52.02.53.0A0.00.51.01.52.02.5BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-II Conc (lb/Mgal)Optiflo-III Conc (lb/Mgal)MO-67 Conc (gal/Mgal)CL-28M BU Conc (gal/Mgal)BAABAA1Conoco Phillips - 3T-613 Interval 20 Plots173 <-Paste Interval 1 Plots HereePRV Test - 6.21.256/21/202507:3307:3407:3507:3607:376/21/202507:38Time01000200030004000500060007000Treating Pressure (psi)Treating Pressure @Pump (psi)I1 Global Kickout Pressure (psi)P2 Kickout Pressure (psi)Pop-off (psi)6543Global Event Log3456Intersection IntersectionePRV - Primary Tubing ePRV - Primary IAePRV - Secondary Tubing ePRV - Secondary IA07:33:43 07:34:5307:36:22 07:37:33TP TP733.9 824.8718.1 698.9TPP TPP855.8 956.1646.2 615.4IGKP IGKP1500 15001500 1500Conoco Phillips - 3T-613 Interval 20 Plots174 <-Paste Interval 1 Plots HerePressure Test - 6.21.256/21/202507:4007:4207:4407:4607:486/21/202507:50Time010002000300040005000600070008000900010000Treating Pressure (psi)Treating Pressure @Pump (psi)I1 Global Kickout Pressure (psi)P2 Kickout Pressure (psi)Pop-off (psi)10987Global Event Log78910Intersection IntersectionTesting Globals Testing LocalsPressure Test - Max Pressure Test - Pass07:40:26 07:40:3307:42:34 07:49:23TP TP738.7 752.79498 9468TPP TPP857.1 870.89649 9567IGKP IGKP25.00 95009500 9500PKP PKP500.4 841.89500 9500Customer: CONOCOPHILLIPS NORTH SLOPE - EBUSJob Date: 21-Jun-2025Sales Order #: 0910128224Well Description: 3T-613 3T-613UWI: 50-103-20914-00Conoco Phillips - 3T-613 Interval 20 Plots175 Treatment Plot - Interval 20 - Minifrac6/21/202509:2009:3009:406/21/202509:50Time010002000300040005000600070008000A0102030405060708090100B012345678910C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD876541420Conoco Phillips - 3T-613 Interval 20 Plots176 ADP Chemical Plots - Interval 20 - Minifrac6/21/202509:1509:2009:2509:3009:3509:4009:456/21/202509:50Time010203040A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)AB876541420Conoco Phillips - 3T-613 Interval 20 Plots177 Blender Chemical Plot - Interval 20 - Minifrac6/21/202509:1009:1509:2009:2509:3009:3509:4009:456/21/202509:50Time0.00.51.01.52.02.53.0A0.00.51.01.52.02.5BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-II Conc (lb/Mgal)Optiflo-III Conc (lb/Mgal)MO-67 Conc (gal/Mgal)CL-28M BU Conc (gal/Mgal)BAABAA876541420Conoco Phillips - 3T-613 Interval 20 Plots178 Net Pressure Plot - Interval 20 - MinifracTime (min)2345678923456789100100010000A-5-4-3-2-1012345CNet Gauge BH Pres (psi)A Closure Pressure = 2854 psi 0 Time = 06/21/25 06:44:26 150.950.0000.000Customer: CONOCOPHILLIPS NORTH SLOPE - EBUSJob Date: 21-Jun-2025Sales Order #: 0910128224Well Description: 3T-613 3T-613UWI: 50-103-20914-00Conoco Phillips - 3T-613 Interval 20 Plots179 Treatment Plot - Interval 206/21/202512:1012:2012:3012:4012:5013:0013:1013:206/21/202513:30Time010002000300040005000600070008000A0102030405060708090100B012345678910C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD3211918171615141312111021Conoco Phillips - 3T-613 Interval 20 Plots180 ADP Chemical Plots - Interval 206/21/202512:1012:2012:3012:4012:5013:0013:106/21/202513:20Time010203040A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)AB211918171615141312111021Conoco Phillips - 3T-613 Interval 20 Plots181 Blender Chemical Plot - Interval 206/21/202512:1012:2012:3012:4012:5013:0013:106/21/202513:20Time0.00.51.01.52.02.53.0A0.00.51.01.52.02.5BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-II Conc (lb/Mgal)Optiflo-III Conc (lb/Mgal)MO-67 Conc (gal/Mgal)CL-28M BU Conc (gal/Mgal)BAABAA211918171615141312111021Conoco Phillips - 3T-613 Interval 20 Plots182 Net Pressure Plot - Interval 204Time (min)2345678923456789100100010000A-5-4-3-2-1012345CNet Gauge BH Pres (psi)A Closure Pressure = 2854 psi 0 Time = 06/21/25 06:44:26 150.950.0000.000Customer: CONOCOPHILLIPS NORTH SLOPE - EBUSJob Date: 21-Jun-2025Sales Order #: 0910128224Well Description: 3T-613 3T-613UWI: 50-103-20914-00Conoco Phillips - 3T-613 Interval 20 Plots183 <-Paste Interval 1 Plots HereTreatment Plot - Interval 21 - Minifrac6/21/202513:2513:3013:3513:406/21/202513:45Time010002000300040005000600070008000A0102030405060708090100B012345678910C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD432121Conoco Phillips - 3T-613 Interval 21 Plots184 <-Paste Interval 1 Plots HereADP Chemical Plots - Interval 21 - Minifrac6/21/202513:2513:3013:356/21/202513:40Time010203040A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)AB432121Conoco Phillips - 3T-613 Interval 21 Plots185 <-Paste Interval 1 Plots HereBlender Chemical Plot - Interval 21 - Minifrac6/21/202513:2513:3013:356/21/202513:40Time0.00.51.01.52.02.53.0A0.00.51.01.52.02.5BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-II Conc (lb/Mgal)Optiflo-III Conc (lb/Mgal)MO-67 Conc (gal/Mgal)CL-28M BU Conc (gal/Mgal)BAABAA432121Conoco Phillips - 3T-613 Interval 21 Plots186 <-Paste Interval 1 Plots HereNet Pressure Plot - Interval 21 - MinifracTime (min)2345678923456789100100010000A-5-4-3-2-1012345CNet Gauge BH Pres (psi)A Closure Pressure = 2854 psi 0 Time = 06/21/25 06:44:26 150.950.0000.000Customer: CONOCOPHILLIPS NORTH SLOPE - EBUSJob Date: 21-Jun-2025Sales Order #: 0910128224Well Description: 3T-613 3T-613UWI: 50-103-20914-00Conoco Phillips - 3T-613 Interval 21 Plots187 Treatment Plot - Interval 216/21/202514:5014:5515:0015:0515:1015:156/21/202515:20Time010002000300040005000600070008000A0102030405060708090100B012345678910C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD1514131211109876Conoco Phillips - 3T-613 Interval 21 Plots188 ADP Chemical Plots - Interval 216/21/202514:5014:5515:0015:0515:106/21/202515:15Time010203040A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)AB1514131211109876Conoco Phillips - 3T-613 Interval 21 Plots189 Blender Chemical Plot - Interval 216/21/202514:5014:5515:0015:0515:1015:156/21/202515:20Time0.00.51.01.52.02.53.0A0.00.51.01.52.02.5BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-II Conc (lb/Mgal)Optiflo-III Conc (lb/Mgal)MO-67 Conc (gal/Mgal)CL-28M BU Conc (gal/Mgal)BAABAA1514131211109876Conoco Phillips - 3T-613 Interval 21 Plots190 Net Pressure Plot - Interval 215Time (min)2345678923456789100100010000A-5-4-3-2-1012345CNet Gauge BH Pres (psi)A Closure Pressure = 2854 psi 0 Time = 06/21/25 06:44:26 150.950.0000.000Customer: CONOCOPHILLIPS NORTH SLOPE - EBUSJob Date: 21-Jun-2025Sales Order #: 0910128224Well Description: 3T-613 3T-613UWI: 50-103-20914-00Conoco Phillips - 3T-613 Interval 21 Plots191 Sales Order# - - - - - - - - - - Real Time QC Event Log Sand Sieve Analysis Fann 15 Minute Test Water Straps Planned Design Stimulation Treatment Appendix Well Summary Chemical Summary Prejob Break Test Water Analysis Prepared for: Chad Burkett June 22, 2025 Harrison Bay County, AK 910128224 Conoco Phillips 3T-613 Intervals 1-21 Moraine Moraine Formation API: 50-103-20914 Conoco Phillips - 3T-613 Appendix 1 CUSTOMERConoco Phillips FALSEAPIBFD (lb/gal)8.48LAT 70.42061242LEASE3T-613SALES ORDERBHST (°F)139LONG-150.266098FORMATIONMoraineDATE Max Pressure (psi)8500*Exceeds 80% of burst pressure*Prop Slurry Design Clean Design Clean Design Slurry Design Prop Stage Interval CL-28M BC-140X2 Losurf-300D MO-67 WG-36 OPTIFLO-III OPTIFLO-IIBE-6Treatment Stage Fluid Stage Proppant Conc Rate Volume Volume Volume Total Time TimeCrosslinker Crosslinker Surfactant Buffer Gel Breaker Breaker BiocideInterval Number Description Description Description(ppg) (bpm) (gal) (bbl) (bbl) (lbs) (hh:mm:ss) (hh:mm:ss)(gpt) (gpt) (gpt) (gpt) (ppt) (ppt) (ppt) (ppt)1-1 Shut-In Shut-In1:42:16 1-2 Freeze Protect Prime Up Pressure Test 5 1,000 24 24 0:04:46 1:42:16 1-3 Shut-In Shut-In1:37:30 1-4 30# Linear Pre-Pad 10 2,100 50 50 0:05:00 1:37:30 1.00 30.00 2.00 2.00 0.151-5 30# Linear DFIT 10 1,680 40 40 0:04:00 1:32:30 1.00 30.00 2.00 2.00 0.151-6 Shut-In Shut-In1:28:30 1-7 30# Linear Step Rate Test 15 8,400 200 200 0:13:20 1:28:30 1.00 30.00 2.00 2.00 0.151-8 30# Hybor G-i Establish Stable Fluid 15 8,400 200 200 0:13:20 1:15:10 1.00 0.25 1.00 0.70 30.00 2.00 2.00 0.151-9 30# Hybor G-i Pad 37 16,030 382 382 0:10:19 1:01:50 1.00 0.25 1.00 0.70 30.00 2.00 2.00 0.151-10 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:51:31 1.00 0.25 1.00 0.70 30.00 2.00 2.00 0.151-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 10,200 243 254 10,200 0:06:52 0:43:43 1.00 0.25 1.00 0.70 30.00 2.00 2.000.151-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 13,600 324 353 27,200 0:09:33 0:36:51 1.00 0.25 1.00 0.70 30.00 2.00 2.000.151-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 13,600 324 367 40,800 0:09:57 0:27:18 1.00 0.25 1.00 0.70 30.00 2.00 2.000.151-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 8,500 202 238 34,000 0:06:28 0:17:21 1.00 0.25 1.00 0.70 30.00 2.00 2.00 0.151-15 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 6,800 162 194 30,600 0:05:16 0:10:53 1.00 0.25 1.00 0.70 30.00 2.00 2.00 0.151-16 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 5,440 130 158 27,200 0:04:18 0:05:37 1.00 0.25 1.00 0.70 30.00 2.00 2.00 0.151-17 30# Linear Spacer and Dart Drop 37 2,041 49 49 0:01:19 0:01:19 1.00 30.00 2.00 2.00 0.152-1 30# Linear Pre-Pad 37 2,100 50 50 0:01:21 1:51:04 1.00 30.00 2.00 2.00 0.152-2 30# Hybor G-i Establish Stable Fluid 37 2,100 50 50 0:01:21 1:49:43 1.00 0.25 1.00 0.70 30.00 2.00 2.00 0.152-3 30# Hybor G-i Pad 37 15,500 369 369 0:09:58 1:48:22 1.00 0.25 1.00 0.70 30.00 2.00 2.00 0.152-4 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 1:38:24 1.00 0.25 1.00 0.70 30.00 2.00 2.00 0.152-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 10,200 243 254 10,200 0:06:52 1:30:35 1.00 0.25 1.00 0.70 30.00 2.00 2.00 0.152-6 30# Linear Flush 37 15,145 361 361 0:09:45 1:23:43 1.00 30.00 2.00 2.00 0.152-7 30# Hybor G-i Establish Stable Fluid 37 2,100 50 50 0:01:21 1:13:58 1.00 0.25 1.00 0.70 30.00 2.00 2.00 0.152-8 30# Hybor G-i Pad 37 15,500 369 369 0:09:58 1:12:37 1.00 0.25 1.00 0.70 30.00 2.00 2.00 0.152-9 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 1:02:39 1.00 0.25 1.00 0.70 30.00 2.00 2.00 0.152-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 10,200 243 254 10,200 0:06:52 0:54:50 1.00 0.25 1.00 0.70 30.00 2.00 2.000.152-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 12,750 304 331 25,500 0:08:57 0:47:58 1.00 0.25 1.00 0.70 30.00 2.00 2.000.152-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00000 37 14,110 336 381 42,330 0:10:19 0:39:01 1.00 0.25 1.00 0.70 30.00 2.00 2.00 0.152-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 6,375 152 179 25,500 0:04:51 0:28:42 1.00 0.25 1.00 0.70 30.00 2.00 2.00 0.152-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 5,270 125 151 23,715 0:04:05 0:23:51 1.00 0.25 1.00 0.70 30.00 2.00 2.00 0.152-15 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 4,437 106 129 22,185 0:03:30 0:19:46 1.00 0.25 1.00 0.70 30.00 2.00 2.00 0.152-16 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 3,740 89 111 20,570 0:03:01 0:16:15 1.00 0.25 1.00 0.70 30.00 2.00 2.00 0.152-17 30# Linear Flush 37 15,145 361 361 0:09:45 0:13:15 1.00 30.00 2.00 2.00 0.152-18 Freeze Protect Freeze Protect 10 1,470 35 35 0:03:30 0:03:30 2-19 Shut-In Shut-In3-1 Shut-In Shut-In1:12:42 3-2 Freeze Protect Prime Up Pressure Test 5 1,000 24 24 0:04:46 1:12:42 3-3 Shut-In Shut-In1:07:57 3-4 30# Linear Spacer and Dart Drop 15 1,260 30 30 0:02:00 1:07:57 1.00 30.00 2.00 2.00 0.153-5 30# Linear Pre-Pad 37 8,400 200 200 0:05:24 1:05:57 1.00 30.00 2.00 2.00 0.153-6 30# Hybor G-i Establish Stable Fluid 37 2,100 50 50 0:01:21 1:00:32 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.153-7 30# Hybor G-i Pad 37 14,800 352 352 0:09:31 0:59:11 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.153-8 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:49:40 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.153-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 10,200 243 254 10,200 0:06:52 0:41:51 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.153-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 12,750 304 331 25,500 0:08:57 0:35:00 1.00 0.25 1.00 0.75 30.00 2.00 2.000.153-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 11,900 283 321 35,700 0:08:42 0:26:02 1.00 0.25 1.00 0.75 30.00 2.00 2.000.153-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 8,500 202 238 34,000 0:06:28 0:17:20 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.153-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 6,800 162 198 34,000 0:05:22 0:10:52 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.153-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 5,100 121 154 30,600 0:04:11 0:05:30 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.153-15 30# Linear Spacer and Dart Drop 37 2,041 49 49 0:01:19 0:01:19 1.00 30.00 2.00 2.00 0.154-1 30# Linear Pre-Pad 37 2,100 50 50 0:01:21 0:57:21 1.00 30.00 2.00 2.00 0.154-2 30# Hybor G-i Establish Stable Fluid 37 8,400 200 200 0:05:24 0:56:00 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.154-3 30# Hybor G-i Pad 37 10,785 257 257 0:06:56 0:50:35 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.154-4 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:43:39 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.154-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 7,225 172 180 7,225 0:04:52 0:35:50 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.154-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 7,225 172 187 14,450 0:05:04 0:30:59 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.154-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 6,800 162 184 20,400 0:04:58 0:25:54 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.154-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 7,650 182 215 30,600 0:05:49 0:20:56 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.154-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 6,800 162 198 34,000 0:05:22 0:15:07 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.154-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 5,950 142 180 35,700 0:04:53 0:09:44 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.154-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37 4,250 101 131 27,625 0:03:33 0:04:52 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.154-12 30# Linear Spacer and Dart Drop 37 2,041 49 49 0:01:19 0:01:19 1.00 30.00 2.00 2.00 0.155-1 30# Linear Pre-Pad 37 2,100 50 50 0:01:21 0:48:02 1.00 30.00 2.00 2.00 0.155-2 30# Hybor G-i Establish Stable Fluid 37 8,400 200 200 0:05:24 0:46:41 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.155-3 30# Hybor G-i Pad 37 6,450 154 154 0:04:09 0:41:17 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.155-4 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:37:08 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.155-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 1,700 40 42 1,700 0:01:09 0:29:19 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.155-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 2,175 52 56 4,350 0:01:32 0:28:11 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.155-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 3,400 81 92 10,200 0:02:29 0:26:39 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.155-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 4,100 98 115 16,400 0:03:07 0:24:10 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.155-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 4,240 101 121 19,080 0:03:17 0:21:03 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.155-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00000 37 4,600 110 134 23,000 0:03:38 0:17:45 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.155-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 4,680 111 139 25,740 0:03:46 0:14:07 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.155-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 4,930 117 149 29,580 0:04:02 0:10:21 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.155-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37 3,400 81 104 22,100 0:02:50 0:06:19 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.155-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37 2,550 61 80 17,850 0:02:10 0:03:29 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.155-15 30# Linear Spacer and Dart Drop 37 2,041 49 49 0:01:19 0:01:19 1.00 30.00 2.00 2.00 0.15Interval 1Moraine@ 23276.81 - 23281.15 ft 137.3 °F"Alpha SleeveInterval 2Moraine@ 22818.85 - 22823.19 ft 137.4 °F"Frac Sleeve 1Interval 3Moraine@ 22324.92 - 22329.26 ft 137.6 °F"Frac Sleeve 2Interval 4Moraine@ 21829.56 - 21833.9 ft 137.8 °F"Frac Sleeve 3Interval 5Moraine@ 21331.62 - 21335.96 ft 138 °F"Frac Sleeve 46/16/25Liquid AdditivesDry Additives50-103-20914910128224Conoco Phillips - 3T-613Planned Design193 CUSTOMERConoco Phillips FALSEAPIBFD (lb/gal)8.48LAT 70.42061242LEASE3T-613SALES ORDERBHST (°F)139LONG-150.266098FORMATIONMoraineDATE Max Pressure (psi)8500*Exceeds 80% of burst pressure*Prop Slurry Design Clean Design Clean Design Slurry Design Prop Stage Interval CL-28M BC-140X2 Losurf-300D MO-67 WG-36 OPTIFLO-III OPTIFLO-IIBE-6Treatment Stage Fluid Stage Proppant Conc Rate Volume Volume Volume Total Time TimeCrosslinker Crosslinker Surfactant Buffer Gel Breaker Breaker BiocideInterval Number Description Description Description(ppg) (bpm) (gal) (bbl) (bbl) (lbs) (hh:mm:ss) (hh:mm:ss)(gpt) (gpt) (gpt) (gpt) (ppt) (ppt) (ppt) (ppt)6/16/25Liquid AdditivesDry Additives50-103-209149101282246-1 30# Linear Pre-Pad 37 2,100 50 50 0:01:21 0:59:58 1.00 30.00 2.00 2.00 0.156-2 30# Hybor G-i Establish Stable Fluid 37 8,400 200 200 0:05:24 0:58:37 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.156-3 30# Hybor G-i Pad 37 6,450 154 154 0:04:09 0:53:13 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.156-4 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:49:04 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.156-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 1,700 40 42 1,700 0:01:09 0:41:15 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.156-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 2,175 52 56 4,350 0:01:32 0:40:07 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.156-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 3,400 81 92 10,200 0:02:29 0:38:35 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.156-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 4,100 98 115 16,400 0:03:07 0:36:06 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.156-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 4,240 101 121 19,080 0:03:17 0:32:59 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.156-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 4,600 110 134 23,000 0:03:38 0:29:41 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.156-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 4,680 111 139 25,740 0:03:46 0:26:03 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.156-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 4,930 117 149 29,580 0:04:02 0:22:17 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.156-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37 3,400 81 104 22,100 0:02:50 0:18:15 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.156-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37 2,550 61 80 17,850 0:02:10 0:15:25 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.156-15 30# Linear Flush 37 15,145 361 361 0:09:45 0:13:15 1.00 30.00 2.00 2.00 0.156-16 Freeze Protect Freeze Protect 10 1,470 35 35 0:03:30 0:03:30 6-17 Shut-In Shut-In7-1 Shut-In Shut-In0:55:18 7-2 Freeze Protect Prime Up Pressure Test 5 1,000 24 24 0:04:46 0:55:18 0.757-3 Shut-In Shut-In0:50:32 7-4 30# Linear Spacer and Dart Drop 20 2,100 50 50 0:02:30 0:50:32 1.00 30.00 2.00 2.00 0.157-5 30# Linear Pre-Pad 37 2,100 50 50 0:01:21 0:48:02 1.00 0.75 30.00 2.00 2.00 0.157-6 30# Hybor G-i Establish Stable Fluid 37 8,400 200 200 0:05:24 0:46:41 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.157-7 30# Hybor G-i Pad 37 6,450 154 154 0:04:09 0:41:17 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.157-8 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:37:08 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.157-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 1,700 40 42 1,700 0:01:09 0:29:19 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.157-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 2,175 52 56 4,350 0:01:32 0:28:11 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.157-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 3,400 81 92 10,200 0:02:29 0:26:39 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.157-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 4,100 98 115 16,400 0:03:07 0:24:10 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.157-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 4,240 101 121 19,080 0:03:17 0:21:03 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.157-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 4,600 110 134 23,000 0:03:38 0:17:45 1.00 0.25 1.00 0.70 30.00 2.00 2.00 0.157-15 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 4,680 111 139 25,740 0:03:46 0:14:07 1.00 0.25 1.00 0.70 30.00 2.00 2.00 0.157-16 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 4,930 117 149 29,580 0:04:02 0:10:21 1.00 0.25 1.00 0.70 30.00 2.00 2.00 0.157-17 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37 3,400 81 104 22,100 0:02:50 0:06:19 1.00 0.25 1.00 0.70 30.00 2.00 2.00 0.157-18 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37 2,550 61 80 17,850 0:02:10 0:03:29 1.00 0.25 1.00 0.70 30.00 2.00 2.00 0.157-19 30# Linear Spacer and Dart Drop 37 2,041 49 49 0:01:19 0:01:19 1.00 30.00 2.00 2.00 0.158-1 30# Linear Pre-Pad 37 2,100 50 50 0:01:21 1:19:53 1.00 30.00 2.00 2.00 0.158-2 30# Hybor G-i Minifrac - Establish Fluid 37 2,100 50 50 0:01:21 1:18:32 1.00 0.25 1.00 0.75 30.00 2.00 2.00 0.158-3 30# Hybor G-i Displacement 37 13,224 315 315 0:08:31 1:17:11 1.00 0.25 1.00 0.70 30.00 2.00 2.00 0.158-4 30# Hybor G-i Minifrac - Treatment 37 6,300 150 150 0:04:03 1:08:40 1.00 0.25 1.00 0.70 30.00 2.00 2.00 0.158-5 30# Hybor G-i Minifrac - Flush 37 13,224 315 315 0:08:31 1:04:37 1.00 0.25 1.00 0.70 30.00 2.00 2.00 0.158-6 Shut-In Shut-In0:56:07 8-7 Freeze Protect Prime Up Pressure Test 5 1,000 24 24 0:04:46 0:56:07 8-8 Shut-In Shut-In0:51:21 8-9 30# Hybor G-i Establish Stable Fluid 37 8,400 200 200 0:05:24 0:51:21 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.158-10 30# Hybor G-i Pad 37 8,610 205 205 0:05:32 0:45:57 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.158-11 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:40:24 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.158-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 1,900 45 47 1,900 0:01:17 0:32:36 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.158-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 2,375 57 62 4,750 0:01:40 0:31:19 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.158-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 3,800 90 103 11,400 0:02:47 0:29:39 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.158-15 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 4,570 109 128 18,280 0:03:29 0:26:52 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.158-16 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 4,760 113 136 21,420 0:03:41 0:23:23 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.158-17 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 5,140 122 150 25,700 0:04:04 0:19:42 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.158-18 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 5,200 124 154 28,600 0:04:11 0:15:38 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.158-19 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 5,550 132 168 33,300 0:04:33 0:11:27 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.158-20 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37 3,800 90 117 24,700 0:03:10 0:06:54 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.158-21 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37 2,850 68 89 19,950 0:02:25 0:03:44 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.158-22 30# Linear Spacer and Dart Drop 37 2,041 49 49 0:01:19 0:01:19 1.00 30.00 2.00 2.00 0.159-1 30# Linear Pre-Pad 37 2,100 50 50 0:01:21 0:48:39 1.00 30.00 2.00 2.00 0.159-2 30# Hybor G-i Establish Stable Fluid 37 2,100 50 50 0:01:21 0:47:18 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.159-3 30# Hybor G-i Pad 37 8,610 205 205 0:05:32 0:45:57 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.159-4 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:40:24 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.159-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 1,900 45 47 1,900 0:01:17 0:32:36 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.159-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 2,375 57 62 4,750 0:01:40 0:31:19 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.159-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 3,800 90 103 11,400 0:02:47 0:29:39 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.159-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 4,570 109 128 18,280 0:03:29 0:26:52 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.159-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.5000 37 4,760 113 136 21,420 0:03:41 0:23:23 1.00 0.25 1.00 0.60 30.00 2.00 2.000.159-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 5,140 122 150 25,700 0:04:04 0:19:42 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.159-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 5,200 124 154 28,600 0:04:11 0:15:38 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.159-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 5,550 132 168 33,300 0:04:33 0:11:27 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.159-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37 3,800 90 117 24,700 0:03:10 0:06:54 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.159-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37 2,850 68 89 19,950 0:02:25 0:03:44 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.159-15 30# Linear Spacer and Dart Drop 37 2,041 49 49 0:01:19 0:01:19 1.00 30.00 2.00 2.00 0.15Interval 9Moraine@ 19337.07 - 19341.41 ft 137.9 °F"Frac Sleeve 8Interval 6Moraine@ 20834.19 - 20838.53 ft 138.3 °F"Frac Sleeve 5Interval 7Moraine@ 20336.33 - 20340.67 ft 138.5 °F"Frac Sleeve 6Interval 8Moraine@ 19795.42 - 19799.76 ft 138.3 °F"Frac Sleeve 7Conoco Phillips - 3T-613Planned Design194 CUSTOMERConoco Phillips FALSEAPIBFD (lb/gal)8.48LAT 70.42061242LEASE3T-613SALES ORDERBHST (°F)139LONG-150.266098FORMATIONMoraineDATE Max Pressure (psi)8500*Exceeds 80% of burst pressure*Prop Slurry Design Clean Design Clean Design Slurry Design Prop Stage Interval CL-28M BC-140X2 Losurf-300D MO-67 WG-36 OPTIFLO-III OPTIFLO-IIBE-6Treatment Stage Fluid Stage Proppant Conc Rate Volume Volume Volume Total Time TimeCrosslinker Crosslinker Surfactant Buffer Gel Breaker Breaker BiocideInterval Number Description Description Description(ppg) (bpm) (gal) (bbl) (bbl) (lbs) (hh:mm:ss) (hh:mm:ss)(gpt) (gpt) (gpt) (gpt) (ppt) (ppt) (ppt) (ppt)6/16/25Liquid AdditivesDry Additives50-103-2091491012822410-1 30# Linear Pre-Pad 37 2,100 50 50 0:01:21 0:48:39 1.00 30.00 2.00 2.00 0.1510-2 30# Hybor G-i Establish Stable Fluid 37 2,100 50 50 0:01:21 0:47:18 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1510-3 30# Hybor G-i Pad 37 8,610 205 205 0:05:32 0:45:57 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1510-4 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:40:24 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1510-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 1,900 45 47 1,900 0:01:17 0:32:36 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1510-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 2,375 57 62 4,750 0:01:40 0:31:19 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1510-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 3,800 90 103 11,400 0:02:47 0:29:39 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1510-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 4,570 109 128 18,280 0:03:29 0:26:52 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1510-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 4,760 113 136 21,420 0:03:41 0:23:23 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1510-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 5,140 122 150 25,700 0:04:04 0:19:42 1.00 0.25 1.00 0.60 30.00 2.00 2.000.1510-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 5,200 124 154 28,600 0:04:11 0:15:38 1.00 0.25 1.00 0.60 30.00 2.00 2.000.1510-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 5,550 132 168 33,300 0:04:33 0:11:27 1.00 0.25 1.00 0.60 30.00 2.00 2.000.1510-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37 3,800 90 117 24,700 0:03:10 0:06:54 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1510-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37 2,850 68 89 19,950 0:02:25 0:03:44 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1510-15 30# Linear Spacer and Dart Drop 37 2,041 49 49 0:01:19 0:01:19 1.00 30.00 2.00 2.00 0.1511-1 30# Linear Pre-Pad 37 2,100 50 50 0:01:21 0:48:09 1.00 30.00 2.00 2.00 0.1511-2 30# Hybor G-i Establish Stable Fluid 37 2,100 50 50 0:01:21 0:46:48 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1511-3 30# Hybor G-i Pad 37 8,610 205 205 0:05:32 0:45:26 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1511-4 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:39:54 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1511-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 1,900 45 47 1,900 0:01:17 0:32:05 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1511-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 2,375 57 62 4,750 0:01:40 0:30:49 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1511-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 3,800 90 103 11,400 0:02:47 0:29:09 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1511-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 4,570 109 128 18,280 0:03:29 0:26:22 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1511-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 4,760 113 136 21,420 0:03:41 0:22:53 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1511-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 5,140 122 150 25,700 0:04:04 0:19:12 1.00 0.25 1.00 0.60 30.00 2.00 2.000.1511-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 5,200 124 154 28,600 0:04:11 0:15:08 1.00 0.25 1.00 0.60 30.00 2.00 2.000.1511-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 5,550 132 168 33,300 0:04:33 0:10:57 1.00 0.25 1.00 0.60 30.00 2.00 2.000.1511-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37 3,800 90 117 24,700 0:03:10 0:06:24 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1511-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37 2,850 68 89 19,950 0:02:25 0:03:14 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1511-15 30# Linear Spacer and Dart Drop 37 1,260 30 30 0:00:49 0:00:49 1.00 30.00 2.00 2.00 0.1512-1 30# Linear Pre-Pad 37 2,100 50 50 0:01:21 0:48:39 1.00 30.00 2.00 2.00 0.1512-2 30# Hybor G-i Establish Stable Fluid 37 2,100 50 50 0:01:21 0:47:18 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1512-3 30# Hybor G-i Pad 37 8,610 205 205 0:05:32 0:45:57 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1512-4 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:40:24 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1512-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 1,900 45 47 1,900 0:01:17 0:32:36 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1512-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 2,375 57 62 4,750 0:01:40 0:31:19 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1512-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 3,800 90 103 11,400 0:02:47 0:29:39 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1512-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 4,570 109 128 18,280 0:03:29 0:26:52 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1512-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 4,760 113 136 21,420 0:03:41 0:23:23 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1512-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 5,140 122 150 25,700 0:04:04 0:19:42 1.00 0.25 1.00 0.60 30.00 2.00 2.000.1512-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 5,200 124 154 28,600 0:04:11 0:15:38 1.00 0.25 1.00 0.60 30.00 2.00 2.000.1512-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 5,550 132 168 33,300 0:04:33 0:11:27 1.00 0.25 1.00 0.60 30.00 2.00 2.000.1512-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37 3,800 90 117 24,700 0:03:10 0:06:54 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1512-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37 2,850 68 89 19,950 0:02:25 0:03:44 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1512-15 30# Linear Spacer and Dart Drop 37 2,041 49 49 0:01:19 0:01:19 1.00 30.00 2.00 2.00 0.1513-1 30# Linear Pre-Pad 37 2,100 50 50 0:01:21 1:02:23 1.00 30.00 2.00 2.00 0.1513-2 30# Hybor G-i Establish Stable Fluid 37 8,400 200 200 0:05:24 1:01:02 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1513-3 30# Hybor G-i Pad 37 8,610 205 205 0:05:32 0:55:38 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1513-4 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:50:05 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1513-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 1,900 45 47 1,900 0:01:17 0:42:17 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1513-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 2,375 57 62 4,750 0:01:40 0:41:00 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1513-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 3,800 90 103 11,400 0:02:47 0:39:20 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1513-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 4,570 109 128 18,280 0:03:29 0:36:33 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1513-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 4,760 113 136 21,420 0:03:41 0:33:05 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1513-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 5,140 122 150 25,700 0:04:04 0:29:23 1.00 0.25 1.00 0.60 30.00 2.00 2.000.1513-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 5,200 124 154 28,600 0:04:11 0:25:19 1.00 0.25 1.00 0.60 30.00 2.00 2.000.1513-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 5,550 132 168 33,300 0:04:33 0:21:08 1.00 0.25 1.00 0.60 30.00 2.00 2.000.1513-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37 3,800 90 117 24,700 0:03:10 0:16:35 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1513-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37 2,850 68 89 19,950 0:02:25 0:13:25 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1513-15 30# Linear Flush 37 11,655 278 278 0:07:30 0:11:00 1.00 30.00 2.00 2.00 0.1513-16 Freeze Protect Freeze Protect 10 1,470 35 35 0:03:30 0:03:30 13-17 Shut-In Shut-InInterval 10Moraine@ 18837.88 - 18842.22 ft 137.9 °F"Frac Sleeve 9Interval 11Moraine@ 18339.06 - 18343.4 ft 138.1 °F"Frac Sleeve 10Interval 12Moraine@ 17840.76 - 17845.1 ft 138.5 °F"Frac Sleeve 11Interval 13Moraine@ 17341.75 - 17346.09 ft 139 °F"Frac Sleeve 12Conoco Phillips - 3T-613Planned Design195 CUSTOMERConoco Phillips FALSEAPIBFD (lb/gal)8.48LAT 70.42061242LEASE3T-613SALES ORDERBHST (°F)139LONG-150.266098FORMATIONMoraineDATE Max Pressure (psi)8500*Exceeds 80% of burst pressure*Prop Slurry Design Clean Design Clean Design Slurry Design Prop Stage Interval CL-28M BC-140X2 Losurf-300D MO-67 WG-36 OPTIFLO-III OPTIFLO-IIBE-6Treatment Stage Fluid Stage Proppant Conc Rate Volume Volume Volume Total Time TimeCrosslinker Crosslinker Surfactant Buffer Gel Breaker Breaker BiocideInterval Number Description Description Description(ppg) (bpm) (gal) (bbl) (bbl) (lbs) (hh:mm:ss) (hh:mm:ss)(gpt) (gpt) (gpt) (gpt) (ppt) (ppt) (ppt) (ppt)6/16/25Liquid AdditivesDry Additives50-103-2091491012822414-1 Shut-In Shut-In1:21:32 14-2 Freeze Protect Prime Up Pressure Test 5 1,000 24 24 0:04:46 1:21:32 14-3 Shut-In Shut-In1:16:46 14-4 30# Linear Spacer and Dart Drop 15 2,100 50 50 0:03:20 1:16:46 1.00 30.00 2.00 2.00 0.1514-5 30# Linear Displacement 20 11,337 270 270 0:13:30 1:13:26 1.00 30.00 2.00 2.00 0.1514-6 30# Linear DFIT 10 1,680 40 40 0:04:00 0:59:57 1.00 30.00 2.00 2.00 0.1514-7 Shut-In Shut-In0:55:57 14-8 30# Hybor G-i Establish Stable Fluid 20 8,400 200 200 0:10:00 0:55:57 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1514-9 30# Hybor G-i Pad 37 8,610 205 205 0:05:32 0:45:57 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1514-10 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:40:24 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1514-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 1,900 45 47 1,900 0:01:17 0:32:36 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1514-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 2,375 57 62 4,750 0:01:40 0:31:19 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1514-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 3,800 90 103 11,400 0:02:47 0:29:39 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1514-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 4,570 109 128 18,280 0:03:29 0:26:52 1.00 0.25 1.00 0.60 30.00 2.00 2.000.1514-15 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 4,760 113 136 21,420 0:03:41 0:23:23 1.00 0.25 1.00 0.60 30.00 2.00 2.000.1514-16 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 5,140 122 150 25,700 0:04:04 0:19:42 1.00 0.25 1.00 0.60 30.00 2.00 2.000.1514-17 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 5,200 124 154 28,600 0:04:11 0:15:38 1.00 0.25 1.00 0.60 30.00 2.00 2.000.1514-18 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 5,550 132 168 33,300 0:04:33 0:11:27 1.00 0.25 1.00 0.60 30.00 2.00 2.000.1514-19 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37 3,800 90 117 24,700 0:03:10 0:06:54 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1514-20 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37 2,850 68 89 19,950 0:02:25 0:03:44 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1514-21 30# Linear Spacer and Dart Drop 37 2,041 49 49 0:01:19 0:01:19 1.00 30.00 2.00 2.00 0.1515-1 30# Linear Pre-Pad 37 2,100 50 50 0:01:21 0:51:01 1.00 30.00 2.00 2.00 0.1515-2 30# Hybor G-i Establish Stable Fluid 37 2,100 50 50 0:01:21 0:49:39 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1515-3 30# Hybor G-i Pad 37 9,710 231 231 0:06:15 0:48:18 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1515-4 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:42:03 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1515-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 2,000 48 50 2,000 0:01:21 0:34:15 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1515-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 2,500 60 65 5,000 0:01:45 0:32:54 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1515-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 4,000 95 108 12,000 0:02:56 0:31:09 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1515-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 4,850 115 136 19,400 0:03:41 0:28:13 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1515-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 5,000 119 143 22,500 0:03:53 0:24:32 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1515-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 5,410 129 158 27,050 0:04:17 0:20:39 1.00 0.25 1.00 0.60 30.00 2.00 2.000.1515-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 5,500 131 163 30,250 0:04:26 0:16:23 1.00 0.25 1.00 0.60 30.00 2.00 2.000.1515-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 5,800 138 175 34,800 0:04:45 0:11:57 1.00 0.25 1.00 0.60 30.00 2.00 2.000.1515-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37 4,000 95 123 26,000 0:03:20 0:07:12 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1515-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37 3,000 71 94 21,000 0:02:33 0:03:52 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1515-15 30# Linear Spacer and Dart Drop 37 2,041 49 49 0:01:19 0:01:19 1.00 30.00 2.00 2.00 0.1516-1 30# Linear Pre-Pad 37 2,100 50 50 0:01:21 0:51:01 1.00 30.00 2.00 2.00 0.1516-2 30# Hybor G-i Establish Stable Fluid 37 2,100 50 50 0:01:21 0:49:39 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1516-3 30# Hybor G-i Pad 37 9,710 231 231 0:06:15 0:48:18 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1516-4 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:42:03 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1516-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 2,000 48 50 2,000 0:01:21 0:34:15 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1516-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 2,500 60 65 5,000 0:01:45 0:32:54 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1516-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 4,000 95 108 12,000 0:02:56 0:31:09 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1516-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 4,850 115 136 19,400 0:03:41 0:28:13 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1516-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 5,000 119 143 22,500 0:03:53 0:24:32 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1516-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 5,410 129 158 27,050 0:04:17 0:20:39 1.00 0.25 1.00 0.60 30.00 2.00 2.000.1516-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 5,500 131 163 30,250 0:04:26 0:16:23 1.00 0.25 1.00 0.60 30.00 2.00 2.000.1516-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00000 37 5,800 138 175 34,800 0:04:45 0:11:57 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1516-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37 4,000 95 123 26,000 0:03:20 0:07:12 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1516-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37 3,000 71 94 21,000 0:02:33 0:03:52 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1516-15 30# Linear Spacer and Dart Drop 37 2,041 49 49 0:01:19 0:01:19 1.00 30.00 2.00 2.00 0.1517-1 30# Linear Pre-Pad 37 2,100 50 50 0:01:21 0:51:01 1.00 30.00 2.00 2.00 0.1517-2 30# Hybor G-i Establish Stable Fluid 37 2,100 50 50 0:01:21 0:49:39 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1517-3 30# Hybor G-i Pad 37 9,710 231 231 0:06:15 0:48:18 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1517-4 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:42:03 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1517-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 2,000 48 50 2,000 0:01:21 0:34:15 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1517-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 2,500 60 65 5,000 0:01:45 0:32:54 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1517-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 4,000 95 108 12,000 0:02:56 0:31:09 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1517-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 4,850 115 136 19,400 0:03:41 0:28:13 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1517-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 5,000 119 143 22,500 0:03:53 0:24:32 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1517-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 5,410 129 158 27,050 0:04:17 0:20:39 1.00 0.25 1.00 0.60 30.00 2.00 2.000.1517-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.5000 37 5,500 131 163 30,250 0:04:26 0:16:23 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1517-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 5,800 138 175 34,800 0:04:45 0:11:57 1.00 0.25 1.00 0.60 30.00 2.00 2.000.1517-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37 4,000 95 123 26,000 0:03:20 0:07:12 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1517-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37 3,000 71 94 21,000 0:02:33 0:03:52 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1517-15 30# Linear Spacer and Dart Drop 37 2,041 49 49 0:01:19 0:01:19 1.00 30.00 2.00 2.00 0.15Interval 14Moraine@ 16843.15 - 16847.49 ft 138.9 °F"Frac Sleeve 13Interval 15Moraine@ 16349.44 - 16353.78 ft 138.9 °F"Frac Sleeve 14Interval 16Moraine@ 15850.53 - 15854.87 ft 138.7 °F"Frac Sleeve 15Interval 17Moraine@ 15352.19 - 15356.53 ft 138.5 °F"Frac Sleeve 16Conoco Phillips - 3T-613Planned Design196 CUSTOMERConoco Phillips FALSEAPIBFD (lb/gal)8.48LAT 70.42061242LEASE3T-613SALES ORDERBHST (°F)139LONG-150.266098FORMATIONMoraineDATE Max Pressure (psi)8500*Exceeds 80% of burst pressure*Prop Slurry Design Clean Design Clean Design Slurry Design Prop Stage Interval CL-28M BC-140X2 Losurf-300D MO-67 WG-36 OPTIFLO-III OPTIFLO-IIBE-6Treatment Stage Fluid Stage Proppant Conc Rate Volume Volume Volume Total Time TimeCrosslinker Crosslinker Surfactant Buffer Gel Breaker Breaker BiocideInterval Number Description Description Description(ppg) (bpm) (gal) (bbl) (bbl) (lbs) (hh:mm:ss) (hh:mm:ss)(gpt) (gpt) (gpt) (gpt) (ppt) (ppt) (ppt) (ppt)6/16/25Liquid AdditivesDry Additives50-103-2091491012822418-1 30# Linear Displacement 20 11,337 270 270 0:13:30 1:07:09 1.00 30.00 2.00 2.00 0.1518-2 30# Linear DFIT 10 1,680 40 40 0:04:00 0:53:39 1.00 30.00 2.00 2.00 0.1518-3 30# Hybor G-i Establish Stable Fluid 37 2,100 50 50 0:01:21 0:49:39 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1518-4 30# Hybor G-i Pad 37 9,710 231 231 0:06:15 0:48:18 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1518-5 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:42:03 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1518-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 2,000 48 50 2,000 0:01:21 0:34:15 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1518-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 2,500 60 65 5,000 0:01:45 0:32:54 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1518-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 4,000 95 108 12,000 0:02:56 0:31:09 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1518-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 4,850 115 136 19,400 0:03:41 0:28:13 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1518-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 5,000 119 143 22,500 0:03:53 0:24:32 1.00 0.25 1.00 0.60 30.00 2.00 2.000.1518-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 5,410 129 158 27,050 0:04:17 0:20:39 1.00 0.25 1.00 0.60 30.00 2.00 2.000.1518-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 5,500 131 163 30,250 0:04:26 0:16:23 1.00 0.25 1.00 0.60 30.00 2.00 2.000.1518-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 5,800 138 175 34,800 0:04:45 0:11:57 1.00 0.25 1.00 0.60 30.00 2.00 2.000.1518-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37 4,000 95 123 26,000 0:03:20 0:07:12 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1518-15 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37 3,000 71 94 21,000 0:02:33 0:03:52 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1518-16 30# Linear Spacer and Dart Drop 37 2,041 49 49 0:01:19 0:01:19 1.00 30.00 2.00 2.00 0.1519-1 30# Linear Pre-Pad 37 2,100 50 50 0:01:21 0:59:28 1.00 30.00 2.00 2.00 0.1519-2 30# Hybor G-i Establish Stable Fluid 37 2,100 50 50 0:01:21 0:58:07 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1519-3 30# Hybor G-i Pad 37 9,710 231 231 0:06:15 0:56:46 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1519-4 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:50:31 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1519-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 2,000 48 50 2,000 0:01:21 0:42:42 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1519-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 2,500 60 65 5,000 0:01:45 0:41:22 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1519-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 4,000 95 108 12,000 0:02:56 0:39:36 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1519-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 4,850 115 136 19,400 0:03:41 0:36:41 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1519-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 5,000 119 143 22,500 0:03:53 0:32:59 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1519-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 5,410 129 158 27,050 0:04:17 0:29:07 1.00 0.25 1.00 0.60 30.00 2.00 2.000.1519-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 5,500 131 163 30,250 0:04:26 0:24:50 1.00 0.25 1.00 0.60 30.00 2.00 2.000.1519-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 5,800 138 175 34,800 0:04:45 0:20:25 1.00 0.25 1.00 0.60 30.00 2.00 2.000.1519-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37 4,000 95 123 26,000 0:03:20 0:15:39 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1519-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37 3,000 71 94 21,000 0:02:33 0:12:19 1.00 0.25 1.00 0.60 30.00 2.00 2.00 0.1519-15 30# Linear Flush 37 9,747 232 232 0:06:16 0:09:46 1.00 30.00 2.00 2.00 0.1519-16 Freeze Protect Freeze Protect 10 1,470 35 35 0:03:30 0:03:30 19-17 Shut-In Shut-In20-1 Shut-In Shut-In2:08:16 20-2 Freeze Protect Prime Up Pressure Test 5 1,000 24 24 0:04:46 2:08:16 20-3 Shut-In Shut-In2:03:30 20-4 30# Linear Spacer and Dart Drop 15 1,260 30 30 0:02:00 2:03:30 1.00 30.00 2.00 2.00 0.1520-5 30# Linear Displacement 15 8,859 211 211 0:14:04 2:01:30 1.00 30.00 2.00 2.00 0.1520-6 30# Hybor G-i Minifrac - Establish Fluid 15 8,400 200 200 0:13:20 1:47:27 1.00 0.25 1.00 0.70 30.00 2.00 2.00 0.1520-7 30# Hybor G-i Minifrac - Treatment 37 16,500 393 393 0:10:37 1:34:07 1.00 0.25 1.00 0.70 30.00 2.00 2.00 0.1520-8 30# Linear Minifrac - Flush 37 9,430 225 225 0:06:04 1:23:30 1.00 30.00 2.00 2.00 0.1520-9 Shut-In Shut-In1:17:25 20-10 30# Hybor G-i Establish Stable Fluid 37 8,400 200 200 0:05:24 1:17:25 1.00 0.25 1.00 0.70 30.00 2.00 2.00 0.1520-11 30# Hybor G-i Pad 37 21,000 500 500 0:13:31 1:12:01 1.00 0.25 1.00 0.70 30.00 2.00 2.00 0.1520-12 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:58:30 1.00 0.25 1.00 0.70 30.00 2.00 2.00 0.1520-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 12,000 286 298 12,000 0:08:04 0:50:42 1.00 0.25 1.00 0.70 30.00 2.00 2.000.1520-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 16,000 381 415 32,000 0:11:14 0:42:37 1.00 0.25 1.00 0.70 30.00 2.00 2.000.1520-15 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 16,000 381 432 48,000 0:11:42 0:31:23 1.00 0.25 1.00 0.70 30.00 2.00 2.000.1520-16 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 10,000 238 281 40,000 0:07:37 0:19:41 1.00 0.25 1.00 0.70 30.00 2.00 2.000.1520-17 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 8,000 190 229 36,000 0:06:12 0:12:04 1.00 0.25 1.00 0.70 30.00 2.00 2.000.1520-18 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 6,400 152 186 32,000 0:05:03 0:05:52 1.00 0.25 1.00 0.70 30.00 2.00 2.000.1520-19 30# Linear Spacer and Dart Drop 37 1,260 30 30 0:00:49 0:00:49 1.00 30.00 2.00 2.00 0.1521-1 30# Linear Pre-Pad 37 2,100 50 50 0:01:21 0:35:52 1.00 30.00 2.00 2.00 0.1521-2 30# Hybor G-i Minifrac - Establish Fluid 37 2,100 50 50 0:01:21 0:34:31 1.00 0.25 1.00 0.70 30.00 2.00 2.00 0.1521-3 30# Hybor G-i Minifrac - Treatment 37 4,110 98 98 0:02:39 0:33:10 1.00 0.25 1.00 0.70 30.00 2.00 2.00 0.1521-4 30# Linear Minifrac - Flush 37 8,540 203 203 0:05:30 0:30:31 1.00 30.00 2.00 2.00 0.1521-5 Shut-In Shut-In0:25:01 21-6 30# Hybor G-i Establish Stable Fluid 37 2,100 50 50 0:01:21 0:25:01 1.00 0.25 1.00 0.70 30.00 2.00 2.00 0.1521-7 30# Hybor G-i Pad 37 2,220 53 53 0:01:26 0:23:40 1.00 0.25 1.00 0.70 30.00 2.00 2.00 0.1521-8 30# Hybor G-i Conditioning Pad Wanli 16/20 Ceramic 0.25 37 6,000 143 144 1,500 0:03:54 0:22:14 1.00 0.25 1.00 0.70 30.00 2.00 2.00 0.1521-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 3,000 71 75 3,000 0:02:01 0:18:20 1.00 0.25 1.00 0.70 30.00 2.00 2.00 0.1521-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 4,000 95 104 8,000 0:02:49 0:16:19 1.00 0.25 1.00 0.70 30.00 2.00 2.00 0.1521-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 4,000 95 108 12,000 0:02:56 0:13:30 1.00 0.25 1.00 0.70 30.00 2.00 2.00 0.1521-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 2,500 60 70 10,000 0:01:54 0:10:35 1.00 0.25 1.00 0.70 30.00 2.00 2.00 0.1521-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 2,000 48 57 9,000 0:01:33 0:08:41 1.00 0.25 1.00 0.70 30.00 2.00 2.00 0.1521-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 1,600 38 47 8,000 0:01:16 0:07:08 1.00 0.25 1.00 0.70 30.00 2.00 2.00 0.1521-15 30# Linear Flush 37 9,111 217 217 0:05:52 0:05:52 1.00 30.00 2.00 2.00 0.1521-16 Shut-In Shut-In1,792,660 42,682 46,767 3,844,700Design Total (gal)Design Total (lbs)CL-28M BC-140X2 Losurf-300D MO-67 WG-36 OPTIFLO-III OPTIFLO-II BE-6-3,781,700(gal) (gal) (gal) (gal) (lbs) (lbs) (lbs) (lbs)220,80563,000Initial Design Material Volume 1,560.0 390.0 1,780.8 1,032.2 53,423.4 3,561.6 3,561.6 267.1-30% Excess 2028 507 2315 1342 69450 4630 4630 34711,880-Whole Units to be ordered1,559,975-CL-28M BC-140X2 Losurf-300D MO-67 WG-36 OPTIFLO-III OPTIFLO-II BE-6-(gpm) (gpm) (gpm) (gpm) ppm ppm ppm ppm-Max Additive Rate 1.6 0.4 1.6 1.2 46.6 3.1 3.1 0.2-Min Additive Rate22:48:23 Interval 18Moraine@ 14854.27 - 14858.61 ft 138.3 °F"Frac Sleeve 17Interval 19Moraine@ 14356.39 - 14360.73 ft 138.1 °F"Frac Sleeve 18Interval 20Moraine@ 13859.35 - 13863.69 ft 138.1 °F"Frac Sleeve 18Interval 21Moraine@ 13361.01 - 13365.35 ft 137.9 °F"Frac Sleeve 20Proppant TypeWanli 16/20 Ceramic100M---Fluid Type-30# LinearSeawaterFreeze Protect30# Hybor G-i---Conoco Phillips - 3T-613Planned Design197 Interval Designed Proppant (lbs) Designed Fluid (bbl) Pad Percentage Design Pad Percentage Actual Proppant Aggressivness (lb/bbl Clean) Top Sleeve (ft) Sleeve Perf (ft) Fluid System Notes 1 173,000 2,614 30.00 29 114 23,277 23,281 Hybor G-i 2 173,000 3,813 42.39 41 106 22,819 22,823 Hybor G-i Extended Pad - Pump Issues - Restarted Stage 3 173,000 2,306 30.01 45 124 22,325 22,329 Hybor G-i Extended Pad 4 173,000 1,934 30.00 29 151 21,830 21,834 Hybor G-i 5 173,000 1,590 30.01 30 193 21,332 21,336 Hybor G-i 6 173,000 1,937 30.01 29 188 20,834 20,839 Hybor G-i 7 173,000 1,663 30.01 29 190 20,336 20,341 Hybor G-i 8 193,000 2,594 30.00 29 191 19,795 19,800 Hybor G-i Pump Issues 9 193,000 1,590 30.00 29 192 19,337 19,341 Hybor G-i 10 193,000 1,590 30.00 29 192 18,838 18,842 Hybor G-i 11 193,000 1,572 30.00 29 190 18,339 18,343 Hybor G-i 12 193,000 1,590 30.00 29 192 17,841 17,845 Hybor G-i 13 193,000 2,004 30.00 29 188 17,342 17,346 Hybor G-i 14 193,000 2,074 30.00 30 192 16,843 16,847 Hybor G-i 15 203,000 1,667 30.00 29 193 16,349 16,354 Hybor G-i Pump Issues 16 203,000 1,667 30.00 29 190 15,851 15,855 Hybor G-i 17 203,000 1,667 30.00 29 189 15,352 15,357 Hybor G-i 18 203,000 1,927 30.00 29 190 14,854 14,859 Hybor G-i Shut down to load proppant 19 203,000 1,885 30.00 29 190 14,356 14,361 Hybor G-i 20 203,000 3,726 30.00 29 119 13,859 13,864 Hybor G-i 21 51,500 1,271 30.01 26 117 13,361 13,365 Hybor G-i 3T-613 Interval Highlights Conoco Phillips - 3T-613 Well Summary 198 CustomerConoco Phillips FormationMoraineLease3T-613API50-103-20914DateInterval Summary - Chemicals CL-28M BC-140X2 Losurf-300D MO-67 WG-36 OPTIFLO-III OPTIFLO-II BE-6(gal) (gal) (gal) (gal) (lbs) (lbs) (lbs) (lbs)191 23 113 69 3683 218 217 752139 35 172 70 5440 345 345 03115 29 122 86 4078 243 243 48474 18 78 56 2608 158 159 -560 17 65 45 2026 129 129 0661 17 78 46 2290 156 156 0785 2 92 42 1913 151 151 39898 25 102 69 3075 205 201 6966 16 70 30 2011 139 139 01065 16 68 29 1878 139 138 01165 17 70 30 1975 139 140 01265 16 69 29 1878 138 138 01366 15 76 48 2068 90 94 01465 17 107 29 2301 161 161 711569 17 74 24 2085 147 148 01670 18 74 24 1985 149 148 01770 17 74 25 2093 148 148 01868 17 82 23 2550 163 164 019113 26 121 40 2109 243 242 020129 23 151 40 4228 300 300 362121 10 32 25 1502 100 75 0Total 1655 391 1890 879 53776 3661 3636 275w/o Prime Up1655 391 1890 879 53776 3661 3636 275Interval6/16/2025Dry AdditivesLiquid AdditivesConoco Phillips - 3T-613 Chemical Summary199 Company:Well Name:BHST (ºF):Depth:Formation:Analyst:cp @Test #1Test #2Test #3Test #4time (hr:min) -->00:00 01:00 02:00 03:00 04:00 05:00 10:00 15:00 20:00 25:00 30:00 45:00 1:00 1:15 1:30 1:45 2:00 2:15 2:30 2:45 3:00 3:30 4:00 4:30 5:00 5:30 6:006:30Test #1 (cp) -->2222 1605 2222 2098 2222 1901 1852 2098 2024 2345 2345 2518 1975 1728 1605 1728 1654 1481 1605 1333 987 617 197 0 0 0 0 0Dial Reading90 65 90 85 90 77 75 85 82 95 95 102 80 70 65 70 67 60 65 54 40 25 8 0Test #2 (cp) -->0000000000000000000000000000Dial ReadingTest #3 (cp) -->0000000000000000000000000000Dial ReadingTest #4 (cp) -->0000000000000000000000000000Dial Reading3T-613Stage(s):Break Test125Water Source:CPF3ALASKA DISTRICT LABORATORY15 Minute Fann Model 35 Crosslinked Fluid ReportFluid System: Date:6/15/2025ConocoPhillipsProject No:EE.. BRITTONHydration Visc:2395Temperature was held at 115 degres for the duration of the testAll chemical concentrations below are in gallons per thousand / pounds per thousandWater pH:6.90MoraineHydration pH:Temp 0FPHLOSURF-300DWG-36MO-67CL-28MBC-140X2OptiFlo-IIOptiFlo-III0.252.002.0030.000.701.00959.301.0005001000150020002500300000:00 02:00 04:00 10:00 20:00 30:00 1:00 1:30 2:00 2:30 3:00 4:00 5:006:00Viscosity (cp)Time (min:sec)Prejob Crosslink Break Tests30# - Opti II @ 2.0 and Optiflo-III @ 2.0Fluid is broken at 200cpConoco Phillips - 3T-613Prejob Break Test200 Specific Gravity Testing Temperature Dissolved Iron (Fe2+) Chloride (Cl-) Sulfate (SO4 2-) Calcium (Ca2+) Magnesium (Mg2+) Total Hardness Linear Viscosity Water pH Gel pH Post-Crosslink pH Crosslink Bacteria - °F mg/L mg/L mg/L mg/L mg/L mg/L cP - - - (Y/N) BQ Value Tank # H2S present? Y/N Hydrometer Digital Thermometer Strip Strip Strip Titration Total Hardness Minus Calcium Titration FANN-35 Probe Probe Probe - Mycometer 1 N 1.024 106.5 0 16,460 1,200 3,000 400 3,400 20,233 2 N 1.026 106.5 0 16,460 1,200 3,000 400 3,400 5,356 3 N 1.024 106.5 0 16,460 1,200 3,000 800 3,800 1,471 4 N 1.024 102.0 0 17,790 1,200 2,800 800 3,600 3,234 5 N 1.024 102.0 0 17,790 1,200 2,800 800 3,600 6,017 6 N 1.024 102.0 0 16,460 1,200 2,600 600 3,200 9,376 7 N 1.024 100.0 0 17,790 1,200 2,800 600 3,400 5,074 8 N 1.024 102.0 0 15,230 1,200 2,600 400 3,000 17,411 9 N 1.026 100.0 0 15,230 1,200 2,600 400 3,000 28,922 10 N 1.024 100.0 0 16,460 1,200 3,000 400 3,400 21,374 11 N 1.024 102.0 0 16,460 1,200 2,800 600 3,400 14,383 12 N 1.024 100.0 0 17,790 1,200 2,200 1,000 3,200 31,386 13 N 1.026 100.0 0 17,790 1,200 2,200 1,000 3,200 33,615 14 N 1.024 100.0 0 19,240 1,200 2,600 600 3,200 25,270 15 N 1.024 102.0 0 17,790 1,200 2,600 1,000 3,600 30,680 16 N 1.024 102.0 0 19,240 1,200 2,600 1,000 3,600 10,827 17 N 1.024 105.0 0 19,240 1,200 2,800 800 3,600 19,243 18 N 1.024 105.0 0 17,790 1,200 2,600 600 3,200 17,083 19 N 1.026 105.0 0 16,460 1,200 2,800 600 3,400 7,087 20 N 1.024 108.0 0 15,230 1,200 2,200 1,200 3,400 11,065 21 N 1.024 108.0 0 15,230 1,200 2,200 1,400 3,600 6,329 22 N 1.024 100.0 0 16,460 1,200 2,600 800 3,400 11,735 23 N 1.024 100.0 0 19,240 1,200 1,840 1,360 3,200 25,308 24 N 1.024 100.0 2 19,240 1,200 2,200 1,000 3,200 10,554 25 N 1.024 102.0 0 17,790 1,200 2,800 800 3,600 3,428 Average 1.024 0 13,907 1200 2,105 625 2,729 23.0 7.28 7.57 9.25 - 15,059 Maximum 1.026 0 19,240 1,200 3,000 1,400 3,800 24.0 7.40 7.71 9.30 - 33,615 Minimum 1.024 0 15,230 1,200 1,840 400 3,000 22.00 7.20 7.40 9.20 - 1,471 Range 0.002 0 4,010 0 1,160 1,000 800 2.0 0.20 0.31 0.10 - 32,145 Alaska District Field QC Prejob Water Analysis on Location Company:Conoco Phillips Well Name:3T-613 Water Source:CPF3 Y 24.0 7.2 7.7 9.3 Y 23.0 7.2 7.4 9.2 22.0 7.3 7.4 9.3 Y 23.0 7.30 7.71 9.30 Y 23.0 7.4 7.6 9.2 Y Conoco Phillips - 3T-613 Water Analysis 6-15 201 Specific Gravity Testing Temperature Dissolved Iron (Fe2+) Chloride (Cl-) Sulfate (SO4 2-) Calcium (Ca2+) Magnesium (Mg2+) Total Hardness Linear Viscosity Water pH Gel pH Post-Crosslink pH Crosslink Bacteria - °F mg/L mg/L mg/L mg/L mg/L mg/L cP - - - (Y/N) BQ Value Tank # H2S present? Y/N Hydrometer Digital Thermometer Strip Strip Strip Titration Total Hardness Minus Calcium Titration FANN-35 Probe Probe Probe - Mycometer 1 N 1.024 106.5 0 16,460 1,200 3,000 400 3,400 20,233 2 N 1.026 106.5 0 16,460 1,200 3,000 400 3,400 5,356 3 N 1.024 100.0 0 16,460 1,200 3,000 800 3,800 1,471 4 N 1.026 100.0 0 15,230 1,200 3,000 600 3,600 1,788 5 N 1.024 100.0 0 15,230 1,200 3,000 600 3,600 3,710 6 N 1.024 100.0 0 15,230 1,200 2,800 600 3,400 7,472 7 N 1.024 100.0 0 17,790 1,200 2,600 400 3,000 10,608 8 N 1.024 102.0 0 15,230 1,200 2,600 400 3,000 17,411 9 N 1.026 100.0 0 15,230 1,200 3,000 400 3,400 28,922 10 N 1.024 100.0 0 16,460 1,200 2,800 600 3,400 21,374 11 N 1.024 102.0 0 16,460 1,200 2,200 1,000 3,200 14,383 12 N 1.024 100.0 0 17,790 1,200 2,200 1,000 3,200 31,386 13 N 1.026 100.0 0 17,790 1,200 2,600 600 3,200 33,615 14 N 1.024 100.0 0 19,240 1,200 2,600 1,000 3,600 25,270 15 N 1.024 102.0 0 17,790 1,200 2,600 1,000 3,600 30,680 16 N 1.024 102.0 0 19,240 1,200 3,200 400 3,600 10,827 17 N 1.024 100.0 0 19,240 1,200 3,000 400 3,400 15,307 18 N 1.024 100.0 0 15,230 1,200 3,000 400 3,400 8,029 19 N 1.026 100.0 0 15,230 1,200 3,000 400 3,400 22,599 20 N 1.024 102.0 0 15,230 1,200 3,200 400 3,600 14,379 21 N 1.024 102.0 0 15,230 1,200 3,200 800 4,000 13,091 22 N 1.024 102.0 0 16,460 1,200 3,200 400 3,600 10,665 23 N 1.026 102.0 0 16,460 1,200 1,840 1,360 3,200 9,893 24 N 1.026 100.0 0 16,460 1,200 3,000 400 3,400 11,763 25 N 1.024 102.0 0 17,790 1,200 3,000 600 3,600 15,174 Average 1.025 0 13,401 1200 2,279 495 2,774 26.0 7.27 7.59 9.24 - 15,416 Maximum 1.026 0 19,240 1,200 3,200 1,360 4,000 28.0 7.40 7.71 9.30 - 33,615 Minimum 1.024 0 15,230 1,200 1,840 400 3,000 25.00 7.20 7.40 9.20 - 1,471 Range 0.002 0 4,010 0 1,360 960 1,000 3.0 0.20 0.31 0.10 - 32,145 Alaska District Field QC Prejob Water Analysis on Location Company:Conoco Phillips Well Name:3T-613 Water Source:CPF3 Y 26.0 7.2 7.7 9.3 Y 25.0 7.2 7.4 9.2 25.0 7.30 7.71 9.30 Y 28.0 7.2 7.7 9.2 y 25.0 7.4 7.6 9.2 Y 27.0 7.3 7.4 9.3 Y Conoco Phillips - 3T-613 Water Analysis 6-17 202 Specific Gravity Testing Temperature Dissolved Iron (Fe2+) Chloride (Cl-) Sulfate (SO4 2-) Calcium (Ca2+) Magnesium (Mg2+) Total Hardness Linear Viscosity Water pH Gel pH Post-Crosslink pH Crosslink Bacteria - °F mg/L mg/L mg/L mg/L mg/L mg/L cP - - - (Y/N) BQ Value Tank # H2S present? Y/N Hydrometer Digital Thermometer Strip Strip Strip Titration Total Hardness Minus Calcium Titration FANN-35 Probe Probe Probe - Mycometer 3 N 1.026 65.8 0 16,460 1,200 2,200 1,600 3,800 3,651 4 N 1.026 66.1 0 16,460 1,200 2,200 1,400 3,600 7,708 5 N 1.026 65.5 0 17,790 1,200 2,600 1,000 3,600 1,860 6 N 1.026 66.0 0 17,790 1,200 2,600 800 3,400 7,568 7 N 1.024 64.9 0 19,240 1,200 2,600 400 3,000 6,824 13 N 1.024 65.0 0 15,230 1,200 2,600 600 3,200 13,798 14 N 1.024 64.8 0 15,230 1,200 2,600 1,000 3,600 21,939 17 N 1.024 65.1 0 16,460 1,200 3,200 200 3,400 10,198 18 N 1.026 66.5 0 16,460 1,200 3,000 600 3,600 8,128 22 N 1.026 67.5 0 16,460 1,200 3,200 400 3,600 13,476 23 N 1.026 66.3 0 15,230 1,200 1,840 1,360 3,200 2,268 24 N 1.026 65.8 0 15,230 1,200 3,200 200 3,400 5,600 25 N 1.026 67.4 0 15,230 1,200 3,000 0 3,000 23,857 Average 1.025 0 7,902 1200 1,685 592 25.7 7.28 7.39 9.17 - 14,104 Maximum 1.026 0 19,240 1,200 3,200 3,400 3,800 27.0 7.30 7.43 9.20 - 31,386 Minimum 1.024 0 0 1,200 0 0 0 25.00 7.20 7.30 9.10 - 1,860 Range 0.002 0 19,240 0 3,200 3,400 3,800 2.0 0.10 0.13 0.10 - 29,526 Alaska District Field QC Prejob Water Analysis on Location Company:Conoco Phillips Well Name:3T-613 Water Source:CPF3 Y 25.0 7.3 7.4 9.2 Y 25.0 7.3 7.4 9.1 25.0 7.30 7.30 9.20 Y 27.0 7.2 7.4 9.2 y 25.0 7.3 7.4 9.2 Y 27.0 7.3 7.4 9.1 Y Conoco Phillips - 3T-613 Water Analysis 6-18 203 Specific Gravity Testing Temperature Dissolved Iron (Fe2+) Chloride (Cl-) Sulfate (SO4 2-) Calcium (Ca2+) Magnesium (Mg2+) Total Hardness Linear Viscosity Water pH Gel pH Post-Crosslink pH Crosslink Bacteria - °F mg/L mg/L mg/L mg/L mg/L mg/L cP - - - (Y/N) BQ Value Tank # H2S present? Y/N Hydrometer Digital Thermometer Strip Strip Strip Titration Total Hardness Minus Calcium Titration FANN-35 Probe Probe Probe - Mycometer 3 N 1.026 88.0 0 16,460 1,200 2,600 1,200 3,800 13,780 25 N 1.026 85.0 0 15,230 1,200 3,000 400 3,400 18,899 Average 1.025 0 15,845 1200 2,800 800 3,600 28.0 7.20 7.40 9.30 - 14,311 Maximum 1.026 0 16,460 1,200 3,000 1,200 3,800 28.0 7.20 7.40 9.30 - 31,386 Minimum 1.024 0 15,230 1,200 2,600 400 3,400 28.00 7.20 7.40 9.30 - 1,860 Range 0.002 0 1,230 0 400 800 400 0.0 0.00 0.00 0.00 - 29,526 Alaska District Field QC Prejob Water Analysis on Location Company:Conoco Phillips Well Name:3T-613 Water Source:CPF3 y28.0 7.2 7.4 9.3 Conoco Phillips - 3T-613 Water Analysis 6-19 204 Specific Gravity Testing Temperature Dissolved Iron (Fe2+) Chloride (Cl-) Sulfate (SO4 2-) Calcium (Ca2+) Magnesium (Mg2+) Total Hardness Linear Viscosity Water pH Gel pH Post-Crosslink pH Crosslink Bacteria - °F mg/L mg/L mg/L mg/L mg/L mg/L cP - - - (Y/N) BQ Value Tank # H2S present? Y/N Hydrometer Digital Thermometer Strip Strip Strip Titration Total Hardness Minus Calcium Titration FANN-35 Probe Probe Probe - Mycometer 1 N 1.020 80.0 2 5,260 400 2,000 1,200 3,200 1,492 2 N 1.020 80.0 0 6,290 200 2,000 1,200 3,200 1,946 3 N 1.000 80.0 0 6,290 200 2,000 1,000 3,000 1,861 4 N 1.000 80.0 2 6,290 400 2,000 1,200 3,200 1,234 5 N 1.000 80.0 0 7,460 400 2,000 1,200 3,200 1,977 6 N 1.000 80.0 2 11,170 400 2,000 1,200 3,200 2,837 7 N 1.000 80.0 0 11,170 400 1,800 1,400 3,200 3,786 8 N 1.000 80.0 2 9,540 400 1,800 1,600 3,400 7,092 9 N 1.000 80.0 0 9,540 200 1,800 1,800 3,600 2,941 10 N 1.000 80.0 0 11,170 800 1,800 1,400 3,200 2,087 11 N 1.000 80.0 0 11,170 400 2,000 1,600 3,600 2,890 12 N 1.000 80.0 2 7,460 200 2,000 1,000 3,000 2,588 13 N 1.000 80.0 2 10,320 200 1,600 1,800 3,400 6,043 14 N 1.000 80.0 2 7,460 400 1,600 1,800 3,400 5,628 15 N 1.000 80.0 2 10,320 800 2,000 1,400 3,400 3,269 16 N 1.000 80.0 2 11,170 800 2,000 1,200 3,200 6,249 17 N 1.000 80.0 2 11,170 400 2,000 1,000 3,000 6,366 18 N 1.000 80.0 2 9,540 400 1,800 1,800 3,600 2,650 19 N 1.000 80.0 2 11,170 400 1,800 1,800 3,600 2,096 20 N 1.000 80.0 2 9,540 400 2,000 1,600 3,600 9,834 21 N 1.000 80.0 2 8,110 800 2,000 1,600 3,600 7,016 22 N 1.000 80.0 2 8,110 800 2,000 1,400 3,400 6,276 23 N 1.000 80.0 2 8,110 800 2,000 1,400 3,400 5,770 24 N 1.000 80.0 2 5,260 1,200 2,000 1,400 3,400 5,184 25 N 1.020 80.0 0 12,070 1,200 2,000 1,200 3,200 4,455 Average 1.002 1 9,006 520 1,920 1408 3,328 25.2 7.20 7.50 9.35 - 4,143 Maximum 1.020 0 12,070 1,200 2,000 1,800 3,600 26.0 7.20 7.60 9.40 - 9,834 Minimum 1.000 0 5,260 200 1,600 1,000 3,000 25.00 7.20 7.40 9.30 - 1,234 Range 0.020 0 6,810 1,000 400 800 600 1.0 0.00 0.20 0.10 - 8,599 Alaska District Field QC Prejob Water Analysis on Location Company:Conoco Phillips Well Name:3T-613 Water Source:CPF3 Y 25.0 7.2 7.5 9.3 Y 25.0 7.2 7.6 9.4 25.0 7.2 7.4 9.4 Y 26.0 7.20 7.50 9.30 Y 25.0 7.2 7.5 9.4 Y Conoco Phillips - 3T-613 Water Analysis 6-20 205 Specific Gravity Testing Temperature Dissolved Iron (Fe2+) Chloride (Cl-) Sulfate (SO4 2-) Calcium (Ca2+) Magnesium (Mg2+) Total Hardness Linear Viscosity Water pH Gel pH Post-Crosslink pH Crosslink Bacteria - °F mg/L mg/L mg/L mg/L mg/L mg/L cP - - - (Y/N) BQ Value Tank # H2S present? Y/N Hydrometer Digital Thermometer Strip Strip Strip Titration Total Hardness Minus Calcium Titration FANN-35 Probe Probe Probe - Mycometer 1 N 1.020 80.0 2 5,260 400 2,000 1,200 3,200 1,492 2 N 1.020 80.0 0 6,290 200 2,000 1,200 3,200 1,946 3 N 1.000 85.2 2 8,800 400 2,400 1,000 3,400 2,232 4 N 1.000 86.3 2 8,800 200 2,200 1,400 3,600 1,860 5 N 1.000 87.0 0 9,540 200 2,200 1,000 3,200 1,002 6 N 1.000 85.9 0 6,290 400 2,600 600 3,200 1,285 7 N 1.000 88.0 0 6,860 200 2,400 1,200 3,600 1,600 8 N 1.000 90.3 0 6,290 200 2,600 1,000 3,600 4,047 9 N 1.000 88.2 2 6,860 400 2,000 1,200 3,200 3,880 10 N 1.000 90.5 2 9,540 400 2,000 1,600 3,600 4,424 11 N 1.000 87.5 0 9,540 400 2,000 1,400 3,400 4,345 12 N 1.000 88.0 0 6,290 200 2,200 1,200 3,400 5,769 13 N 1.000 89.0 0 6,290 200 2,400 1,000 3,400 5,258 14 N 1.000 90.2 2 5,260 200 2,400 800 3,200 6,161 Average 1.002 1 7,279 286 2,243 1129 3,371 25.3 7.20 7.57 9.33 - 3,236 Maximum 1.020 0 9,540 400 2,600 1,600 3,600 26.0 7.20 7.60 9.40 - 6,161 Minimum 1.000 0 5,260 200 1,800 600 3,000 25.00 7.20 7.40 9.30 - 1,002 Range 0.020 0 4,280 200 800 1,000 600 1.0 0.00 0.20 0.10 - 5,159 Alaska District Field QC Prejob Water Analysis on Location Company:Conoco Phillips Well Name:3T-613 Water Source:CPF3 Y 25.0 7.2 7.5 9.3 Y 25.0 7.2 7.6 9.4 26.0 7.20 7.60 9.30 Y Conoco Phillips - 3T-613 Water Analysis 6-21 206 Customer:Well:Date:Formation:SO#:Tank Type Water Source Inches Gallons BarrelsTemperature (°F)Inches Gallons Barrels1 Atigan 3J 105 19,949 475 99 105 19,949 4752 Atigan 3J 105 19,949 475 105 105 19,949 4753 Atigan 3J 105 19,949 475 100 10 1,627 394 Atigan 3J 105 19,949 475 104 10 1,627 395 Atigan 3J 105 19,949 475 110 10 1,627 396 Atigan 3J 105 19,949 475 110 10 1,627 397 Atigan 3J 88 16,660 397 102 88 16,660 3978 Atigan 3J 86 16,273 387 98 86 16,273 3879 Atigan 3J 105 19,949 475 100 105 19,949 47510 Atigan 3J 105 19,949 475 98 105 19,949 47511 Atigan 3J 92 17,434 415 90 92 17,434 41512 Atigan 3J 100 18,981 452 95 100 18,981 45213 Wichita 3J 100 20,160 480 95 100 20,160 48014 Wichita 3J 100 20,160 480 90 100 20,160 48015 Wichita 3J 100 20,160 480 95 100 20,160 48016 Wichita 3J 100 20,160 480 90 100 20,160 48017 Wichita 3J 100 20,160 480 100 10 1,890 4518 Wichita 3J 100 20,160 480 100 10 1,890 4519 Wichita 3J 92 18,480 440 95 92 18,480 44020 Wichita 3J 100 20,160 480 101 10 1,890 4521 Wichita 3J 100 20,160 480 102 10 1,890 4522 Wichita 3J 100 20,160 480 96 10 1,890 4523 Wichita 3J 79 15,750 375 95 10 1,890 4524 Wichita 3J 85 17,010 405 95 10 1,890 4525 Wichita 3J 100 20,160 480 92 10 1,890 4523 Wichita 3J 100 20,160 480 96 100 20,160 48024 Wichita 3J 100 20,160 480 95 100 20,160 48025 Wichita 3J 100 20,160 480 98 100 20,160 480Gallons Barrels Gallons Barrels Gallons Barrels542,259 12,911 330,372 7,866 211,887 5,045Conoco Phillips 3T-6136/16/2025A-Sand910128224GeneralBeginning StrapEnding StrapLocation SummaryStarting VolumeEnding VolumeTotal UsedConoco Phillips - 3T-613Water Straps 6-16207 Customer:Well:Date:Formation:SO#:Tank Type Water Source Inches Gallons BarrelsTemperature (°F)Inches Gallons Barrels1 Atigan 3J 100 18,981 452 97 100 18,981 4522 Atigan 3J 97 18,401 438 110 97 18,401 4383 Atigan 3J 97 18,401 438 110 10 1,627 394 Atigan 3J 99 18,788 447 107 10 1,627 395 Atigan 3J 100 18,981 452 98 10 1,627 396 Atigan 3J 95 18,014 429 98 10 1,627 397 Atigan 3J 99 18,788 447 102 10 1,627 398 Atigan 3J 99 18,788 447 99 99 18,788 4479 Atigan 3J 99 18,788 447 98 99 18,788 44710 Atigan 3J 100 18,981 452 100 100 18,981 45211 Atigan 3J 99 18,788 447 101 99 18,788 44712 Atigan 3J 99 18,788 447 97 99 18,788 44713 Wichita 3J 100 20,160 480 92 10 1,890 4514 Wichita 3J 98 19,740 470 100 10 1,890 4515 Wichita 3J 103 20,790 495 96 103 20,790 49516 Wichita 3J 104 21,000 500 95 104 21,000 50017 Wichita 3J 104 21,000 500 98 10 1,890 4518 Wichita 3J 102 20,580 490 102 10 1,890 4519 Wichita 3J 102 20,580 490 91 102 20,580 49020 Wichita 3J 99 19,950 475 91 99 19,950 47521 Wichita 3J 105 21,000 500 99 105 21,000 50022 Wichita 3J 104 21,000 500 96 10 1,890 4523 Wichita 3J 104 21,000 500 105 10 1,890 4524 Wichita 3J 110 21,000 500 100 10 1,890 4525 Wichita 3J 103 20,790 495 98 10 1,890 45Gallons Barrels Gallons Barrels Gallons Barrels493,078 11,740 258,091 6,145 234,987 5,595Conoco Phillips 3T-6136/17/2025A-Sand910128224GeneralBeginning StrapEnding StrapLocation SummaryStarting VolumeEnding VolumeTotal UsedConoco Phillips - 3T-613Water Straps 6-17208 Customer:Well:Date:Formation:SO#:Tank Type Water Source Inches Gallons BarrelsTemperature (°F)Inches Gallons Barrels1 Atigan 3J 103 19,562 466 103 103 19,562 4662 Atigan 3J 105 19,949 475 98 105 19,949 4753 Atigan 3J 102 19,368 461 92 10 1,627 394 Atigan 3J 102 19,368 461 93 102 19,368 4615 Atigan 3J 102 19,368 461 98 102 19,368 4616 Atigan 3J 103 19,562 466 100 103 19,562 4667 Atigan 3J 104 19,755 470 100 104 19,755 4708 Atigan 3J 105 19,949 475 100 105 19,949 4759 Atigan 3J 101 19,175 457 90 101 19,175 45710 Atigan 3J 101 19,175 457 92 101 19,175 45711 Atigan 3J 105 19,949 475 100 105 19,949 47512 Atigan 3J 103 19,562 466 97 103 19,562 46613 Wichita 3J 100 20,160 480 100 100 20,160 48014 Wichita 3J 100 20,160 480 102 100 20,160 48015 Wichita 3J 100 20,160 480 105 100 20,160 48016 Wichita 3J 98 19,740 470 105 98 19,740 47017 Wichita 3J 97 19,530 465 98 97 19,530 46518 Wichita 3J 95 19,110 455 97 95 19,110 45519 Wichita 3J 99 19,950 475 98 99 19,950 47520 Wichita 3J 100 20,160 480 102 100 20,160 48021 Wichita 3J 98 19,740 470 100 98 19,740 47022 Wichita 3J 102 20,580 490 108 102 20,580 49023 Wichita 3J 100 20,160 480 100 50 9,660 23024 Wichita 3J 99 19,950 475 104 50 9,660 23025 Wichita 3J 99 19,950 475 102 10 1,890 45Gallons Barrels Gallons Barrels Gallons Barrels494,090 11,764 437,499 10,417 56,591 1,347Conoco Phillips 3T-6136/18/2025A-Sand910128224GeneralBeginning StrapEnding StrapLocation SummaryStarting VolumeEnding VolumeTotal UsedConoco Phillips - 3T-613Water Straps 6-18209 Customer:Well:Date:Formation:SO#:Tank Type Water Source Inches Gallons BarrelsTemperature (°F)Inches Gallons Barrels1 Atigan 3J 104 19,755 470 98 104 19,755 4702 Atigan 3J 105 19,949 475 94 105 19,949 4753 Atigan 3J 104 19,755 470 90 10 1,627 394 Atigan 3J 104 19,755 470 94 10 1,627 395 Atigan 3J 105 19,949 475 97 10 1,627 396 Atigan 3J 104 19,755 470 99 10 1,627 397 Atigan 3J 105 19,949 475 97 10 1,627 398 Atigan 3J 104 19,755 470 97 10 1,627 399 Atigan 3J 105 19,949 475 91 10 1,627 3910 Atigan 3J 105 19,949 475 91 10 1,627 3911 Atigan 3J 104 19,755 470 96 10 1,627 3912 Atigan 3J 105 19,949 475 96 10 1,627 3913 Wichita 3J 99 19,950 475 98 10 1,890 4514 Wichita 3J 101 20,370 485 100 10 1,890 4515 Wichita 3J 100 20,160 480 105 10 1,890 4516 Wichita 3J 103 20,790 495 104 10 1,890 4517 Wichita 3J 100 20,160 480 96 10 1,890 4518 Wichita 3J 100 20,160 480 95 10 1,890 4519 Wichita 3J 99 19,950 475 96 10 1,890 4520 Wichita 3J 99 19,950 475 100 10 1,890 4521 Wichita 3J 109 21,000 500 98 10 1,890 4522 Wichita 3J 100 20,160 480 105 10 1,890 4523 Wichita 3J 101 20,370 485 101 10 1,890 4524 Wichita 3J 100 20,160 480 104 10 1,890 4525 Wichita 3J 102 20,580 490 107 10 1,890 4525 Wichita 3J 100 20,160 480 100 100 20,160 48024 Wichita 3J 100 20,160 480 100 100 20,160 48023 Wichita 3J 100 20,160 480 100 100 20,160 48022 Wichita 3J 100 20,160 480 100 100 20,160 48021 Wichita 3J 100 20,160 480 100 100 20,160 480Gallons Barrels Gallons Barrels Gallons Barrels602,783 14,352 181,345 4,318 421,439 10,034GeneralBeginning StrapEnding StrapLocation SummaryStarting VolumeEnding VolumeTotal UsedConoco Phillips 3T-6136/19/2025A-Sand910128224Conoco Phillips - 3T-613Water Straps 6-19210 Customer:Well:Date:Formation:SO#:Tank Type Water Source Inches Gallons BarrelsTemperature (°F)Inches Gallons Barrels1 Atigan 3J 100 18,981 452 98 100 18,981 4522 Atigan 3J 105 19,949 475 94 105 19,949 4753 Atigan 3J 105 19,949 475 90 10 1,627 394 Atigan 3J 105 19,949 475 94 10 1,627 395 Atigan 3J 105 19,949 475 97 10 1,627 396 Atigan 3J 105 19,949 475 99 10 1,627 397 Atigan 3J 105 19,949 475 97 10 1,627 398 Atigan 3J 105 19,949 475 97 10 1,627 399 Atigan 3J 106 20,142 480 91 10 1,627 3910 Atigan 3J 106 20,142 480 91 10 1,627 3911 Atigan 3J 104 19,755 470 96 10 1,627 3912 Atigan 3J 103 19,562 466 96 10 1,627 3913 Wichita 3J 105 21,000 500 98 10 1,890 4514 Wichita 3J 100 20,160 480 100 10 1,890 4515 Wichita 3J 99 19,950 475 105 10 1,890 4516 Wichita 3J 100 20,160 480 104 10 1,890 4517 Wichita 3J 90 18,060 430 96 10 1,890 4518 Wichita 3J 101 20,370 485 95 10 1,890 4519 Wichita 3J 103 20,790 495 96 10 1,890 4520 Wichita 3J 103 20,790 495 100 10 1,890 4521 Wichita 3J 101 20,370 485 98 10 1,890 4522 Wichita 3J 100 20,160 480 105 10 1,890 4523 Wichita 3J 103 20,790 495 101 10 1,890 4524 Wichita 3J 99 19,950 475 104 10 1,890 4525 Wichita 3J 99 19,950 475 107 52 10,080 24024 Wichita 3J 100 20,160 480 100 45 8,610 20523 Wichita 3J 100 20,160 480 100 45 8,610 20522 Wichita 3J 75 14,910 355 100 30 5,670 13521 Wichita 3J 100 20,160 480 100 100 20,160 480Gallons Barrels Gallons Barrels Gallons Barrels576,113 13,717 131,011 3,119 445,102 10,598Conoco Phillips 3T-6136/20/2025A-Sand910128224GeneralBeginning StrapEnding StrapLocation SummaryStarting VolumeEnding VolumeTotal UsedConoco Phillips - 3T-613Water Straps 6-20211 Customer:Well:Date:Formation:SO#:Tank Type Water Source Inches Gallons Barrels Temperature (°F) Inches Gallons Barrels1 Atigan 3J 103 19,562 466 95 95 18,014 4292 Atigan 3J 100 18,981 452 100 95 18,014 4293 Atigan 3J 99 18,788 447 99 55 10,159 2424 Atigan 3J 99 18,788 447 102 10 1,627 395 Atigan 3J 98 18,595 443 102 10 1,627 396 Atigan 3J 97 18,401 438 103 10 1,627 397 Atigan 3J 99 18,788 447 103 10 1,627 398 Atigan 3J 99 18,788 447 98 10 1,627 399 Atigan 3J 104 19,755 470 99 10 1,627 3910 Atigan 3J 105 19,949 475 98 10 1,627 3911 Atigan 3J 100 18,981 452 100 10 1,627 3912 Atigan 3J 105 19,949 475 104 10 1,627 3913 Wichita 3J 99 19,950 475 103 10 1,890 4514 Wichita 3J 101 20,370 485 105 10 1,890 45Gallons Barrels Gallons Barrels Gallons Barrels269,644 6,420 64,612 1,538 205,033 4,882GeneralBeginning StrapEnding StrapLocation SummaryStarting VolumeEnding VolumeTotal UsedConoco Phillips 3T-6136/21/2025A-Sand910128224Conoco Phillips - 3T-613 Water Straps 6-21212 Linear Linear XL XL XL Lip time #NAME? Linear Linear XL XL XL Lip time #NAME? Linear Linear XL XL XL Lip time Interval Stage Visc pH Temp °F pH min Interval Stage Visc pH Temp °F pH min Interval Stage Visc pH Temp °F pH min 1 Pad 25 7 85 8.96 0 11 Pad 25 7 90 9.3 0 21 Pad 25 7.1 95 9.3 0 .25# 27 7 95 9.22 0 26 Avg Linear Visc .25# 24 7.1 92 9.25 0 26 Avg Linear Visc .25# 25 7 90 9.3 0 1.00# 27 7 97 9.25 0 94.5 Avg XLTemp 1.00# 25 7 90 9.3 0 93.2 Avg XLTemp 1.00# 26 7.1 93 9.3 0 2.00# 25 7 95 9.2 0 9.2 Avg XL pH 2.00# 26 7 97 9.3 0 9.32 Avg XL pH 2.00# 25 7 95 9.3 0 3.00# 25 7.2 97 9.2 0 3.00# 26 7.1 93 9.3 0 3.00# 25 7 95 9.4 0 4.00# 27 7.2 97 9.2 0 4.00# 26 7 97 9.3 0 4.00# 25 7 97 9.4 0 4.50# 25 7 95 9.2 0 4.50# 26 7 95 9.3 0 4.50# 25 7.1 96 9.4 0 5.00# 25 7 95 9.2 0 5.00# 27 7.2 90 9.4 0 5.00# 5.50# 26 7.2 95 9.4 0 6.00# 26 7.1 90 9.3 0 6.50# 7.00# 2 Pad 22 7 88 9 0 12 Pad 26 7 93 9.3 0 22 Pad .25# 25 7 90 9.2 0 .25# 26 7.1 95 9.3 0 .25# 1.00# 27 7.1 97 9.2 0 1.00# 26 7 97 9.3 0 1.00# 2.00# 27 7 95 9.2 0 26 Avg Linear Visc 2.00# 26 7 92 9.35 0 26 Avg Linear Visc 2.00# 3.00# 25 7 95 9.2 0 94.6 Avg XLTemp 3.00# 26 7.1 92 9.4 0 93.0 Avg XLTemp 3.00# 4.00# 25 7.1 97 9.2 0 9.2 Avg XL pH 4.00# 26 7.1 94 9.4 0 9.32 Avg XL pH 4.00# 4.50# 27 7 95 9.2 0 4.50# 26 7 90 9.27 0 4.50# 5.00# 27 6.9 97 9.2 0 5.00# 26 7 92 9.25 0 5.00# 5.50# 27 6.9 97 9.2 0 5.50# 26 7 92 9.3 0 5.50# 6.00# 26 7.1 93 9.3 0 6.00# 6.50#6.50# 7.00#7.00# 3 Pad 27 7.2 90 9.2 0 13 Pad 25 7.2 92 9.2 0 23 Pad .25# 27 7.2 95 9.3 0 .25# 25 7.1 90 9.25 0 .25# 1.00# 27 7.1 100 9.2 0 1.00# 25 7.1 90 9.25 0 1.00# 2.00# 27 7.1 100 9.2 0 27 Avg Linear Visc 2.00# 26 7 95 9.2 0 25 Avg Linear Visc 2.00# 3.00# 27 7 100 9.2 0 97.4 Avg XLTemp 3.00# 26 7.1 92 9.1 0 92.3 Avg XLTemp 3.00# 4.00# 27 7.2 97 9.3 0 9.2 Avg XL pH 4.00# 25 7 92 9.2 0 9.20 Avg XL pH 4.00# 5.00# 27 7.2 98 9.2 0 4.50# 25 7.1 95 9.2 0 4.50# 6.00# 27 7.2 99 9.3 0 5.00# 25 7.1 95 9.2 0 5.00# 5.50# 26 7.2 92 9.2 0 5.50# 6.00# 26 7.2 90 9.2 0 6.00# 6.50# 26 7 92 9.25 0 6.50# 7.00#7.00# 4 Pad 27 7 100 9.3 0 14 Pad 24 7.2 95 9.45 0 24 Pad .25# 27 7 95 9.3 0 .25# 25 7.2 100 9.5 0 .25# 1.00# 27 7 95 9.4 0 1.00# 25 7.2 97 9.5 0 1.00# 2.00# 27 7 97 9.3 0 27.00 Avg Linear Visc 2.00# 25 Avg Linear Visc 2.00# 3.00# 27 7.1 100 9.3 0 97.44 Avg XLTemp 3.00# 25 7.2 95 9.4 0 96.1 Avg XLTemp 3.00# 4.00# 27 7.1 98 9.3 0 9.28 Avg XL pH 4.00# 25 7.2 95 9.45 0 9.45 Avg XL pH 4.00# 5.00# 27 7 100 9.25 0 4.50#4.50# 6.00# 27 7 97 9.2 0 5.00# 25 7.2 92 9.45 0 5.00# 6.50# 27 7 95 9.2 0 5.50# 26 7.1 100 9.45 0 5.50# 6.00# 25 7.2 95 9.4 0 6.00# 6.50#6.50# 7.00#7.00# 5 Pad 27 7 95 9.3 0 15 Pad 25 7.2 97 9.4 0 25 Pad .25# 27 7.1 100 9.2 0 .25# 25 7.2 95 9.4 0 .25# 1.00# 27 7.1 97 9.3 0 1.00# 24 7.2 92 9.34 0 1.00# 2.00# 27 7 95 9.2 0 27.00 Avg Linear Visc 2.00# 25 Avg Linear Visc 2.00# 3.00# 27 7 97 9.2 0 96.17 Avg XLTemp 3.00# 24 7.2 92 9.35 0 92.8 Avg XLTemp 3.00# 4.00# 27 7 100 9.2 0 9.28 Avg XL pH 4.00# 25 7.1 90 9.35 0 9.36 Avg XL pH 4.00# 4.50# 27 7.1 95 9.3 0 4.50# 25 7.1 92 9.35 0 4.50# 5.00# 27 7 95 9.4 0 5.00#5.00# 5.50# 27 7 95 9.3 0 5.50# 25 7.1 95 9.37 0 5.50# 6.00# 27 7 95 9.3 0 6.00# 25 7.1 90 9.35 0 6.00# 6.50# 27 7 95 9.3 0 6.50# 25 7.1 92 9.35 0 6.50# 7.00# 27 7 95 9.3 0 7.00#7.00# 6 Pad 27 7 95 9.38 0 16 Pad 25 7.2 92 9.3 0 26 Pad .25# 28 7 95 9.3 0 .25# 25 7.1 95 9.35 0 .25# 1.00# 28 7 95 9.3 0 1.00# 24 7.1 97 9.3 0 1.00# 2.00# 28 7 95 9.3 0 28.08 Avg Linear Visc 2.00# 25 7.1 95 9.35 0 25 Avg Linear Visc 2.00# 3.00# 29 7 95 9.2 0 94.58 Avg XLTemp 3.00# 94.8 Avg XLTemp 3.00# 4.00# 28 7 95 9.2 0 9.30 Avg XL pH 4.00# 25 7.2 95 9.35 0 9.35 Avg XL pH 4.00# 4.50# 28 7.1 95 9.2 0 4.50# 25 7.1 92 9.35 0 4.50# 5.00# 30 7.1 92 9.40 0 5.00# 25 7.1 95 9.32 0 5.00# 5.50# 28 7.1 93 9.40 0 5.50# 25 7.1 97 9.33 0 5.50# 6.00# 28 7.1 95 9.35 0 6.00# 25 7.1 95 9.4 0 6.00# 6.50# 28 7 95 9.3 0 6.50# 25 7.2 95 9.4 0 6.50# 7.00# 27 7 95 9.3 0 7.00#7.00# 7 Pad 29 7.2 87 9.4 0 17 Pad 25 7.2 100 9.3 0 27 Pad .25# 30 7.2 95 9.4 0 .25# 25 7.2 102 9.35 0 .25# 1.00# 30 7 95 9.45 0 1.00# 25 7.1 105 9.25 0 1.00# 2.00# 30 7.1 92 9.45 0 29 Avg Linear Visc 2.00# 25 7.1 105 9.25 0 25 Avg Linear Visc 2.00# 3.00# 30 7 92 9.3 0 92.2 Avg XLTemp 3.00# 25 7 108 9.3 0 102.4 Avg XLTemp 3.00# 4.00# 29 7 90 9.4 0 9.4 Avg XL pH 4.00# 25 7 97 9.2 0 9.29 Avg XL pH 4.00# 4.50# 30 7 95 9.4 0 4.50#4.50# 5.00# 28 7 92 9.4 0 5.00# 25 7 100 9.3 0 5.00# 5.50# 29 7.1 92 9.4 0 5.50# 25 7.1 100 9.3 0 5.50# 6.00# 29 7.1 92 9.4 0 6.00# 25 7 102 9.3 0 6.00# 6.50#6.50# 25 7.1 105 9.3 0 6.50# 7.00#7.00#7.00# 8 Pad 26 7.1 88 9.26 0 18 Pad 24 7.2 100 9.2 0 28 Pad .25# 28 7.1 90 9.45 0 .25# 24 7.2 102 9.2 0 .25# 1.00# 28 7 90 9.5 0 1.00# 25 7.2 100 9.2 0 1.00# 2.00# 30 7 95 9.45 0 28.55 Avg Linear Visc 2.00# 25 7.1 97 9.2 0 25 Avg Linear Visc 2.00# 3.00# 30 7 95 9.5 0 93.18 Avg XLTemp 3.00# 25 7.1 95 9.2 0 96.7 Avg XLTemp 3.00# 4.00# 30 7 95 9.5 0 9.45 Avg XL pH 4.00# 25 7.1 97 9.2 0 9.2 Avg XL pH 4.00# 4.50# 30 7.1 95 9.5 0 4.50# 25 7.1 95 9.3 0 4.50# 5.00# 29 7 95 9.45 0 5.00# 26 7.2 95 9.25 0 5.00# 5.50# 28 7 95 9.45 0 5.50# 26 7.2 96 9.25 0 5.50# 6.00# 28 7 92 9.45 0 6.00# 25 7.1 92 9.3 0 6.00# 6.50# 27 7 95 9.4 0 6.50# 25 7.1 95 9.3 0 6.50# 7.00#7.00#7.00# 9 Pad 26 7 90 9.4 0 19 Pad 25 7.1 97 9.3 0 29 Pad .25# 26 7 92 9.4 0 .25# 25 7.1 95 9.3 0 .25# 1.00# 25 7 95 9.25 0 1.00# 26 7.1 98 9.3 0 1.00# 2.00# 26 7 95 9.25 0 26 Avg Linear Visc 2.00# 25 7.1 95 9.3 0 25 Avg Linear Visc 2.00# 3.00# 26 7.1 95 9.25 0 93.2 Avg XLTemp 3.00# 25 7 95 9.3 0 97.9 Avg XLTemp 3.00# 4.00# 26 7.1 95 9.27 0 9.34 Avg XL pH 4.00# 26 7.1 98 9.3 0 9.3 Avg XL pH 4.00# 4.50# 26 7 95 9.27 0 4.50# 25 7.1 99 9.3 0 4.50# 5.00# 26 7 92 9.4 0 5.00# 25 7.1 100 9.3 0 5.00# 5.50# 25 7 92 9.4 0 5.50# 25 7.1 100 9.35 0 5.50# 6.00# 25 7.1 92 9.4 0 6.00# 25 7.1 100 9.3 0 6.00# 6.50# 25 7 92 9.4 0 6.50# 26 7.1 100 9.3 0 6.50# 7.00#7.00#7.00# 10 Pad 25 7 98 9.4 0 20 Pad 26 7 97 9.2 0 30 Pad .25# 25 7.1 92 9.4 0 .25# 25 7.1 95 9.3 0 .25# 1.00# 25 7.1 90 9.4 0 1.00# 25 7.1 95 9.35 0 1.00# 2.00# 26 7 92 9.25 0 25 Avg Linear Visc 2.00# 24 7.1 92 9.4 0 25 Avg Linear Visc 2.00# 3.00# 26 7.1 92 9.25 0 91.6 Avg XLTemp 3.00# 25 7.1 98 9.45 0 95.9 Avg XLTemp 3.00# 4.00# 25 7 90 9.3 0 9.35 Avg XL pH 4.00# 25 7 95 9.45 0 9.4 Avg XL pH 4.00# 4.50# 25 7 92 9.3 0 . 4.50# 25 7 97 9.5 0 4.50# 5.00# 26 7.1 90 9.4 0 5.00# 25 7.1 98 9.45 0 5.00# 5.50# 26 7.1 90 9.4 0 5.50# 6.00# 26 7.1 92 9.4 0 6.00# 6.50# 25 7 90 9.4 0 6.50# 7.00# 7.00# Customer:CONOCO PHILLIPS Wellname & #:3T-613 Date:June 16, 2025 Comments Comments Comments Comments Comments Comments Comments Comments Comments Comments Comments Comments Comments Comments Comments Comments Comments Comments Comments Comments Conoco Phillips - 3T-613 Real-Time QC 213 Company:Well Name:BHST (ºF):Depth:Formation:Analyst:cp @Lot Number--->Pad0.5 ppg 1 ppg 2 ppg3 ppg4 ppgALASKA DISTRICT LABORATORY15 Minute Fann Model 35 Crosslinked Fluid ReportFluid System: Date:6/16/2025ConocoPhillipsProject No:Water pH:7.303T-613Stage(s):1125Water Source:cpf3EE.. BRITTONHydration Visc:2585All chemical concentrations below are in gallons per thousand / pounds per thousand858.961.000.251.00Temp 0FPHLOSURF-300DBC-140X2CLMO-67Optiflo-IIOptiflo-III0.752.002.00010002000300040005000600000:00 02:00 04:00 06:00 08:00 10:00 12:00 14:00Viscosity (cp)Time (min:sec)Zone 1 Crosslink TestsPad0.5 ppg2 ppg3 ppg4 ppg5 ppgFluid is broken at 200cpConoco Phillips - 3T-613Fann 15 Minute Interval 1214 Company:Well Name:BHST (ºF):Depth:Formation:Analyst:cp @Lot Number--->Pad0.5 ppg 1 ppg 2 ppg3 ppg4 ppg3T-613Stage(s):2125Water Source:cpf3ALASKA DISTRICT LABORATORY15 Minute Fann Model 35 Crosslinked Fluid ReportFluid System: Date:6/16/2025ConocoPhillipsProject No:EE.. BRITTONHydration Visc:2288All chemical concentrations below are in gallons per thousand / pounds per thousandWater pH:7.30Temp 0FPHLOSURF-300DBC-140X2CLMO-67Optiflo-IIOptiflo-III889.001.000.251.002.000.752.00050010001500200025003000350040004500500000:00 02:00 04:00 06:00 08:00 10:00 12:00 14:00Viscosity (cp)Time (min:sec)Zone 2 Crosslink TestsPad0.5 ppg2 ppg3 ppg4 ppg5 ppgFluid is broken at 200cpConoco Phillips - 3T-613Fann 15 Minute Interval 2215 Company:Well Name:BHST (ºF):Depth:Formation:Analyst:cp @Lot Number--->Pad0.5 ppg 1 ppg 2 ppg3 ppg4 ppg3T-613Stage(s):3125Water Source:CPF 3ALASKA DISTRICT LABORATORY15 Minute Fann Model 35 Crosslinked Fluid ReportFluid System: Date:6/17/2025ConocoPhillipsProject No:EE.. BRITTONHydration Visc:2790All chemical concentrations below are in gallons per thousand / pounds per thousandWater pH:Hydration pH:Temp 0FPHLOSURF-300DBC-140X2CLMO-67Optiflo-IIOptiflo-III909.201.000.251.002.000.752.0005001000150020002500300035004000450000:00 02:00 04:00 06:00 08:00 10:00 12:00 14:00Viscosity (cp)Time (min:sec)Zone 3 Crosslink TestsPad0.5 ppg2 ppg3 ppg4 ppg5 ppgFluid is broken at 200cpConoco Phillips - 3T-613Fann 15 Minute Interval 3216 Company:Well Name:BHST (ºF):Depth:Formation:Analyst:cp @Lot Number--->Pad.50 ppg 1 ppg 2 ppg3 ppg4 ppg3T-613Stage(s):4125Water Source:CPF3ALASKA DISTRICT LABORATORY15 Minute Fann Model 35 Crosslinked Fluid ReportFluid System: Date:6/17/2025ConocoPhillipsProject No:EE.. BRITTONHydration Visc:27100All chemical concentrations below are in gallons per thousand / pounds per thousandWater pH:Hydration pH:Temp 0FPHLOSURF-300DBC-140X2CLMO-67Optiflo-IIOptiflo-III1009.301.000.251.002.000.752.00050010001500200025003000350040004500500000:00 02:00 04:00 06:00 08:00 10:00 12:00 14:00Viscosity (cp)Time (min:sec)Zone 4 Crosslink Tests.50 ppg1 ppg2 ppg3 ppg4 ppg5 ppgFluid is broken at 200cpConoco Phillips - 3T-613Fann 15 Minute Interval 4217 Company:Well Name:BHST (ºF):Depth:Formation:Analyst:cp @Lot Number--->Pad.50 ppg 1 ppg 2 ppg3 ppg4 ppg3T-613Stage(s):5125Water Source:CPF3ALASKA DISTRICT LABORATORY15 Minute Fann Model 35 Crosslinked Fluid ReportFluid System: Date:6/17/2025ConocoPhillipsProject No:EE.. BRITTONHydration Visc:2795All chemical concentrations below are in gallons per thousand / pounds per thousandWater pH:Hydration pH:Temp 0FPHLOSURF-300DBC-140X2CLMO-67Optiflo-IIOptiflo-III959.301.000.251.002.000.752.00050010001500200025003000350000:00 02:00 04:00 06:00 08:00 10:00 12:00 14:00Viscosity (cp)Time (min:sec)Zone 5 Crosslink TestsPad1 ppg2 ppg3 ppg4 ppg5 ppgFluid is broken at 200cpConoco Phillips - 3T-613Fann 15 Minute Interval 5218 Company:Well Name:BHST (ºF):Depth:Formation:Analyst:cp @Lot Number--->Pad.50 ppg 1 ppg 2 ppg3 ppg4 ppg3T-613Stage(s):6125Water Source:CPF3ALASKA DISTRICT LABORATORY15 Minute Fann Model 35 Crosslinked Fluid ReportFluid System: Date:6/17/2025ConocoPhillipsProject No:EE.. BRITTONHydration Visc:2795All chemical concentrations below are in gallons per thousand / pounds per thousandWater pH:Hydration pH:Temp 0FPHLOSURF-300DBC-140X2CLMO-67Optiflo-IIOptiflo-III959.381.000.251.002.000.752.000500100015002000250030003500400000:00 02:00 04:00 06:00 08:00 10:00 12:00 14:00Viscosity (cp)Time (min:sec)Zone 6 Crosslink TestsPad1 ppg2 ppg3 ppg4 ppg5 ppgFluid is broken at 200cpConoco Phillips - 3T-613Fann 15 Minute Interval 6219 Company:Well Name:BHST (ºF):Depth:Formation:Analyst:cp @Lot Number--->Pad0.5 ppg 1 ppg 2 ppg3 ppg4 ppg3T-613Stage(s):7125Water Source:CPF3ALASKA DISTRICT LABORATORY15 Minute Fann Model 35 Crosslinked Fluid ReportFluid System: Date:6/18/2025ConocoPhillipsProject No:EE.. BRITTONHydration Visc:2987All chemical concentrations below are in gallons per thousand / pounds per thousandWater pH:Hydration pH:Temp 0FPHLOSURF-300DBC-140X2CLMO-67Optiflo-IIOptiflo-III879.401.000.251.002.000.752.000500100015002000250030003500400000:00 02:00 04:00 06:00 08:00 10:00 12:00 14:00Viscosity (cp)Time (min:sec)Zone 7 Crosslink TestsPad1 ppg2 ppg3 ppg4 ppg5 ppgFluid is broken at 200cpConoco Phillips - 3T-613Fann 15 Minute Interval 7220 Company:Well Name:BHST (ºF):Depth:Formation:Analyst:cp @Lot Number--->Pad0.5 ppg 1 ppg 2 ppg3 ppg4 ppg3T-613Stage(s):8125Water Source:CPF3ALASKA DISTRICT LABORATORY15 Minute Fann Model 35 Crosslinked Fluid ReportFluid System: Date:6/19/2025ConocoPhillipsProject No:EE.. BRITTONHydration Visc:2688All chemical concentrations below are in gallons per thousand / pounds per thousandWater pH:Hydration pH:Temp 0FPHLOSURF-300DBC-140X2CLMO-67Optiflo-IIOptiflo-III889.261.000.251.002.000.602.00010002000300040005000600000:00 02:00 04:00 06:00 08:00 10:00 12:00 14:00Viscosity (cp)Time (min:sec)Zone 8 Crosslink TestsPad1 ppg2 ppg3 ppg4 ppg5 ppgFluid is broken at 200cpConoco Phillips - 3T-613Fann 15 Minute Interval 8221 Company:Well Name:BHST (ºF):Depth:Formation:Analyst:cp @Lot Number--->Pad0.5 ppg 1 ppg 2 ppg3 ppg4 ppg3T-613Stage(s):9125Water Source:CPF3ALASKA DISTRICT LABORATORY15 Minute Fann Model 35 Crosslinked Fluid ReportFluid System: Date:6/19/2025ConocoPhillipsProject No:EE.. BRITTONHydration Visc:2690All chemical concentrations below are in gallons per thousand / pounds per thousandWater pH:Hydration pH:Temp 0FPHLOSURF-300DBC-140X2CLMO-67Optiflo-IIOptiflo-III909.401.000.251.002.000.452.00050010001500200025003000350000:00 02:00 04:00 06:00 08:00 10:00 12:00 14:00Viscosity (cp)Time (min:sec)Zone 9 Crosslink TestsPad1 ppg2 ppg3 ppg4 ppg5 ppgFluid is broken at 200cpConoco Phillips - 3T-613Fann 15 Minute Interval 9222 Company:Well Name:BHST (ºF):Depth:Formation:Analyst:cp @Lot Number--->Pad0.5 ppg 1 ppg 2 ppg3 ppg4 ppg3T-613Stage(s):10125Water Source:CPF3ALASKA DISTRICT LABORATORY15 Minute Fann Model 35 Crosslinked Fluid ReportFluid System: Date:6/19/2025ConocoPhillipsProject No:EE.. BRITTONHydration Visc:2598All chemical concentrations below are in gallons per thousand / pounds per thousandWater pH:Hydration pH:Temp 0FPHLOSURF-300DBC-140X2CLMO-67Optiflo-IIOptiflo-III989.401.000.251.002.000.452.000500100015002000250030003500400000:00 02:00 04:00 06:00 08:00 10:00 12:00 14:00Viscosity (cp)Time (min:sec)Zone 10 Crosslink TestsPad1 ppg2 ppg3 ppg4 ppg5 ppgFluid is broken at 200cpConoco Phillips - 3T-613Fann 15 Minute Interval 10223 Company:Well Name:BHST (ºF):Depth:Formation:Analyst:cp @Lot Number--->Pad0.5 ppg 1 ppg 2 ppg3 ppg4 ppg3T-613Stage(s):11125Water Source:CPF3ALASKA DISTRICT LABORATORY15 Minute Fann Model 35 Crosslinked Fluid ReportFluid System: Date:6/19/2025ConocoPhillipsProject No:EE.. BRITTONHydration Visc:2590All chemical concentrations below are in gallons per thousand / pounds per thousandWater pH:Hydration pH:Temp 0FPHLOSURF-300DBC-140X2CLMO-67Optiflo-IIOptiflo-III909.301.000.251.002.000.452.000500100015002000250030003500400000:00 02:00 04:00 06:00 08:00 10:00 12:00 14:00Viscosity (cp)Time (min:sec)Zone 11 Crosslink TestsPad1 ppg2 ppg3 ppg4 ppg5 ppgFluid is broken at 200cpConoco Phillips - 3T-613Fann 15 Minute Interval 11224 Company:Well Name:BHST (ºF):Depth:Formation:Analyst:cp @Lot Number--->Pad0.5 ppg 1 ppg 2 ppg3 ppg4 ppg3T-613Stage(s):12125Water Source:CPF3ALASKA DISTRICT LABORATORY15 Minute Fann Model 35 Crosslinked Fluid ReportFluid System: Date:6/19/2025ConocoPhillipsProject No:EE.. BRITTONHydration Visc:2693All chemical concentrations below are in gallons per thousand / pounds per thousandWater pH:Hydration pH:Temp 0FPHLOSURF-300DBC-140X2CLMO-67Optiflo-IIOptiflo-III939.301.000.251.002.000.452.00050010001500200025003000350040004500500000:00 02:00 04:00 06:00 08:00 10:00 12:00 14:00Viscosity (cp)Time (min:sec)Zone 12 Crosslink TestsPad1 ppg2 ppg3 ppg4 ppg5 ppgFluid is broken at 200cpConoco Phillips - 3T-613Fann 15 Minute Interval 12225 Company:Well Name:BHST (ºF):Depth:Formation:Analyst:cp @Lot Number--->Pad0.5 ppg 1 ppg 2 ppg3 ppg4 ppg3T-613Stage(s):13125Water Source:CPF3ALASKA DISTRICT LABORATORY15 Minute Fann Model 35 Crosslinked Fluid ReportFluid System: Date:6/19/2025ConocoPhillipsProject No:EE.. BRITTONHydration Visc:2592All chemical concentrations below are in gallons per thousand / pounds per thousandWater pH:Hydration pH:Temp 0FPHLOSURF-300DBC-140X2CLMO-67Optiflo-IIOptiflo-III929.201.000.251.002.000.452.000500100015002000250030003500400000:00 02:00 04:00 06:00 08:00 10:00 12:00 14:00Viscosity (cp)Time (min:sec)Zone 13 Crosslink TestsPad1 ppg2 ppg3 ppg4 ppg5 ppgFluid is broken at 200cpConoco Phillips - 3T-613Fann 15 Minute Interval 13226 Company:Well Name:BHST (ºF):Depth:Formation:Analyst:cp @Lot Number--->Pad0.5 ppg 1 ppg 2 ppg3 ppg4 ppg3T-613Stage(s):14125Water Source:CPF3ALASKA DISTRICT LABORATORY15 Minute Fann Model 35 Crosslinked Fluid ReportFluid System: Date:6/20/2025ConocoPhillipsProject No:EE.. BRITTONHydration Visc:2495All chemical concentrations below are in gallons per thousand / pounds per thousandWater pH:Hydration pH:Temp 0FPHLOSURF-300DBC-140X2CLMO-67Optiflo-IIOptiflo-III959.451.000.251.002.000.602.0005001000150020002500300035004000450000:00 02:00 04:00 06:00 08:00 10:00 12:00 14:00Viscosity (cp)Time (min:sec)Zone 14 Crosslink TestsPad1 ppg2 ppg3 ppg4 ppg5 ppgFluid is broken at 200cpConoco Phillips - 3T-613Fann 15 Minute Interval 14227 Company:Well Name:BHST (ºF):Depth:Formation:Analyst:cp @Lot Number--->Pad0.5 ppg 1 ppg 2 ppg3 ppg4 ppg3T-613Stage(s):15125Water Source:CPF3ALASKA DISTRICT LABORATORY15 Minute Fann Model 35 Crosslinked Fluid ReportFluid System: Date:6/20/2025ConocoPhillipsProject No:EE.. BRITTONHydration Visc:2597All chemical concentrations below are in gallons per thousand / pounds per thousandWater pH:Hydration pH:Temp 0FPHLOSURF-300DBC-140X2CLMO-67Optiflo-IIOptiflo-III979.401.000.251.002.000.352.0005001000150020002500300035004000450000:00 02:00 04:00 06:00 08:00 10:00 12:00 14:00Viscosity (cp)Time (min:sec)Zone 15 Crosslink TestsPad1 ppg2 ppg3 ppg4 ppg5 ppgFluid is broken at 200cpConoco Phillips - 3T-613Fann 15 Minute Interval 15228 Company:Well Name:BHST (ºF):Depth:Formation:Analyst:cp @Lot Number--->Pad0.5 ppg 1 ppg 2 ppg3 ppg4 ppg3T-613Stage(s):16125Water Source:CPF3ALASKA DISTRICT LABORATORY15 Minute Fann Model 35 Crosslinked Fluid ReportFluid System: Date:6/20/2025ConocoPhillipsProject No:EE.. BRITTONHydration Visc:2592All chemical concentrations below are in gallons per thousand / pounds per thousandWater pH:Hydration pH:Temp 0FPHLOSURF-300DBC-140X2CLMO-67Optiflo-IIOptiflo-III929.301.000.251.002.000.352.00050010001500200025003000350040004500500000:00 02:00 04:00 06:00 08:00 10:00 12:00 14:00Viscosity (cp)Time (min:sec)Zone 16 Crosslink TestsPad1 ppg2 ppg3 ppg4 ppg5 ppgFluid is broken at 200cpConoco Phillips - 3T-613Fann 15 Minute Interval 16229 Company:Well Name:BHST (ºF):Depth:Formation:Analyst:cp @Lot Number--->Pad0.5 ppg 1 ppg 2 ppg3 ppg4 ppg3T-613Stage(s):17125Water Source:CPF3ALASKA DISTRICT LABORATORY15 Minute Fann Model 35 Crosslinked Fluid ReportFluid System: Date:6/20/2025ConocoPhillipsProject No:EE.. BRITTONHydration Visc:25100All chemical concentrations below are in gallons per thousand / pounds per thousandWater pH:Hydration pH:Temp 0FPHLOSURF-300DBC-140X2CLMO-67Optiflo-IIOptiflo-III1009.301.000.251.002.000.352.0005001000150020002500300035004000450000:00 02:00 04:00 06:00 08:00 10:00 12:00 14:00Viscosity (cp)Time (min:sec)Zone 17 Crosslink TestsPad1 ppg2 ppg3 ppg4 ppg5 ppgFluid is broken at 200cpConoco Phillips - 3T-613Fann 15 Minute Interval 17230 Company:Well Name:BHST (ºF):Depth:Formation:Analyst:cp @Lot Number--->Pad0.5 ppg 1 ppg 2 ppg3 ppg4 ppg3T-613Stage(s):18125Water Source:CPF3ALASKA DISTRICT LABORATORY15 Minute Fann Model 35 Crosslinked Fluid ReportFluid System: Date:6/20/2025ConocoPhillipsProject No:EE.. BRITTONHydration Visc:24100All chemical concentrations below are in gallons per thousand / pounds per thousandWater pH:Hydration pH:Temp 0FPHLOSURF-300DBC-140X2CLMO-67Optiflo-IIOptiflo-III1009.201.000.251.002.000.352.0005001000150020002500300035004000450000:00 02:00 04:00 06:00 08:00 10:00 12:00 14:00Viscosity (cp)Time (min:sec)Zone 18 Crosslink TestsPad1 ppg2 ppg3 ppg4 ppg5 ppgFluid is broken at 200cpConoco Phillips - 3T-613Fann 15 Minute Interval 18231 Company:Well Name:BHST (ºF):Depth:Formation:Analyst:cp @Lot Number--->Pad0.5 ppg 1 ppg 2 ppg3 ppg4 ppg3T-613Stage(s):19125Water Source:CPF3ALASKA DISTRICT LABORATORY15 Minute Fann Model 35 Crosslinked Fluid ReportFluid System: Date:6/20/2025ConocoPhillipsProject No:EE.. BRITTONHydration Visc:2597All chemical concentrations below are in gallons per thousand / pounds per thousandWater pH:Hydration pH:Temp 0FPHLOSURF-300DBC-140X2CLMO-67Optiflo-IIOptiflo-III979.301.000.251.002.000.352.000500100015002000250030003500400000:00 02:00 04:00 06:00 08:00 10:00 12:00 14:00Viscosity (cp)Time (min:sec)Zone 19 Crosslink TestsPad1 ppg2 ppg3 ppg4 ppg5 ppgFluid is broken at 200cpConoco Phillips - 3T-613Fann 15 Minute Interval 19232 Company:Well Name:BHST (ºF):Depth:Formation:Analyst:cp @Lot Number--->Pad0.5 ppg 1 ppg 2 ppg3 ppg4 ppg3T-613Stage(s):20125Water Source:CPF3ALASKA DISTRICT LABORATORY15 Minute Fann Model 35 Crosslinked Fluid ReportFluid System: Date:6/21/2025ConocoPhillipsProject No:EE.. BRITTONHydration Visc:2697All chemical concentrations below are in gallons per thousand / pounds per thousandWater pH:Hydration pH:Temp 0FPHLOSURF-300DBC-140X2CLMO-67Optiflo-IIOptiflo-III979.201.000.251.002.000.352.0005001000150020002500300035004000450000:00 02:00 04:00 06:00 08:00 10:00 12:00 14:00Viscosity (cp)Time (min:sec)Zone 20 Crosslink TestsPad1 ppg2 ppg3 ppg4 ppg5 ppgFluid is broken at 200cpConoco Phillips - 3T-613Fann 15 Minute Interval 20233 Company:Well Name:BHST (ºF):Depth:Formation:Analyst:cp @Lot Number--->Pad0.5 ppg 1 ppg 2 ppg3 ppg4 ppg3T-613Stage(s):21125Water Source:CPF3ALASKA DISTRICT LABORATORY15 Minute Fann Model 35 Crosslinked Fluid ReportFluid System: Date:6/21/2025ConocoPhillipsProject No:EE.. BRITTONHydration Visc:2595All chemical concentrations below are in gallons per thousand / pounds per thousandWater pH:Hydration pH:Temp 0FPHLOSURF-300DBC-140X2CLMO-67Optiflo-IIOptiflo-III959.301.000.251.002.000.302.0005001000150020002500300035004000450000:00 02:00 04:00 06:00 08:00 10:00 12:00 14:00Viscosity (cp)Time (min:sec)Zone 21 Crosslink TestsPad1 ppg2 ppg3 ppg4 ppg5 ppgFluid is broken at 200cpConoco Phillips - 3T-613Fann 15 Minute Interval 21234 Company: Well: Sand Type Date Tested Total Sample Size Seive Weight Seive Weight 100.0 g Sieve Size Before Sand With sand WT. rtn'd % rtn'd % API Spec 12 355.0 355 0 0.0% 0.00% <0.1% 16 340.1 345 4.9 4.9% 18 303.3 392.7 89.4 89.4% 20 296.5 300 3.5 3.5% 25 419.4 421.1 1.7 1.7% 30 281.5 281.9 0.4 0.4% 40 407.6 411 3.4 3.4% Pan 306.6 306.6 0 0.0% 0.00% <1.0% Total: 103.3 103% 95.00%>/= 90% Sample:16 / 20 - 6/16/2025 Conoco Phillips 3T-613 16/20 Proppant 6/16/2025 Ceramic Proppant Sieves Conoco Phillips - 3T-613 Sand Sieve Analysis 235 Seq No. Time Activity Code Comment Job Slurry Vol Treating Pressure Treating Pressure @Pump Slurry Rate Tubing Gauge BH Pres1 06:26:00 (06/16/25) Start Job Starting Job 0 11 12 0 01 06:26:00 (06/16/25) Next Treatment Treatment Interval 1 0 11 12 0 02 7:35:55 Prime Pumps Prime Pumps 0 0 -5 0 21033 7:52:19 Pressure Test ePRV - Primary Tubing 0 931 975 0 21044 7:54:37 Pressure Test ePRV - Primary IA 0 2051 2091 0 21045 8:08:37 Pressure Test ePRV - Secondary Tubing 0 1501 1054 0 21056 8:10:01 Pressure Test ePRV - Secondary IA 0 1320 746 0 21057 8:14:57 Pressure Test Testing Globals 0 414 179 0 21058 8:15:04 Pressure Test Testing Locals 0 416 151 0 21059 8:18:04 Pressure Test Pressure Test - Max 0 9444 9478 0 210510 8:23:51 Pressure Test Pressure Test - Pass 0 9137 9126 0 210511 9:40:26 Start Pumping Start Pumping 0 992 1015 0 240912 9:40:49 Open Well Open Well 0 537 477 0 248013 9:45:17 Other Pump 582 32.98 2613 2617 10.7 426414 9:50:32 ISIP ISIP 85.69 1181 1122 0 323515 10:32:53 Open Well Open Well 85.69 667 622 0 270716 10:35:02 Other Step Rate Test - 1 bpm 86.51 1382 1428 0.9 351917 10:37:38 Other Step Rate Test - 2 bpm 90.75 1599 1610 2.2 367418 10:39:39 Other Step Rate Test - 3 bpm 96.1 1710 1721 2.9 375219 10:41:24 Other Step Rate Test - 4 bpm 102.28 1830 1838 3.9 382820 10:43:31 Other Step Rate Test - 5 bpm 111.72 1957 1967 4.9 392921 10:45:28 Other Step Rate Test - 6 bpm 122.04 2074 2094 5.9 404522 10:47:19 Other Step Rate Test - 7 bpm 134.1 2353 2346 7.1 422123 10:49:11 Other Step Rate Test - 8 bpm 148.56 2444 2432 8.1 426724 10:50:15 Other Step Rate Test - 9 bpm 157.9 2636 2663 8.9 446025 10:52:25 Other Step Rate Test - 10 bpm 178.12 2740 2720 10 448426 10:54:11 Other Step Rate Test - 11 bpm 196.78 2741 2735 11 451027 10:56:05 Other Step Rate Test - 12 bpm 218.63 2755 2749 11.9 451728 10:57:54 Other Step Rate Test - 13 bpm 241.15 2870 2891 12.8 463529 10:59:54 Other Step Rate Test - 14 bpm 267.59 2900 2893 13.8 460030 11:01:53 Other Step Rate Test - 15 bpm 295.7 2874 2882 14.9 456731 11:06:45 Alarm Delta Stage At Top Perf = 4 368.83 2700 2702 15 441132 11:07:48 Alarm Delta Stage At Top Perf = 5 389.52 3717 3713 24.9 502833 11:09:49 Alarm Delta Stage At Top Perf = 7 455.48 4456 4453 36 539934 11:15:53 Alarm Delta Stage At Top Perf = 8 681.06 4852 4854 37.3 530535 11:17:12 Alarm Delta Stage At Top Perf = 9 730.27 5010 5024 37.3 545636 11:21:24 Other Pump 670 - Shut off 886.2 5193 5174 37.3 559037 11:25:39 Other Pump 670 - Shut off 1034.81 5241 5227 37.3 565738 11:28:07 Alarm Delta Stage At Top Perf = 10 1113.7 5187 5229 36.3 564139 11:29:46 Other Pump 177 - Preload 1174.21 5160 5141 37.1 565040 11:36:06 Alarm Delta Stage At Top Perf = 11 1403.02 4943 4947 37.1 551041 11:42:56 Alarm Delta Stage At Top Perf = 12 1656.36 4966 4972 37.1 552942 11:52:34 Alarm Delta Stage At Top Perf = 13 2008.2 5101 5075 37 570743 11:52:47 Other Pump 670 - Shut off 2016.22 5095 5079 37 571544 11:59:41 Other Bin 2 Gate Not Opening 2264.84 5188 5174 36.8 574845 12:02:41 Alarm Delta Stage At Top Perf = 14 2375.4 5249 5236 36.8 587546 12:08:40 Other Shut Gate on mover 2595.3 5385 5394 36.7588547 12:09:11 Alarm Delta Stage At Top Perf = 15 2614.26 5401 5418 36.7589948 12:10:51 Other Cut Xlink for Spacer 2676.03 5544 5537 37.2598649 12:12:13 Ball on Seat Launch Dart 2726.8 5708 5678 37.261042 12:12:21 (06/16/25) Next Treatment Treatment Interval 2 2731.14 5688 5663 37.2609650 12:14:10 Alarm Delta Stage At Top Perf = 16 2799.32 5538 5546 37.2616351 12:20:13 Other Slow for Dart 3025.49 4643 4669 37.6510952 12:20:33 Alarm Delta Stage At Top Perf = 17 3035.48 2848 2832 22.9 440153 12:21:45 Ball on Seat Dart on Seat 3054.43 3147 3164 15.2 426354 12:22:00 Break Formation Break Formation 3058.21 6471 6468 15.1 745855 12:22:01 Other Pump Kickout 3058.46 6194 6248 15 733056 12:24:42 Alarm Delta Stage At Top Perf = 1 3091.52 5038 5066 27.5 545757 12:26:09 Alarm Delta Stage At Top Perf = 2 3142.19 5047 5052 37.4 556458 12:31:46 Alarm Delta Stage At Top Perf = 3 3352.97 5075 5091 37.6 550159 12:32:07 Other Pump 670 - Shut Off 3365.55 5153 5148 37.9 552760 12:36:44 Other Pump 621 - Radiator Cap 3531.16 5214 5242 37.8 559161 12:39:28 Other Pump 621 3614.81 4502 4539 29.7 501862 12:40:02 Other Pump 621 - Lock Up 3632.88 4790 4787 32.8 521363 12:43:16 Alarm Delta Stage At Top Perf = 4 3731.23 4644 4651 31.9 515364 12:46:41 Other Pump 584 - Shut Off 3841.23 4527 4538 32.2 524965 12:51:41 Other Cut Sand 3961 4060 4108 23.4 499366 12:53:11 Other Stage to Flush 3996.23 4090 4077 23.4 495467 12:54:25 Alarm Delta Stage At Top Perf = 5 4025.08 4009 4064 23.3 494068 13:08:36 Alarm Delta Stage At Top Perf = 6 4357.16 2265 2468 23.4 441969 13:08:54 ISIP ISIP 4358.91 1426 1486 0 368970 16:38:48 Pressure Test Pressure Test - Max 4358.91 9493 9510 0 318471 16:44:34 Pressure Test Pressure Test - Pass 4358.91 9194 9194 0 317572 16:52:16 Open Well Open Well 4358.91 1059 1112 0 337273 0.705798611 Start Pad Good XLink (Start Pad) 4388.79 2730 2722 15.1 429374 17:06:22 Alarm Delta Stage At Top Perf = 7 4718.88 5124 5102 37.5 538875 17:07:21 Alarm Delta Stage At Top Perf = 8 4755.77 5026 5048 37.5 532076 17:17:15 Alarm Delta Stage At Top Perf = 9 5126.97 5323 5317 37.5 567077 17:25:00 Alarm Delta Stage At Top Perf = 10 5417.71 5024 5000 37.5 550878 17:31:45 Alarm Delta Stage At Top Perf = 11 5670.64 4992 4982 37.4 552079 17:40:37 Alarm Delta Stage At Top Perf = 12 6001.18 5023 5004 37.2 562280 17:50:57 Alarm Delta Stage At Top Perf = 13 6385.14 5296 5271 37 578681 17:55:50 Alarm Delta Stage At Top Perf = 14 6565.91 5400 5401 37 589382 17:59:52 Alarm Delta Stage At Top Perf = 15 6716.37 5608 5593 37.5 601883 18:03:19 Alarm Delta Stage At Top Perf = 16 6845.81 5236 5257 37.5 592884 18:08:08 Alarm Delta Stage At Top Perf = 17 7027 4341 4346 37.6 503185 18:08:26 ISIP ISIP 7032.22 1637 73 0 372586 18:13:06 Shut-In Pressure @ 5 Minutes Shut-In Pressure @ 5 Minutes 7032.22 307 287 0 355387 18:18:08 Shut-In Pressure @ 10 Minutes Shut-In Pressure @ 10 Minutes 7032.22 70 44 0 353388 18:23:07 Shut-In Pressure @ 15 Minutes Shut-In Pressure @ 15 Minutes 7032.22 14 4 0 3519Event Log 6.16.25Conoco Phillips - 3T-613 Event Log 6.16.25236 Seq No. Time Activity Code Comment Job Slurry Vol Treating Pressure Treating Pressure @Pump Slurry Rate Tubing Gauge BH Pres1 06:30:18 (06/17/25) Start Job Starting Job 0 0 0 0 01 06:30:18 (06/17/25) Next Treatment Treatment Interval 1 0 0 0 0 02 7:28:08 Prime Pumps Prime Pumps 0 -8 -5 0 28103 7:50:02 Other Maintenace on Pump 177 0 14 -9 0 27993 07:50:58 (06/17/25) Next Treatment Treatment Interval 3 0 14 -9 0 27994 8:54:41 Prime Pumps Prime Pumps 0 -7 4 0 27715 9:12:55 Pressure Test ePRV - Primary Tubing 0 854 980 0 27646 9:14:45 Pressure Test ePRV - Primary IA 0 551 715 0 27637 9:16:18 Pressure Test ePRV - Secondary Tubing 0 606 782 0 27628 9:17:48 Pressure Test ePRV - Secondary IA 0 776 956 0 27629 9:19:59 Other Testing Globals 0 1112 1256 0 276110 9:20:06 Other Testing Locals 0 1116 1254 0 276111 9:23:06 Pressure Test Pressure Test - Max 0 9532 9703 0 275912 9:29:52 Pressure Test Pressure Test - Pass 0 9293 9426 0 275713 9:44:31 Start Pumping Start Pumping 0 -27 102 0 276714 9:45:58 Open Well Open Well 0 693 788 0 276615 9:48:52 Drop Ball Launch Dart 27.62 2677 2802 14.7 423716 9:59:55 Alarm Delta Stage At Top Perf = 4 352.93 2883 3029 15 404417 10:00:24 Ball on Seat Dart on Seat 360.22 2924 3071 15.2 404818 10:01:21 Break Formation Break Formation 374.63 4173 4314 15.1 530619 10:02:21 Alarm Delta Stage At Top Perf = 5 389.79 4257 4406 16.4 527820 10:05:02 Alarm Delta Stage At Top Perf = 6 438.93 4889 5027 18.3 579521 10:07:02 Other OSR - Drop Rate 475.45 6033 6179 18.2 685422 10:08:45 Other OSR - Extend Pad Due to Pressure 503.85 5514 5652 16.3 620923 10:09:39 Alarm Delta Stage At Top Perf = 7 518.53 5571 5717 16.3 629824 10:43:40 Alarm Delta Stage At Top Perf = 8 1070.06 5069 5182 16.2 588625 11:07:42 Alarm Delta Stage At Top Perf = 9 1796.12 5310 5446 36.7 599826 11:14:33 Alarm Delta Stage At Top Perf = 10 2048.06 5058 5204 36.7 573027 11:23:32 Alarm Delta Stage At Top Perf = 11 2377.34 5186 5296 36.5 588128 11:29:50 Other Load Dart 2607.38 5270 5356 36.5 591629 11:32:19 Alarm Delta Stage At Top Perf = 12 2697.91 5302 5457 36.4 601530 11:38:54 Alarm Delta Stage At Top Perf = 13 2937.7 5490 5661 36.4 614131 11:39:16 Other Shut Gate on Mover 2950.42 5551 5715 36.4 615432 11:42:03 Drop Ball Launch Dart 3052.45 5798 5921 36.8 62714 11:42:06 (06/17/25) Next Treatment Treatment Interval 4 3054.9 5793 5914 36.8 627133 11:44:10 Alarm Delta Stage At Top Perf = 14 3131.04 5603 5753 36.8 636934 11:49:27 Other Slow for Dart 3326.45 4718 4864 37.1 526635 11:50:26 Alarm Delta Stage At Top Perf = 15 3347.59 2928 3088 14.9 429836 11:51:42 Ball on Seat Dart on Seat 3366.09 3158 3311 14.7 433637 11:51:55 Break Formation Break Formation 3369.52 6484 6593 14.7 757238 11:53:42 Alarm Delta Stage At Top Perf = 1 3399.95 3723 3876 22.4 459539 11:55:21 Alarm Delta Stage At Top Perf = 2 3450.34 4597 4728 36.8 515740 11:57:27 Alarm Delta Stage At Top Perf = 3 3528.45 4577 4713 37.3 521441 12:04:21 Alarm Delta Stage At Top Perf = 4 3784.98 4907 5019 37.1 535642 12:12:12 Alarm Delta Stage At Top Perf = 5 4075.88 5009 5135 37 541443 12:17:03 Alarm Delta Stage At Top Perf = 6 4254.93 5201 5326 36.8 555144 12:22:12 Alarm Delta Stage At Top Perf = 7 4444.07 5426 5559 36.7582345 12:27:16 Alarm Delta Stage At Top Perf = 8 4629.59 5589 5726 36.6600746 12:30:47 Other Load Dart 4757.5 5721 5853 36.5606247 12:33:12 Alarm Delta Stage At Top Perf = 9 4846.34 5894 6030 36.4615648 12:36:50 Other Shut Gate on Mover 4977.98 6131 6284 36.4630049 12:38:39 Alarm Delta Stage At Top Perf = 10 5045.05 6276 6430 36.9633950 12:40:16 Drop Ball Launch Dart 5104.7 6388 6517 36.964195 12:40:39 (06/17/25) Next Treatment Treatment Interval 5 5118.85 6471 6550 36.9 655151 12:43:20 Alarm Delta Stage At Top Perf = 11 5218.12 5558 5682 37.2 636752 12:47:35 Other Slow for Dart 5375.52 4451 4610 37.3 494653 12:48:23 Alarm Delta Stage At Top Perf = 12 5392.87 2585 2753 15.2 399654 12:49:29 Ball on Seat Dart on Seat 5409.31 2829 2994 15.1 403555 12:49:42 Break Formation Break Formation 5412.59 5889 5951 15.1 672356 12:51:55 Alarm Delta Stage At Top Perf = 1 5456.28 4520 4682 28.2 519857 12:53:30 Alarm Delta Stage At Top Perf = 2 5510.1 5119 5249 37 560758 12:55:53 Alarm Delta Stage At Top Perf = 3 5598.68 5147 5265 37.2 553659 13:00:06 Alarm Delta Stage At Top Perf = 4 5755.38 5059 5181 37.1 542360 13:07:58 Alarm Delta Stage At Top Perf = 5 6045.6 5056 5182 36.8 543761 13:09:09 Alarm Delta Stage At Top Perf = 6 6089.06 5152 5334 36.7 550662 13:10:41 Alarm Delta Stage At Top Perf = 7 6145.36 5459 5617 36.7 572163 13:13:12 Alarm Delta Stage At Top Perf = 8 6237.54 5853 5991 36.6 603964 13:16:22 Alarm Delta Stage At Top Perf = 9 6353.25 6117 6282 36.5 624665 13:19:46 Alarm Delta Stage At Top Perf = 10 6477.27 6377 6482 36.5 637966 13:23:29 Alarm Delta Stage At Top Perf = 11 6612.63 6549 6722 36.4 648567 13:26:21 Other Shut Gate on Mover 6716.23 6752 6889 36.3 655968 13:27:20 Alarm Delta Stage At Top Perf = 12 6752.58 6853 6979 36.5 659369 13:28:20 Other Pump Kickout 6788.64 6976 7109 36.8 659570 13:29:35 Drop Ball Launch Dart 6829.71 6333 6485 34 62826 13:29:40 (06/17/25) Next Treatment Treatment Interval 6 6831.98 6352 6489 34.1 630071 13:31:28 Alarm Delta Stage At Top Perf = 13 6894.86 6438 6607 36.4 677372 13:34:21 Alarm Delta Stage At Top Perf = 14 7001.52 5417 5560 37.2 623373 13:37:42 Alarm Delta Stage At Top Perf = 15 7111.61 2378 2547 15.3 388974 13:38:49 Ball on Seat Dart on Seat 7128.42 2652 2806 15.1 395475 13:39:05 Break Formation Break Formation 7132.44 6223 6453 15 711576 13:40:41 Alarm Delta Stage At Top Perf = 1 7162 3865 4018 25.6 465677 13:42:15 Alarm Delta Stage At Top Perf = 2 7213.13 4608 4721 37.2 517078 13:45:19 Alarm Delta Stage At Top Perf = 3 7327.54 4832 4954 37.3 522779 13:49:26 Alarm Delta Stage At Top Perf = 4 7481 4940 5102 37.2 522880 13:57:14 Alarm Delta Stage At Top Perf = 5 7769.9 4901 5055 36.9 536581 13:58:21 Alarm Delta Stage At Top Perf = 6 7811.07 4918 5068 36.8 536982 13:59:54 Alarm Delta Stage At Top Perf = 7 7868.16 5005 5126 36.8 541083 14:02:25 Alarm Delta Stage At Top Perf = 8 7960.76 5128 5298 36.8 553584 14:05:36 Alarm Delta Stage At Top Perf = 9 8077.65 5373 5494 36.7 567885 14:08:56 Alarm Delta Stage At Top Perf = 10 8199.82 5550 5674 36.6 581286 14:12:38 Alarm Delta Stage At Top Perf = 11 8335.27 5677 5838 36.6 590787 14:15:59 Other Shut Gate on Mover 8457.59 5861 5994 36.5 597088 14:16:28 Alarm Delta Stage At Top Perf = 12 8475.22 5887 6003 36.5 598189 14:20:34 Alarm Delta Stage At Top Perf = 13 8626.81 5797 5960 37.1 615490 14:23:24 Alarm Delta Stage At Top Perf = 14 8732.05 4902 5066 37.2 587191 14:26:56 Alarm Delta Stage At Top Perf = 15 8863.97 3714 3854 37.4 461292 14:27:09 ISIP ISIP 8867.13 1131 1172 0 336793 14:32:08 Shut-In Pressure @ 5 Minutes Shut-In Pressure @ 5 Minutes 8867.13 483 682 0 342094 14:37:03 Shut-In Pressure @ 10 Minutes Shut-In Pressure @ 10 Minutes 8867.13 -168 -23 0 340395 14:42:04 Shut-In Pressure @ 15 Minutes Shut-In Pressure @ 15 Minutes 8867.13 265 394 0 3390Event Log 6.17.25Conoco Phillips - 3T-613 Event Log 6.17.25237 Seq No. Time Activity Code Comment Job Slurry Vol Treating Pressure Treating Pressure @Pump Slurry Rate Tubing Gauge BH Pres1 14:59:58 (06/18/25) Start Job Starting Job 0 0 0 0 01 14:59:58 (06/18/25) Next Treatment Treatment Interval 1 0 0 0 0 02 15:43:59 Prime Pumps Prime Pumps 0 -6 22 0 26153 15:57:43 Pressure Test ePRV - Primary Tubing 0 1311 1408 0 26154 16:00:47 Pressure Test ePRV - Primary IA 0 1144 1217 0 26145 16:02:04 Pressure Test ePRV - Secondary Tubing 0 2010 2092 0 26146 16:03:14 Pressure Test ePRV - Secondary IA 0 899 988 0 26147 16:27:53 Other Testing Globals 0 968 1024 0 26148 16:28:00 Other Testing Locals 0 1001 1053 0 26149 16:29:35 Pressure Test Pressure Test - Max 0 9556 9604 0 261410 16:34:55 Pressure Test Pressure Test - Pass 0 9511 9513 0 26137 17:04:00 (06/18/25) Next Treatment Treatment Interval 7 0 91 89 0 295411 17:05:36 Open Well Open Well 0 1016 955 0 288212 17:07:28 Other Load Dart 10.75 2862 2885 13.8 425913 17:08:18 Drop Ball Launch Dart 22.4 2854 2867 14.4 424914 17:16:27 Other Slow for Dart 275.43 5025 5061 36.9 536915 17:18:54 Ball on Seat Dart on Seat 318.76 2740 2754 15.1 388316 17:19:06 Break Formation Break Formation 322.03 5825 5771 15.1 643717 17:19:08 Alarm Delta Stage At Top Perf = 3 322.53 5528 5550 15.1 627118 17:19:14 Alarm Delta Stage At Top Perf = 4 324.04 4808 4728 15 578319 17:21:15 Alarm Delta Stage At Top Perf = 5 354.85 4156 4150 17.4 500420 17:23:25 Alarm Delta Stage At Top Perf = 6 404.75 5156 5161 28.2 574621 17:25:14 Alarm Delta Stage At Top Perf = 7 461.79 5620 5615 34.4 598322 17:29:22 Alarm Delta Stage At Top Perf = 8 615.08 5418 5429 37.3 562623 17:37:09 Alarm Delta Stage At Top Perf = 9 904.35 5529 5543 37 557824 17:38:17 Alarm Delta Stage At Top Perf = 10 946.23 5762 5751 37 571425 17:39:47 Alarm Delta Stage At Top Perf = 11 1001.61 5993 5974 36.9 590426 17:42:17 Alarm Delta Stage At Top Perf = 12 1093.79 6294 6272 36.8 611427 17:42:55 Other Pump 621 1117.12 6353 6342 36.9 615428 17:45:43 Alarm Delta Stage At Top Perf = 13 1215.43 6340 6320 36.2 619229 17:47:05 Other Pump 670 - Shut Off 1264.19 6381 6377 36.1 623130 17:49:27 Alarm Delta Stage At Top Perf = 14 1337.33 5629 5587 31.8 569631 17:53:27 Alarm Delta Stage At Top Perf = 15 1472.74 6210 6213 34.2 611432 17:54:00 Other Load Dart 1491.55 6267 6259 34.3 616533 17:57:11 Other Shut Gate on Mover 1600.99 6355 6339 34.4 618134 17:57:31 Alarm Delta Stage At Top Perf = 16 1612.45 6330 6317 34.4 617935 18:00:17 Drop Ball Launch Dart 1708.71 6386 6391 34.9 61788 18:00:20 (06/18/25) Next Treatment Treatment Interval 8 1709.88 6382 6379 34.9 617836 18:01:36 Alarm Delta Stage At Top Perf = 17 1754.76 6034 6032 35 615437 18:04:38 Alarm Delta Stage At Top Perf = 18 1861.48 5096 5065 35.3 582238 18:08:13 Alarm Delta Stage At Top Perf = 19 1975.63 2598 2615 15.3 385139 18:09:14 Ball on Seat Dart on Seat 1990.93 2869 2867 15.2 391640 18:09:26 Break Formation Break Formation 1994 6191 6123 15.1 713641 18:11:22 Alarm Delta Stage At Top Perf = 1 2024.6 3975 3970 20.4 475142 18:13:08 Alarm Delta Stage At Top Perf = 2 2075.22 5237 5205 36.4 547743 18:15:02 Alarm Delta Stage At Top Perf = 3 2147.12 5255 5246 38 554944 18:22:02 Alarm Delta Stage At Top Perf = 4 2412.62 4489 4491 38510845 18:25:58 Alarm Delta Stage At Top Perf = 5 2562.43 3535 3519 38.1443246 18:26:10 ISIP ISIP 2564.81 968 42 0320747 18:31:09 Shut-In Pressure @ 5 Minutes Shut-In Pressure @ 5 Minutes 2564.81 412 449 0334348 18:36:04 Shut-In Pressure @ 10 Minutes Shut-In Pressure @ 10 Minutes 2564.81 3 -5 0333649 18:41:05 Shut-In Pressure @ 15 Minutes Shut-In Pressure @ 15 Minutes 2564.81 -8 -2 03324Event Log 6.18.25Conoco Phillips - 3T-613 Event Log 6.18.25238 Seq No. Time Activity Code Comment Job Slurry Vol Treating Pressure Treating Pressure @Pump Slurry Rate Tubing Gauge BH Pres 1 07:30:28 (06/19/25) Start Job Starting Job 0 0 0 0 0 1 07:30:28 (06/19/25) Next Treatment Treatment Interval 1 0 0 0 0 0 2 8:26:22 Prime Pumps Prime Pumps 0 -71 -61 0 0 3 8:43:50 Pressure Test ePRV - Primary Tubing 0 1636 1655 0 0 4 8:45:39 Pressure Test ePRV - Primary IA 0 1085 902 0 0 5 8:47:25 Pressure Test ePRV - Secondary Tubing 0 1135 1187 0 0 6 8:48:43 Pressure Test ePRV - Secondary IA 0 1064 1108 0 0 7 8:50:35 Other Testing Globals 0 1101 1155 0 0 8 8:50:40 Other Testing Locals 0 1124 1180 0 0 9 8:52:53 Pressure Test Pressure Test - Max 0 9521 9556 0 0 10 8:58:17 Pressure Test Pressure Test - Pass 0 9511 9528 0 0 11 9:38:43 Alarm Delta I1 Pressure 8 = -117 psi 0 -62 -54 0 3099 12 9:39:00 Alarm Delta I1 Pressure 8 = -210 psi 0 -62 -54 0 3098 13 9:39:29 Alarm Delta I1 Pressure 8 = -108 psi 0 -62 -54 0 3096 14 9:39:39 Alarm Delta I1 Pressure 8 = -16 psi 0 -62 -54 0 3096 15 9:40:15 Alarm Delta I1 Pressure 8 = 78 psi 0 -62 -54 0 3094 16 9:40:35 Alarm Delta I1 Pressure 8 = 170 psi 0 -62 -54 0 3092 8 09:56:19 (06/19/25) Next Treatment Treatment Interval 8 0 -65 -54 0 3057 17 9:58:33 Start Pumping Start Pumping 0 -64 -54 0 3050 18 10:02:55 Open Well Open Well 0 956 943 0 3049 19 10:14:19 Alarm Delta Stage At Top Perf = 4 315.08 4763 4790 37.8 5067 20 10:15:35 Alarm Delta Stage At Top Perf = 5 363.02 4841 4857 37.8 5122 21 10:21:01 Alarm Delta Stage At Top Perf = 6 567.93 5018 5037 37.8 5268 22 10:21:52 Other Pump 579 - Restarted 599.41 4844 4835 36.5 5181 23 10:28:54 Alarm Delta Stage At Top Perf = 7 858.19 4915 4938 37.2 5248 24 10:30:14 Alarm Delta Stage At Top Perf = 8 907.82 5049 5049 37.2 5333 25 10:31:52 Alarm Delta Stage At Top Perf = 9 968.52 5216 5199 37.1 5455 26 10:34:37 Alarm Delta Stage At Top Perf = 10 1070.55 5350 5372 37.1 5603 27 10:38:05 Alarm Delta Stage At Top Perf = 11 1199.02 5470 5483 37 5655 28 10:41:49 Alarm Delta Stage At Top Perf = 12 1337.18 5588 5601 37 5760 29 10:45:53 Alarm Delta Stage At Top Perf = 13 1487.55 5606 5614 37 5750 30 10:47:56 Other Load Dart 1563.22 5574 5609 36.9 5766 31 10:50:05 Alarm Delta Stage At Top Perf = 14 1642.66 5564 5596 37 5811 32 10:51:14 Other Shut Gate on Mover 1685.1 5529 5559 36.9 5810 33 10:54:11 Drop Ball Launch Dart 1795.34 5681 5702 37.6 5770 9 10:54:15 (06/19/25) Next Treatment Treatment Interval 9 1797.85 5680 5687 37.6 5765 34 10:54:25 Alarm Delta Stage At Top Perf = 15 1804.11 5659 5655 37.6 5758 35 10:57:32 Alarm Delta Stage At Top Perf = 16 1921.96 4854 4868 38 5714 36 11:00:26 Other Slow for Dart 2032.32 4000 3999 38.2 4644 37 11:01:20 Alarm Delta Stage At Top Perf = 17 2053.43 2362 2388 15.6 3844 38 11:02:58 Ball on Seat Dart on Seat 2078.69 2661 2693 15.5 3856 39 11:03:11 Break Formation Break Formation 2081.78 5916 5898 15.5 7142 40 11:04:35 Alarm Delta Stage At Top Perf = 1 2104.89 3993 4019 20.2 5044 41 11:06:22 Alarm Delta Stage At Top Perf = 2 2158.26 5009 5015 38.1 5638 42 11:08:05 Alarm Delta Stage At Top Perf = 3 2223.84 4337 4330 37.5 5062 43 11:13:33 Alarm Delta Stage At Top Perf = 4 2429.07 4162 4163 37.5 4719 44 11:21:21 Alarm Delta Stage At Top Perf = 5 2719.13 3974 3985 36.9 4724 45 11:22:39 Alarm Delta Stage At Top Perf = 6 2767.15 3990 4011 36.9 4734 46 11:24:19 Alarm Delta Stage At Top Perf = 7 2828.67 4078 4091 36.9 4795 47 11:27:06 Alarm Delta Stage At Top Perf = 8 2931.23 4232 4254 36.8 4914 48 11:30:37 Alarm Delta Stage At Top Perf = 9 3060.52 4372 4401 36.7 5025 49 11:34:24 Alarm Delta Stage At Top Perf = 10 3199.45 4532 4556 36.7 5124 50 11:38:31 Alarm Delta Stage At Top Perf = 11 3350.39 4699 4718 36.6 5238 51 11:42:48 Alarm Delta Stage At Top Perf = 12 3507.19 4853 4877 36.6 5345 52 11:43:42 Other Shut Gate on Mover 3540.09 4888 4898 36.6 5359 53 11:47:00 Drop Ball Launch Dart 3662.14 5161 5190 37.3 5416 10 11:47:01 (06/19/25) Next Treatment Treatment Interval 10 3662.76 5160 5189 37.3 5408 54 11:47:10 Alarm Delta Stage At Top Perf = 13 3668.35 5157 5177 37.3 5417 55 11:50:18 Alarm Delta Stage At Top Perf = 14 3785.55 4494 4515 37.5 5414 56 11:53:06 Other Slow for Dart 3890.81 3647 3683 37.7 4455 57 11:53:57 Alarm Delta Stage At Top Perf = 15 3911.18 2144 2197 15.7 3726 58 11:55:33 Ball on Seat Dart on Seat 3935.9 2412 2455 15.6 3724 59 11:55:44 Break Formation Break Formation 3939.03 5609 5631 15.7 7019 60 11:57:11 Alarm Delta Stage At Top Perf = 1 3962.32 2714 2759 19.1 3857 61 11:58:53 Alarm Delta Stage At Top Perf = 2 4012.04 3593 3596 37.3 4354 62 12:00:29 Alarm Delta Stage At Top Perf = 3 4072.29 3578 3592 37.7 4405 63 12:05:56 Alarm Delta Stage At Top Perf = 4 4277.77 3956 3975 37.6 4521 64 12:13:42 Alarm Delta Stage At Top Perf = 5 4567.47 3866 3876 37 4626 65 12:14:58 Alarm Delta Stage At Top Perf = 6 4614.39 3888 3921 37 4652 66 12:16:41 Alarm Delta Stage At Top Perf = 7 4677.88 4000 4026 37 4735 67 12:19:27 Alarm Delta Stage At Top Perf = 8 4780.04 4178 4204 36.9 4877 68 12:22:58 Alarm Delta Stage At Top Perf = 9 4909.66 4341 4353 36.8 4988 69 12:26:42 Alarm Delta Stage At Top Perf = 10 5046.96 4474 4502 36.8 5092 70 12:30:52 Alarm Delta Stage At Top Perf = 11 5199.96 4644 4670 36.7 5195 71 0.522974537 Other Load Dart 5281.33 4693 4758 36.7 5245 72 12:35:05 Alarm Delta Stage At Top Perf = 12 5354.69 4788 4816 36.6 5286 73 12:36:16 Other Shut Gate on Mover 5397.41 4849 4862 36.6 5304 74 12:39:22 Drop Ball Launch Dart 5512.19 5147 5182 37.3 5410 11 12:39:24 (06/19/25) Next Treatment Treatment Interval 11 5514.05 5146 5185 37.2 5413 75 12:39:26 Alarm Delta Stage At Top Perf = 13 5515.29 5155 5179 37.3 5415 76 12:42:36 Alarm Delta Stage At Top Perf = 14 5633.7 4504 4555 37.5 5461 77 12:46:09 Alarm Delta Stage At Top Perf = 15 5755.53 2243 2278 15.7 3785 78 12:47:48 Ball on Seat Dart on Seat 5781 2510 2542 15.6 3817 79 12:47:59 Break Formation Break Formation 5784.11 5633 5673 15.5 6700 80 12:49:22 Alarm Delta Stage At Top Perf = 1 5805.97 2908 2955 18.6 4016 81 12:51:17 Alarm Delta Stage At Top Perf = 2 5858.16 4155 4164 37 4866 82 12:52:51 Alarm Delta Stage At Top Perf = 3 5916.97 3860 3893 37.6 4647 83 12:58:16 Alarm Delta Stage At Top Perf = 4 6120.64 4049 4056 37.6 4571 84 13:06:01 Alarm Delta Stage At Top Perf = 5 6409.34 3868 3894 37 4554 85 13:07:18 Alarm Delta Stage At Top Perf = 6 6456.83 3927 3962 37 4585 86 13:08:58 Alarm Delta Stage At Top Perf = 7 6518.41 4039 4056 36.9 4652 87 13:11:44 Alarm Delta Stage At Top Perf = 8 6620.55 4191 4242 36.8 4794 88 13:15:16 Alarm Delta Stage At Top Perf = 9 6750.77 4331 4385 36.8 4901 89 13:19:01 Alarm Delta Stage At Top Perf = 10 6888.72 4474 4488 36.8 4989 90 13:23:13 Alarm Delta Stage At Top Perf = 11 7042.94 4633 4654 36.7 5075 91 13:27:28 Alarm Delta Stage At Top Perf = 12 7198.68 4770 4792 36.6 5147 92 13:29:12 Other Shut Gate on Mover 7262.11 4841 4877 36.6 5167 93 13:32:10 Alarm Delta Stage At Top Perf = 13 7371.84 5154 5165 37.2 5257 94 13:32:20 Drop Ball Launch Dart 7378.04 5140 5157 37.2 5264 12 13:32:23 (06/19/25) Next Treatment Treatment Interval 12 7379.28 5132 5152 37.2 5263 95 13:35:06 Alarm Delta Stage At Top Perf = 14 7481.34 4481 4513 37.5 5323 96 13:38:10 Other Slow for Dart 7596.43 3637 3689 37.6 4358 97 13:38:58 Alarm Delta Stage At Top Perf = 15 7613.64 2114 2180 15.7 3683 98 13:40:32 Ball on Seat Dart on Seat 7637.72 2394 2426 15.5 3691 99 13:40:42 Break Formation Break Formation 7640.56 5031 5115 15.5 6602 100 13:42:07 Alarm Delta Stage At Top Perf = 1 7663.53 2722 2760 20.1 3736 101 13:43:50 Alarm Delta Stage At Top Perf = 2 7716.56 3581 3627 37.4 4167 102 13:45:24 Alarm Delta Stage At Top Perf = 3 7775.39 3668 3704 37.6 4297 103 13:50:50 Alarm Delta Stage At Top Perf = 4 7979.48 4076 4108 37.5 4548 104 13:58:38 Alarm Delta Stage At Top Perf = 5 8270.29 3839 3865 37 4488 105 13:59:55 Alarm Delta Stage At Top Perf = 6 8317.76 3949 3954 37 4559 106 14:01:34 Alarm Delta Stage At Top Perf = 7 8378.78 4044 4089 37 4643 107 14:04:24 Alarm Delta Stage At Top Perf = 8 8483.59 4196 4193 37 4792 108 14:07:56 Alarm Delta Stage At Top Perf = 9 8614.2 4175 4206 37 4839 109 14:11:40 Alarm Delta Stage At Top Perf = 10 8752.22 4156 4184 36.9 4803 110 14:15:46 Alarm Delta Stage At Top Perf = 11 8903.49 4251 4255 36.9 4828 111 14:17:01 Other Load Dart 8949.61 4318 4340 36.9 4853 112 14:19:58 Alarm Delta Stage At Top Perf = 12 9058.18 4451 4449 36.8 4907 113 14:24:30 Alarm Delta Stage At Top Perf = 13 9226.23 4781 4781 37.4 5022 114 14:24:37 Drop Ball Launch Dart 9229.97 4772 4785 37.4 5030 13 14:24:39 (06/19/25) Next Treatment Treatment Interval 13 9231.22 4769 4782 37.4 5031 115 14:27:20 Alarm Delta Stage At Top Perf = 14 9332.57 4206 4207 37.7 5091 116 14:30:15 Other Slow for Dart 9442.81 3282 3302 37.9 4213 117 14:30:57 Alarm Delta Stage At Top Perf = 15 9457.86 2091 2133 15.9 3670 118 14:32:42 Ball on Seat Dart on Seat 9485.51 2302 2338 15.9 3672 119 14:32:52 Break Formation Break Formation 9488.16 5220 5221 15.9 6616 120 14:34:03 Alarm Delta Stage At Top Perf = 1 9507.76 2716 2740 20 3827 121 14:35:45 Alarm Delta Stage At Top Perf = 2 9559.62 3413 3431 37.4 4291 122 14:37:17 Alarm Delta Stage At Top Perf = 3 9617.49 3334 3362 37.8 4302 123 14:42:42 Alarm Delta Stage At Top Perf = 4 9821.77 3430 3473 37.8 4276 124 14:50:25 Alarm Delta Stage At Top Perf = 5 10112.51 3263 3306 37.4 4248 125 14:51:41 Alarm Delta Stage At Top Perf = 6 10159.92 3336 3382 37.4 4274 126 14:53:22 Alarm Delta Stage At Top Perf = 7 10222.77 3444 3466 37.3 4325 127 14:56:08 Alarm Delta Stage At Top Perf = 8 10325.8 3569 3595 37.2 4425 128 14:59:37 Alarm Delta Stage At Top Perf = 9 10454.58 3696 3723 37.2 4494 129 15:03:19 Alarm Delta Stage At Top Perf = 10 10591.91 3841 3852 37.1 4559 130 15:07:23 Alarm Delta Stage At Top Perf = 11 10742.41 4078 4134 36.9 4648 131 15:11:36 Alarm Delta Stage At Top Perf = 12 10897.9 4431 4433 36.8 4811 132 15:16:11 Alarm Delta Stage At Top Perf = 13 11067.08 4829 4868 37.5 4932 133 15:19:21 Alarm Delta Stage At Top Perf = 14 11185.62 4430 4464 37.5 5055 134 15:23:14 Alarm Delta Stage At Top Perf = 15 11331.67 3004 3132 37.7 4162 135 15:23:23 ISIP ISIP 11334.52 1150 804 0 3371 136 15:28:42 Shut-In Pressure @ 5 Minutes Shut-In Pressure @ 5 Minutes 11334.52 279 331 0 3339 137 15:32:41 Shut-In Pressure @ 10 Minutes Shut-In Pressure @ 10 Minutes 11334.52 -173 -155 0 3316 138 15:37:44 Shut-In Pressure @ 15 Minutes Shut-In Pressure @ 15 Minutes 11334.52 -212 -168 0 3293 Event Log 6.19.25 Conoco Phillips - 3T-613 Event Log 6.19.25 239 Seq No. Time Activity Code Comment Job Slurry Vol Treating Pressure Treating Pressure @Pump Slurry Rate Tubing Gauge BH Pres 1 06:43:54 (06/20/25) Start Job Starting Job 0 0 0 0 0 1 06:43:54 (06/20/25) Next Treatment Treatment Interval 1 0 0 0 0 1 2 7:03:59 Other Shut Down to Work LA1 0 -163 -109 0 2332 3 8:44:59 Prime Pumps Prime Pumps 0 57 69 0 2321 4 8:56:44 Pressure Test ePRV - Primary Tubing 0 995 1137 0 2320 5 8:58:08 Pressure Test ePRV - Primary IA 0 699 850 0 2320 6 8:59:51 Pressure Test ePRV - Secondary Tubing 0 1108 1258 0 2320 7 9:01:12 Pressure Test ePRV - Secondary IA 0 989 1069 0 2320 8 9:03:53 Other Testing Globals 0 872 720 0 2319 9 9:04:01 Other Testing Locals 0 870 736 0 2319 10 9:06:03 Pressure Test Pressure Test - Max 0 9535 9657 0 2319 14 09:28:08 (06/20/25) Next Treatment Treatment Interval 14 0 25 124 0 2391 11 9:29:33 Start Pumping Start Pumping 0 24 123 0 2353 12 9:30:57 Open Well Open Well 0 347 421 0 2372 13 9:32:26 Other Load Dart 6.96 1893 2011 11.8 3492 14 9:33:02 Drop Ball Launch Dart 15.26 2171 2295 14.9 3648 15 9:43:21 Other Slow for Dart 215.03 2347 2459 20.2 3913 16 9:46:07 Ball on Seat Dart on Seat 259.89 1934 2036 15.4 3660 17 9:46:16 Break Formation Break Formation 261.94 4652 4530 15.3 6229 18 9:46:46 Alarm Delta Stage At Top Perf = 4 269.83 2027 2135 15.3 3738 19 9:48:58 Alarm Delta Stage At Top Perf = 5 294.54 1592 1687 10.3 3479 20 9:51:46 ISIP ISIP 321.83 1168 1280 0 3290 21 10:56:48 Alarm Delta Stage At Top Perf = 6 551.2 3997 4133 37.2 4434 22 10:57:53 Alarm Delta Stage At Top Perf = 8 591.46 4173 4289 37.2 4509 23 10:59:04 Alarm Delta Stage At Top Perf = 9 635.43 4300 4384 37.2 4584 24 11:04:35 Alarm Delta Stage At Top Perf = 10 840.35 4346 4457 37.1 4601 25 11:12:32 Alarm Delta Stage At Top Perf = 11 1134.23 4044 4142 36.8 4499 26 11:13:50 Alarm Delta Stage At Top Perf = 12 1182.01 4095 4185 36.7 4570 27 11:15:30 Alarm Delta Stage At Top Perf = 13 1243.17 4176 4288 36.7 4635 28 11:18:18 Alarm Delta Stage At Top Perf = 14 1345.67 4284 4360 36.6 4643 29 11:21:50 Alarm Delta Stage At Top Perf = 15 1474.79 4444 4547 36.5 4755 30 11:25:37 Alarm Delta Stage At Top Perf = 16 1612.83 4590 4672 36.4 4844 31 11:29:47 Alarm Delta Stage At Top Perf = 17 1764.56 4615 4693 36.4 4929 32 11:32:23 Other Load Dart 1859.12 4581 4664 36.4 4866 33 11:34:04 Alarm Delta Stage At Top Perf = 18 1920.33 4574 4663 36.4 4876 34 11:36:10 Other Shut Gate on Mover 1996.62 4643 4746 36.3 4897 35 11:38:57 Alarm Delta Stage At Top Perf = 19 2099.08 4903 4998 37.1 4971 36 11:39:11 Drop Ball Launch Dart 2107.75 4881 4982 37.1 4981 15 11:39:13 (06/20/25) Next Treatment Treatment Interval 15 2108.99 4882 4974 37.1 4984 37 11:41:49 Alarm Delta Stage At Top Perf = 20 2205.83 4290 4369 37.4 5031 38 11:44:26 Other Slow for Dart 2303.79 3566 3701 37.5 4294 39 11:45:17 Alarm Delta Stage At Top Perf = 21 2321.51 2383 2504 15.5 3811 40 11:46:52 Ball on Seat Dart on Seat 2345.83 2554 2667 15.3 3782 41 11:47:03 Break Formation Break Formation 2348.38 5865 5970 15.3 6514 42 11:48:25 Alarm Delta Stage At Top Perf = 1 2370.51 2949 3097 20.8 3895 43 11:50:10 Alarm Delta Stage At Top Perf = 2 2422.53 3844 3937 36.9 4359 44 11:52:13 Alarm Delta Stage At Top Perf = 3 2499.22 3760 3872 37.5 4384 45 11:58:20 Alarm Delta Stage At Top Perf = 4 2728.45 3926 4041 37.4 4405 46 11:58:45 Other Pump 329 - Preload 2744.06 3915 4005 37.5 4391 47 12:06:25 Alarm Delta Stage At Top Perf = 5 3020.28 3670 3772 37.5 4340 48 12:07:42 Alarm Delta Stage At Top Perf = 6 3068.39 3622 3758 37.5 4302 49 12:09:27 Alarm Delta Stage At Top Perf = 7 3134 3738 3861 37.5 4372 50 12:12:19 Alarm Delta Stage At Top Perf = 8 3241.33 3874 3960 37.4 4428 51 12:16:00 Alarm Delta Stage At Top Perf = 9 3378.91 3933 4064 37.3 4498 52 12:19:52 Alarm Delta Stage At Top Perf = 10 3523.1 4032 4165 37.3 4551 53 12:24:11 Alarm Delta Stage At Top Perf = 11 3683.82 4194 4277 37.2 4619 54 12:28:38 Alarm Delta Stage At Top Perf = 12 3849.2 4284 4412 37.1 4655 55 12:31:21 Other Shut Gate on Mover 3949.26 4392 4510 37 4704 56 12:33:24 Alarm Delta Stage At Top Perf = 13 4026.41 4631 4737 37.9 4758 57 12:34:46 Drop Ball Launch Dart 4077.48 4691 4794 37.7 4805 16 12:34:49 (06/20/25) Next Treatment Treatment Interval 16 4079.36 4694 4797 37.7 4807 58 12:36:28 Alarm Delta Stage At Top Perf = 14 4142 4388 4496 37.8 4869 59 12:40:28 Alarm Delta Stage At Top Perf = 15 4282.53 2234 2332 15.7 3721 60 12:42:18 Ball on Seat Dart on Seat 4310.91 2379 2500 15.5 3711 61 12:42:28 Break Formation Break Formation 4313.24 5015 5029 15.5 6502 62 12:43:41 Alarm Delta Stage At Top Perf = 1 4333.34 2652 2758 19.6 3740 63 12:45:29 Alarm Delta Stage At Top Perf = 2 4384.19 3537 3630 36.9 4170 64 12:47:57 Alarm Delta Stage At Top Perf = 3 4476.63 3654 3764 37.5 4232 65 12:54:08 Alarm Delta Stage At Top Perf = 4 4708.13 3953 4051 37.4 4277 66 13:01:52 Alarm Delta Stage At Top Perf = 5 4996.24 3602 3692 37 4216 67 13:03:13 Alarm Delta Stage At Top Perf = 6 5046.09 3606 3689 36.9 4196 68 13:04:57 Alarm Delta Stage At Top Perf = 7 5110.07 3631 3751 36.9 4222 69 13:07:53 Alarm Delta Stage At Top Perf = 8 5218.17 3724 3827 36.8 4281 70 13:11:38 Alarm Delta Stage At Top Perf = 9 5356.09 3830 3961 36.7 4351 71 0.552476852 Alarm Delta Stage At Top Perf = 10 5500.33 3932 4047 36.7 4415 72 13:19:54 Alarm Delta Stage At Top Perf = 11 5658.97 4025 4126 36.6 4449 73 13:24:08 Other Load Dart 5813.6 4141 4254 36.5 4508 74 13:24:27 Alarm Delta Stage At Top Perf = 12 5825.15 4118 4270 36.5 4512 75 13:26:45 Other Shut Gate on Mover 5909 4260 4367 36.4 4529 76 13:29:17 Alarm Delta Stage At Top Perf = 13 6001.99 4399 4519 37.2 4571 77 13:30:41 Drop Ball Launch Dart 6053.4 4482 4597 37.2 4627 17 13:30:43 (06/20/25) Next Treatment Treatment Interval 17 6055.26 4477 4593 37.2 4632 78 13:32:29 Alarm Delta Stage At Top Perf = 14 6121.04 4126 4238 37.3 4653 79 13:36:25 Alarm Delta Stage At Top Perf = 15 6253.89 2270 2408 15.5 3687 80 13:38:00 Ball on Seat Dart on Seat 6278.2 2415 2540 15.4 3643 81 13:38:09 Break Formation Break Formation 6280.5 5541 5508 15.3 6295 82 13:39:30 Alarm Delta Stage At Top Perf = 1 6302.96 3048 3197 22.2 3931 83 13:41:10 Alarm Delta Stage At Top Perf = 2 6354.99 3579 3704 37.2 4082 84 13:43:09 Alarm Delta Stage At Top Perf = 3 6429.36 3465 3582 37.6 4075 85 13:49:21 Alarm Delta Stage At Top Perf = 4 6662.67 3563 3685 37.5 4016 86 13:57:05 Alarm Delta Stage At Top Perf = 5 6951.41 3368 3519 37 4032 87 13:58:27 Alarm Delta Stage At Top Perf = 6 7002 3353 3467 37 4016 88 14:00:15 Alarm Delta Stage At Top Perf = 7 7067.97 3448 3570 37 4063 89 14:03:09 Alarm Delta Stage At Top Perf = 8 7175.55 3552 3668 36.9 4128 90 14:06:53 Alarm Delta Stage At Top Perf = 9 7312.58 3600 3721 36.8 4184 91 14:10:47 Alarm Delta Stage At Top Perf = 10 7456.59 3672 3814 36.7 4227 92 14:15:07 Alarm Delta Stage At Top Perf = 11 7615.49 3786 3886 36.6 4268 93 14:19:37 Alarm Delta Stage At Top Perf = 12 7779.6 3905 4015 36.6 4327 94 14:23:10 Other Shut Gate on Mover 7908.94 3956 4100 36.5 4334 95 14:24:25 Alarm Delta Stage At Top Perf = 13 7955.61 4041 4168 37.2 4385 96 14:26:15 Drop Ball Launch Dart 8023.46 4207 4302 37.3 4405 18 14:26:19 (06/20/25) Next Treatment Treatment Interval 18 8025.97 4203 4296 37.3 4409 97 14:27:35 Alarm Delta Stage At Top Perf = 14 8073.91 3973 4081 37.4 4455 98 14:30:55 Other Slow for Dart 8198.43 3133 3245 37.6 3998 99 14:31:35 Alarm Delta Stage At Top Perf = 15 8214.24 1860 1949 16.5 3624 100 14:33:16 Ball on Seat Dart on Seat 8240.45 1855 1970 15.6 3594 101 14:33:27 Break Formation Break Formation 8243.31 5572 5754 15.6 6761 102 14:35:11 Alarm Delta Stage At Top Perf = 1 8266.08 1713 1852 10.6 3638 103 14:38:38 ISIP ISIP 8300.75 1029 1187 0 3323 104 15:11:03 Open Well Open Well 8300.75 1076 1175 0 3295 105 15:14:06 Start Pad Good XLink (Start Pad) 8345.48 3229 3347 30.7 4358 106 15:18:21 Alarm Delta Stage At Top Perf = 2 8501.64 3483 3613 37.4 4251 107 15:19:24 Alarm Delta Stage At Top Perf = 4 8540.86 3594 3722 37.4 4194 108 15:20:44 Alarm Delta Stage At Top Perf = 5 8590.67 3707 3853 37.3 4236 109 15:26:55 Alarm Delta Stage At Top Perf = 6 8821.27 3798 3912 37.2 4198 110 15:34:40 Alarm Delta Stage At Top Perf = 7 9109.16 3435 3556 36.9 4026 111 15:36:01 Alarm Delta Stage At Top Perf = 8 9158.88 3375 3517 36.8 4003 112 15:38:02 Alarm Delta Stage At Top Perf = 9 9233.09 3455 3586 36.8 4042 113 15:41:03 Alarm Delta Stage At Top Perf = 10 9343.86 3551 3679 36.7 4091 114 15:45:23 Alarm Delta Stage At Top Perf = 11 9502.6 3639 3783 36.6 4143 115 15:48:45 Alarm Delta Stage At Top Perf = 12 9625.7 3719 3869 36.6 4177 116 15:53:05 Alarm Delta Stage At Top Perf = 13 9784.19 3725 3876 36.6 4229 117 15:57:33 Alarm Delta Stage At Top Perf = 14 9947.43 3714 3858 36.5 4188 118 16:00:45 Other Shut Gate on Mover 10063.35 3819 3957 36.3 4211 119 16:02:23 Alarm Delta Stage At Top Perf = 15 10123.8 3942 4083 37.3 4257 120 16:03:57 Drop Ball Launch Dart 10181.72 4054 4199 37.3 4277 19 16:04:02 (06/20/25) Next Treatment Treatment Interval 19 10185.44 4062 4186 37.3 4275 121 16:05:29 Alarm Delta Stage At Top Perf = 16 10239.59 3808 3928 37.4 4315 122 16:08:23 Other Slow for Dart 10347.83 3172 3308 37.5 3983 123 16:09:26 Alarm Delta Stage At Top Perf = 17 10368.64 2196 2347 15.4 3657 124 16:10:59 Ball on Seat Dart on Seat 10392.3 2316 2456 15.2 3638 125 16:11:09 Break Formation Break Formation 10394.59 5354 5329 15.2 6196 126 16:12:37 Alarm Delta Stage At Top Perf = 1 10418 2644 2775 20 3655 127 16:14:22 Alarm Delta Stage At Top Perf = 2 10471.61 3440 3572 37.4 3998 128 16:16:29 Alarm Delta Stage At Top Perf = 3 10550.98 3350 3490 37.5 3956 129 16:22:40 Alarm Delta Stage At Top Perf = 4 10782.9 3524 3660 37.5 3981 130 16:30:27 Alarm Delta Stage At Top Perf = 5 11072.92 3285 3415 37 3915 131 16:31:49 Alarm Delta Stage At Top Perf = 6 11123.35 3258 3399 36.9 3908 132 16:33:34 Alarm Delta Stage At Top Perf = 7 11187.83 3315 3454 36.8 3927 133 16:36:31 Alarm Delta Stage At Top Perf = 8 11296.35 3412 3544 36.8 3976 134 16:40:15 Alarm Delta Stage At Top Perf = 9 11433.35 3521 3635 36.6 4015 135 16:44:11 Alarm Delta Stage At Top Perf = 10 11577.39 3624 3750 36.5 4061 136 16:48:30 Alarm Delta Stage At Top Perf = 11 11734.84 3714 3853 36.4 4108 137 16:53:01 Alarm Delta Stage At Top Perf = 12 11899.04 3817 3944 36.3 4143 138 16:56:52 Other Shut Gate on Mover 12038.38 3965 4074 36.2 4158 139 16:57:53 Alarm Delta Stage At Top Perf = 13 12075.23 4091 4213 36.7 4208 140 17:01:12 Alarm Delta Stage At Top Perf = 14 12198.6 3937 4032 37.2 4225 141 17:04:55 Alarm Delta Stage At Top Perf = 15 12337.44 1554 2321 37.4 3825 142 17:05:03 ISIP ISIP 12339.46 1277 1000 0 3346 143 17:10:13 Shut-In Pressure @ 5 Minutes Shut-In Pressure @ 5 Minutes 12339.46 386 508 0 3413 144 17:15:11 Shut-In Pressure @ 10 Minutes Shut-In Pressure @ 10 Minutes 12339.46 21 59 0 3394 145 17:20:00 Shut-In Pressure @ 15 Minutes Shut-In Pressure @ 15 Minutes 12339.46 -137 -18 0 3377 Event Log 6.20.25 Conoco Phillips - 3T-613 Event Log 6.20.25 240 Seq No. Time Activity Code Comment Job Slurry Vol Treating Pressure Treating Pressure @Pump Slurry Rate Tubing Gauge BH Pres 1 06:44:26 (06/21/25) Start Job Starting Job 0 0 0 0 0 1 06:44:26 (06/21/25) Next Treatment Treatment Interval 1 0 0 0 0 0 2 7:20:03 Prime Pumps Prime Pumps 0 0 2 0 2434 3 7:33:42 Pressure Test ePRV - Primary Tubing 0 734 856 0 2432 4 7:34:53 Pressure Test ePRV - Primary IA 0 825 956 0 2432 5 7:36:22 Pressure Test ePRV - Secondary Tubing 0 718 646 0 2431 6 7:37:32 Pressure Test ePRV - Secondary IA 0 699 615 0 2431 7 7:40:26 Other Testing Globals 0 739 857 0 2431 8 7:40:32 Other Testing Locals 0 753 871 0 2431 9 7:42:34 Pressure Test Pressure Test - Max 0 9498 9649 0 2430 10 7:49:22 Pressure Test Pressure Test - Pass 0 9468 9567 0 2429 11 8:58:19 Other Swapped LA's for BC-140 X2 0 -5 83 0 2420 20 09:13:51 (06/21/25) Next Treatment Treatment Interval 20 0 -6 83 0 2422 12 9:14:12 Start Pumping Start Pumping 0 0 95 0 2422 13 9:15:25 Open Well Open Well 0 463 516 0 2442 14 9:17:35 Drop Ball Launch Dart 15.96 2151 2250 14.4 3567 15 9:25:20 Other Slow for Dart 183.3 2515 2599 24.1 3847 16 9:27:10 Ball on Seat Dart on Seat 214.18 1794 1904 15.4 3495 17 9:27:17 Break Formation Break Formation 215.97 4629 4544 15.4 6136 18 9:27:53 Alarm Delta Stage At Top Perf = 4 225.43 2078 2161 15.3 3763 19 9:29:09 Alarm Delta Stage At Top Perf = 5 246.47 2388 2505 20.8 3896 20 9:35:57 Alarm Delta Stage At Top Perf = 6 453.88 3493 3594 37.2 3974 21 9:38:53 Alarm Delta Stage At Top Perf = 7 562.91 3897 3990 37.1 4040 22 9:49:26 Alarm Delta Stage At Top Perf = 8 954.87 601 735 34.1 3829 23 9:49:32 ISIP ISIP 955.82 913 794 0 3222 24 12:05:39 Open Well Open Well 955.82 846 917 0 3026 25 12:10:26 Start Pad Good XLink (Start Pad) 1027.03 2391 2502 24.5 3777 26 12:13:26 Other Burst Hose 1115.82 3225 3336 37.3 3961 27 12:14:59 Alarm Delta Stage At Top Perf = 10 1181.17 3303 3421 42.7 3891 28 12:16:53 Alarm Delta Stage At Top Perf = 11 1261.68 2919 3033 35.1 3777 29 12:26:31 Other Rate Adjustment 1597.82 3660 3778 37 3989 30 12:30:53 Alarm Delta Stage At Top Perf = 12 1759.77 3756 3868 37.4 3994 31 12:38:36 Alarm Delta Stage At Top Perf = 13 2048.7 3584 3708 37.4 3979 32 12:46:34 Alarm Delta Stage At Top Perf = 14 2346.43 3508 3629 37.3 3961 33 12:57:42 Alarm Delta Stage At Top Perf = 15 2761.01 3588 3692 37.1 3999 34 13:09:22 Alarm Delta Stage At Top Perf = 16 3192.91 3696 3817 36.9 4041 35 13:17:01 Alarm Delta Stage At Top Perf = 17 3474.93 3731 3850 36.9 4090 36 13:17:30 Other Load Dart 3492.78 3683 3794 36.9 4043 37 13:21:39 Other Shut Gate on Mover 3645.63 3571 3693 36.8 4034 38 13:23:24 Alarm Delta Stage At Top Perf = 18 3710.42 3597 3714 37.4 4045 39 13:25:11 Drop Ball Launch Dart 3777.31 3678 3773 37.4 4054 21 13:25:15 (06/21/25) Next Treatment Treatment Interval 21 3779.81 3673 3774 37.4 4053 40 13:29:15 Other Slow for Dart 3929.93 3148 3249 37.7 3919 41 13:30:00 Alarm Delta Stage At Top Perf = 19 3946.26 2156 2295 15.3 3660 42 13:32:04 Ball on Seat Dart on Seat 3977.36 2322 2434 15.2 3625 43 13:32:13 Break Formation Break Formation 3979.64 5449 5424 15.2 6248 44 13:33:21 Alarm Delta Stage At Top Perf = 1 3997.09 2316 2424 15.2 3533 45 13:35:22 Alarm Delta Stage At Top Perf = 2 4049.52 3347 3483 35.9 3839 46 13:37:29 Alarm Delta Stage At Top Perf = 3 4128.42 3148 3266 37.5 3778 47 13:42:50 Alarm Delta Stage At Top Perf = 4 4329.24 2681 2847 37.5 3743 48 13:42:58 ISIP ISIP 4331 1245 1289 0 3289 49 14:49:59 Open Well Open Well 4331 887 978 0 3081 50 14:57:59 Alarm Delta Stage At Top Perf = 6 4548.48 3092 3222 37.6 3754 51 14:58:48 Alarm Delta Stage At Top Perf = 7 4579.19 3162 3290 37.6 3732 52 15:00:13 Alarm Delta Stage At Top Perf = 8 4632.36 3334 3470 37.5 3806 53 15:04:02 Alarm Delta Stage At Top Perf = 9 4775.14 3313 3423 37.2 3897 54 15:06:02 Alarm Delta Stage At Top Perf = 10 4849.5 3254 3387 37.1 3887 55 15:08:50 Alarm Delta Stage At Top Perf = 11 4953.11 3263 3403 36.9 3912 56 15:11:47 Alarm Delta Stage At Top Perf = 12 5061.94 3353 3461 36.9 3923 57 15:13:40 Alarm Delta Stage At Top Perf = 13 5132.46 3513 3613 37.6 3913 58 15:15:13 Alarm Delta Stage At Top Perf = 14 5190.12 3847 3986 37.6 3957 59 15:18:51 Alarm Delta Stage At Top Perf = 15 5326.55 1232 1540 35.5 3893 60 15:18:58 ISIP ISIP 5326.55 1308 1453 0 3406 61 15:23:15 Shut-In Pressure @ 5 Minutes Shut-In Pressure @ 5 Minutes 5326.55 174 360 0 3534 62 15:28:15 Shut-In Pressure @ 10 Minutes Shut-In Pressure @ 10 Minutes 5326.55 645 747 0 3515 63 15:33:24 Shut-In Pressure @ 15 Minutes Shut-In Pressure @ 15 Minutes 5326.55 -29 74 0 3502 Event Log 6.21.25 Conoco Phillips - 3T-613 Event Log 6.21.25 241 Page 1/1 3T-613 Report Printed: 7/9/2025 Daily STIM Report ORIG SPUD DATE: [ 5/4/2025 ] DRLG RIG RELEASE: [ 6/5/2025 ] CMPLT JOB START [ 6/12/2025 ] ON PRODUCTION: [ ] DAYS FROM SPUD: [ 39.70 ] REPORT # [ 1] REPORT DATE: [ 6/12/2025] API / UWI 5010320914 Original KB/RT Elevation (ft) 51.00 Ground Elevation (ft) 12.00 Original Spud Date 5/4/2025 Job Category COMPLETIONS Primary Job Type INITIAL COMPLETION Total AFE (Cost) 7,944,313.57 AFE / RFE / Maint.# GKA.00044.E.W007.CO.I S;GKA.00044.E.W007.C O.IF;GKA.00044.E.W007. CO.IW Network/Order Number 11005807;11005806;1100 5808 AFE+Supp Amt (Cost) 7,944,313.57 Daily Cost Total (Cost) 90,050.00 Cumulative Cost (Cost) 90,050.00 Weather Temperature (°F) Road Condition Wind Last 24hr Summary BREAK DOWN TANK FARM FOR MOVE, LAY LINER/SEAM, BEGIN MOVING TANKS TO NEW LOCATION, SPOT IA/BLEED OFF/ePRV TANKS. FINISH RIGGING DOWN HARDLINE, LOAD CHEMICALS 24hr Forecast HAL - 15/3 General Remarks ZX Code ZX02 Fracturing Contact Name Title Mobile CAMPBELL, JAMES Frac Supervisor 661-203-1472 CHERRY, JACOB Supervisor 907-953-9294 Time Log Start Time Dur (hr) Phase Activity Code Time P-T-X Operation Start Depth (ftKB) End Depth (ftKB) 00:00 23.9 9 COMPZN, STIM RURD P BREAK DOWN TANK FARM FOR MOVE, LAY LINER/SEAM, BEGIN MOVING TANKS TO NEW LOCATION, SPOT IA/BLEED OFF/ePRV TANKS. FINISH RIGGING DOWN HARDLINE, LOAD CHEMICALS 0.0 Report Fluids Summary Fluid To well (bbl) Cum to Well (bbl) Contractor Rig Name/# Rig Supervisor Rig Accept Date RR Date Rig Type HES Frac Equipment FAUR, DAN,Wells Supervisor 6/12/2025 00:00 6/12/2025 23:59 FRAC HES 765 FERGUSON, SID,Wells Supervisor 6/12/2025 14:30 6/12/2025 21:00 SLICK LINE HES Frac Equipment FAUR, DAN,Wells Supervisor 6/13/2025 00:00 6/13/2025 23:59 FRAC HES 765 FERGUSON, SID,Wells Supervisor 6/13/2025 05:30 6/13/2025 22:15 SLICK LINE LRS 74-H FAUR, DAN,Wells Supervisor 6/14/2025 05:30 6/14/2025 13:00 PUMPING HES Frac Equipment FAUR, DAN,Wells Supervisor 6/15/2025 00:00 6/15/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 6/16/2025 00:00 6/16/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 6/17/2025 00:00 6/17/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 6/18/2025 00:00 6/18/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/19/2025 00:00 6/19/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/20/2025 00:00 6/20/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/21/2025 00:00 6/21/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/22/2025 00:00 6/22/2025 19:00 FRAC HES 765 ROGERS, BRENT,Wells Supervisor 6/23/2025 05:30 6/23/2025 19:45 SLICK LINE HES 765 ROGERS, BRENT,Wells Supervisor 6/24/2025 05:30 6/24/2025 12:30 SLICK LINE AES DHD RICHWINE, BRUCE,DHD Field Supervisor 6/26/2025 06:00 6/26/2025 18:00 WELL INTEGRITY HES 046 ROGERS, BRENT,Wells Supervisor 6/27/2025 05:30 6/27/2025 19:30 SLICK LINE Offline Activities Type Subtype Des Start Date End Date PUMPING 38 6/12/2025 14:30 6/12/2025 20:00 PUMPING 38 6/13/2025 07:30 6/18/2025 20:00 PUMPING 38 6/23/2025 08:00 6/24/2025 12:30 PUMPING 66 6/27/2025 07:00 6/27/2025 18:00 Page 1/2 3T-613 Report Printed: 7/9/2025 Daily STIM Report ORIG SPUD DATE: [ 5/4/2025 ] DRLG RIG RELEASE: [ 6/5/2025 ] CMPLT JOB START [ 6/12/2025 ] ON PRODUCTION: [ ] DAYS FROM SPUD: [ 39.57 ] REPORT # [ 2] REPORT DATE: [ 6/12/2025] API / UWI 5010320914 Original KB/RT Elevation (ft) 51.00 Ground Elevation (ft) 12.00 Original Spud Date 5/4/2025 Job Category COMPLETIONS Primary Job Type INITIAL COMPLETION Total AFE (Cost) 7,944,313.57 AFE / RFE / Maint.# GKA.00044.E.W007.CO.I S;GKA.00044.E.W007.C O.IF;GKA.00044.E.W007. CO.IW Network/Order Number 11005807;11005806;1100 5808 AFE+Supp Amt (Cost) 7,944,313.57 Daily Cost Total (Cost) Cumulative Cost (Cost) 90,050.00 Weather Temperature (°F) Road Condition Wind Last 24hr Summary DRIFT TBG TO 10354' SLM, TOOLS FALL SLOW, BUT NO OBSTRUCTIONS. SET 3.72" SLIP STOP CATCHER 2422' SLM, JOB IN PROGRESS. 24hr Forecast General Remarks T/IA/OA INITIAL=0/0/350 FINAL=25/25/350 ZX Code ZX50 Slickline / DSL Misc. (or Multiple Operations Contact Name Title Mobile ROGERS, ANTONIO Slickline Supervisor 907-203-5869 Time Log Start Time Dur (hr) Phase Activity Code Time P-T-X Operation Start Depth (ftKB) End Depth (ftKB) 14:30 1.00 COMPZN, STIM TRAV P *** START TKT 14:00 *** CONTACT DSO, ARRIVE, SIGN IN TO RIG SHACK, SPOT IN EQUIPMENT 0.0 15:30 0.50 COMPZN, STIM RURD P INSPECT AREA, PULL CUT 100', REPACK & RE-TIE ROPE SOCKET, RU .125" WIRE & 2.125" RLLR (2.62" WHEELS) TS= RS QC, QC 5' QC, QC KJ 5' QC, OJS, LSS (OAL 27') STACK PCE 16:00 2.50 COMPZN, STIM SLKL P PT W/ LRS 2500, RIH W/ QC 3.46" CENT 1.875" X 5' STEM 3.75" G. RING (OAL 81") TOOLS START FALLING 100' FPM ~ 3350' SLM, TOOLS FALL SLOWLY DOWN TO ~10100' SLM THEN START FALLING 40-50' FPM, STOP 10354' SLM, POOH, OOH W/ TOOLS 18:30 1.00 COMPZN, STIM SLKL P PT W/ LRS 2500, RIH W/ QC 4 1/2 GS (UNDERSIZED) 3.72" SLIP STOP CATCHER, TRIP & SET CATCHER 2422' SLM, POOH, OOH W/O CATCHER 19:30 0.50 COMPZN, STIM RURD P *** END TKT 19:00 *** LDFN, SECURE TREE CAP, INSPECT AREA, PJSM, NOTIFY DSO 20:00 1.00 COMPZN, STIM TRAV P TRAVEL TO F-WING, TIWF, SYNC CPU Report Fluids Summary Fluid To well (bbl) Cum to Well (bbl) Contractor Rig Name/# Rig Supervisor Rig Accept Date RR Date Rig Type HES Frac Equipment FAUR, DAN,Wells Supervisor 6/12/2025 00:00 6/12/2025 23:59 FRAC HES 765 FERGUSON, SID,Wells Supervisor 6/12/2025 14:30 6/12/2025 21:00 SLICK LINE HES Frac Equipment FAUR, DAN,Wells Supervisor 6/13/2025 00:00 6/13/2025 23:59 FRAC HES 765 FERGUSON, SID,Wells Supervisor 6/13/2025 05:30 6/13/2025 22:15 SLICK LINE LRS 74-H FAUR, DAN,Wells Supervisor 6/14/2025 05:30 6/14/2025 13:00 PUMPING HES Frac Equipment FAUR, DAN,Wells Supervisor 6/15/2025 00:00 6/15/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 6/16/2025 00:00 6/16/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 6/17/2025 00:00 6/17/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 6/18/2025 00:00 6/18/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/19/2025 00:00 6/19/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/20/2025 00:00 6/20/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/21/2025 00:00 6/21/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/22/2025 00:00 6/22/2025 19:00 FRAC HES 765 ROGERS, BRENT,Wells Supervisor 6/23/2025 05:30 6/23/2025 19:45 SLICK LINE HES 765 ROGERS, BRENT,Wells Supervisor 6/24/2025 05:30 6/24/2025 12:30 SLICK LINE AES DHD RICHWINE, BRUCE,DHD Field Supervisor 6/26/2025 06:00 6/26/2025 18:00 WELL INTEGRITY HES 046 ROGERS, BRENT,Wells Supervisor 6/27/2025 05:30 6/27/2025 19:30 SLICK LINE Offline Activities Type Subtype Des Start Date End Date PUMPING 38 6/12/2025 14:30 6/12/2025 20:00 PUMPING 38 6/13/2025 07:30 6/18/2025 20:00 Page 2/2 3T-613 Report Printed: 7/9/2025 Daily STIM Report ORIG SPUD DATE: [ 5/4/2025 ] DRLG RIG RELEASE: [ 6/5/2025 ] CMPLT JOB START [ 6/12/2025 ] ON PRODUCTION: [ ] DAYS FROM SPUD: [ 39.57 ] REPORT # [ 2] REPORT DATE: [ 6/12/2025] Offline Activities Type Subtype Des Start Date End Date PUMPING 38 6/23/2025 08:00 6/24/2025 12:30 PUMPING 66 6/27/2025 07:00 6/27/2025 18:00 Page 1/1 3T-613 Report Printed: 7/9/2025 Daily STIM Report ORIG SPUD DATE: [ 5/4/2025 ] DRLG RIG RELEASE: [ 6/5/2025 ] CMPLT JOB START [ 6/12/2025 ] ON PRODUCTION: [ ] DAYS FROM SPUD: [ 40.70 ] REPORT # [ 3] REPORT DATE: [ 6/13/2025] API / UWI 5010320914 Original KB/RT Elevation (ft) 51.00 Ground Elevation (ft) 12.00 Original Spud Date 5/4/2025 Job Category COMPLETIONS Primary Job Type INITIAL COMPLETION Total AFE (Cost) 7,944,313.57 AFE / RFE / Maint.# GKA.00044.E.W007.CO.I S;GKA.00044.E.W007.C O.IF;GKA.00044.E.W007. CO.IW Network/Order Number 11005807;11005806;1100 5808 AFE+Supp Amt (Cost) 7,944,313.57 Daily Cost Total (Cost) 90,050.00 Cumulative Cost (Cost) 180,100.00 Weather Temperature (°F) Road Condition Wind Last 24hr Summary FINISH MOVING TANK FARM, HYDRO TEST MANIFOLD AND BEGIN HEATING/LOADING SW. HAL LAY LINER AND SPOT EQUIPMENT, BEGIN RUNNING HARDLINE AND TIE IN PUMPS. PUT DOWN RIG MATS ON PAD EXPANSION. IN PROGRESS 24hr Forecast HAL - 15/3 General Remarks ZX Code ZX02 Fracturing Contact Name Title Mobile CAMPBELL, JAMES Frac Supervisor 661-203-1472 CHERRY, JACOB Supervisor 907-953-9294 Time Log Start Time Dur (hr) Phase Activity Code Time P-T-X Operation Start Depth (ftKB) End Depth (ftKB) 00:00 23.9 9 COMPZN, STIM RURD P FINISH MOVING TANK FARM, HYDRO TEST MANIFOLD AND BEGIN HEATING/LOADING SW. HAL LAY LINER AND SPOT EQUIPMENT, BEGIN RUNNING HARDLINE AND TIE IN PUMPS. PUT DOWN RIG MATS ON PAD EXPANSION. Report Fluids Summary Fluid To well (bbl) Cum to Well (bbl) Contractor Rig Name/# Rig Supervisor Rig Accept Date RR Date Rig Type HES Frac Equipment FAUR, DAN,Wells Supervisor 6/12/2025 00:00 6/12/2025 23:59 FRAC HES 765 FERGUSON, SID,Wells Supervisor 6/12/2025 14:30 6/12/2025 21:00 SLICK LINE HES Frac Equipment FAUR, DAN,Wells Supervisor 6/13/2025 00:00 6/13/2025 23:59 FRAC HES 765 FERGUSON, SID,Wells Supervisor 6/13/2025 05:30 6/13/2025 22:15 SLICK LINE LRS 74-H FAUR, DAN,Wells Supervisor 6/14/2025 05:30 6/14/2025 13:00 PUMPING HES Frac Equipment FAUR, DAN,Wells Supervisor 6/15/2025 00:00 6/15/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 6/16/2025 00:00 6/16/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 6/17/2025 00:00 6/17/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 6/18/2025 00:00 6/18/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/19/2025 00:00 6/19/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/20/2025 00:00 6/20/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/21/2025 00:00 6/21/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/22/2025 00:00 6/22/2025 19:00 FRAC HES 765 ROGERS, BRENT,Wells Supervisor 6/23/2025 05:30 6/23/2025 19:45 SLICK LINE HES 765 ROGERS, BRENT,Wells Supervisor 6/24/2025 05:30 6/24/2025 12:30 SLICK LINE AES DHD RICHWINE, BRUCE,DHD Field Supervisor 6/26/2025 06:00 6/26/2025 18:00 WELL INTEGRITY HES 046 ROGERS, BRENT,Wells Supervisor 6/27/2025 05:30 6/27/2025 19:30 SLICK LINE Offline Activities Type Subtype Des Start Date End Date PUMPING 38 6/12/2025 14:30 6/12/2025 20:00 PUMPING 38 6/13/2025 07:30 6/18/2025 20:00 PUMPING 38 6/23/2025 08:00 6/24/2025 12:30 PUMPING 66 6/27/2025 07:00 6/27/2025 18:00 Page 1/2 3T-613 Report Printed: 7/9/2025 Daily STIM Report ORIG SPUD DATE: [ 5/4/2025 ] DRLG RIG RELEASE: [ 6/5/2025 ] CMPLT JOB START [ 6/12/2025 ] ON PRODUCTION: [ ] DAYS FROM SPUD: [ 40.63 ] REPORT # [ 4] REPORT DATE: [ 6/13/2025] API / UWI 5010320914 Original KB/RT Elevation (ft) 51.00 Ground Elevation (ft) 12.00 Original Spud Date 5/4/2025 Job Category COMPLETIONS Primary Job Type INITIAL COMPLETION Total AFE (Cost) 7,944,313.57 AFE / RFE / Maint.# GKA.00044.E.W007.CO.I S;GKA.00044.E.W007.C O.IF;GKA.00044.E.W007. CO.IW Network/Order Number 11005807;11005806;1100 5808 AFE+Supp Amt (Cost) 7,944,313.57 Daily Cost Total (Cost) Cumulative Cost (Cost) 180,100.00 Weather Temperature (°F) Road Condition Wind Last 24hr Summary PULLED SOV FROM STA# 1 @ 2313' RKB, SET 1" INCONEL TOP SUB DMY. MIT-T PASSED @ 4200 PSI. MIT-IA PASSED @ 3850 PSI. PULLED 3.72" SLIP STOP CATCHER FROM 2422' SLM. READY FOR DISC SHEAR & INJECTIVITY. 24hr Forecast General Remarks T/IA/OA INITIAL=25/25/350 FINAL=175/0/350 ZX Code ZX50 Slickline / DSL Misc. (or Multiple Operations Contact Name Title Mobile ROGERS, ANTONIO Slickline Supervisor 907-203-5869 Time Log Start Time Dur (hr) Phase Activity Code Time P-T-X Operation Start Depth (ftKB) End Depth (ftKB) 05:30 1.50 COMPZN, STIM TRAV P HAL MEETING, MEET W/ CWG, GRAB WELL FILE, SYNC CPU, CONTACT DSO, TRAVEL TO 3T-613 07:00 0.50 COMPZN, STIM RURD P ARRIVE, INSPECT AREA, TGSM, RU .125" WIRE & 2.125" TS= RS QC, QC 5' QC, QC KJ 5' QC, OJS, LSS (OAL 27') STACK PCE 07:30 0.50 COMPZN, STIM WOOV P *** START TKT 08:00 *** STAND BY FOR SCAFFOLDING TO BE SIGNED OFF 08:00 1.00 COMPZN, STIM SLKL P PT W/ LRS 2500, RIH W/ QC KJ 4 1/2 OMK 1.25" JDC (OAL 108") LOC 2287' SLM MULTIPLE TIMES, UNABLE TO SD, ATTEMPT TO SLOP ON FOR 15 MIN, UNABLE, POOH, OOH W/ TOOLS, (ARM KICKED OUT) 09:00 1.00 COMPZN, STIM SLKL P PT W/ LRS 2500, RIH W/ QC 4 1/2 OMK 1.25" JDC (OAL 102") LOC & SD 2287' SLM / 2313' RKB, TAP DOWN, PICK UP SLIP OFF, SD TAP DOWN HARDER, SLIGHT OVER PULL, SD @ SAME TAP DOWN HARDER, SLIGHT OVER PULL, POOH, OOH W/ TOOLS, CONFER W/ CWG 10:00 1.00 COMPZN, STIM SLKL P PT W/ LRS 2500, RIH W/ QC 4 1/2 OMK 1.25" JDC (OAL 102") LOC & SD 2287' SLM / 2313' RKB, TAP DOWN LATCH UP, 3 OJ LICKS, COME FREE, POOH, OOH W/O VLV 11:00 1.00 COMPZN, STIM SLKL P PT W/ LRS 2500, RIH W/ QC 4 1/2 OMK 1.25" JDC (OAL 102") LOC & SD 2287' SLM / 2313' RKB, LOC SD 2285' SLM / 2313' RKB, TAP DOWN LATCH, UP, 1 OJ LICK, COME FREE, POOH, OOH W/ VLV 12:00 1.25 COMPZN, STIM SLKL P PT W/ LRS 2500, RIH W/ QC XO 4 1/2 OMK GA-2 RT 1" INCONEL DMY VLV (INTRAGAL LATCH) LOC SD 2283' SLM, START SETTING, SEE TRAVEL, PRESSURE TBG UP, IA TRACKING, JAR DOWN, BLEED IA OFF, PRESSURE UP TBG 600 PSI, NO CHANGE IA, WALK OFF VLV, NO CHANGE IN PRESSURE, POOH, OOH W/O VLV, TAKE PCE OFF WELL HEAD, SECURE TREE CAP 13:15 1.25 COMPZN, STIM SLKL P LRS RU TO TREE CAP TO PERFORM MIT-T T/IA/OA INITIAL 575/0/350 START 4250/300/375 (2.1 BBLS TO REACH PRESSURE) 15 MIN 4150/300/375 30 MIN 4100/300/375 PASS 14:30 2.25 COMPZN, STIM SLKL P LRS RU TO IA TO PERFORM MIT-IA, TBG TRACKING, CONFER W/ CWG, LRS ATTEMPT TO BLEED OFF IA PRESSURE, UNABLE TO FLOW BACK, TROUBLE SHOOT HOSE/CONNECTIONS, BLEED BACK IA & TBG, STAB BACK ON WELL Page 2/2 3T-613 Report Printed: 7/9/2025 Daily STIM Report ORIG SPUD DATE: [ 5/4/2025 ] DRLG RIG RELEASE: [ 6/5/2025 ] CMPLT JOB START [ 6/12/2025 ] ON PRODUCTION: [ ] DAYS FROM SPUD: [ 40.63 ] REPORT # [ 4] REPORT DATE: [ 6/13/2025] Time Log Start Time Dur (hr) Phase Activity Code Time P-T-X Operation Start Depth (ftKB) End Depth (ftKB) 16:45 2.00 COMPZN, STIM SLKL P PT W/ LRS 2500, RIH W/ QC KINLEY SWVL XO 4 1/2 OMK 7" EXT JK RT, LOC SD 2285' SLM / 2313' RKB, BLEED TBG TO 0 PSI, LRS RIG UP TO IA, JAR DOWN 15 TIME, LRS BRING IA UP TO 3850 FOR MIT-IA, POOH, OOH W/ TOOLS, LRS BLEED IA TO 0 START 0/0/300 INITAL 200/3850/550 15 MIN 250/3800/550 30 MIN 300/3750/550 45 MIN 325/3725/550 PASS 18:45 1.00 COMPZN, STIM SLKL P PT W/ LRS 3000, BRING TBG UP TO 3000 WATCH FOR 10 MIN, NO CHANGE, BLEED TBG BACK TO 150, RIH W/ QC 4 1/2 GR, SD LATCH SLIP STOP CATCHER 2422' SLM, 5 OJ LICKS, COME FREE, SEE WEIGHT INCREASE, POOH, OOH W/ CATCHER 19:45 1.00 COMPZN, STIM RURD P RDMO, SECURE TREE CAP, INSPECT AREA, PJSM, NOTIFY DSO 20:45 1.50 COMPZN, STIM TRAV P *** END TKT 21:00 *** STAGE EQUIPMENT ON 3S-624 FOR JOB IN AM, TRAVEL TO F-WING, SYNC CPU, TIWF Report Fluids Summary Fluid To well (bbl) Cum to Well (bbl) DIESEL 6.0 6.0 Contractor Rig Name/# Rig Supervisor Rig Accept Date RR Date Rig Type HES Frac Equipment FAUR, DAN,Wells Supervisor 6/12/2025 00:00 6/12/2025 23:59 FRAC HES 765 FERGUSON, SID,Wells Supervisor 6/12/2025 14:30 6/12/2025 21:00 SLICK LINE HES Frac Equipment FAUR, DAN,Wells Supervisor 6/13/2025 00:00 6/13/2025 23:59 FRAC HES 765 FERGUSON, SID,Wells Supervisor 6/13/2025 05:30 6/13/2025 22:15 SLICK LINE LRS 74-H FAUR, DAN,Wells Supervisor 6/14/2025 05:30 6/14/2025 13:00 PUMPING HES Frac Equipment FAUR, DAN,Wells Supervisor 6/15/2025 00:00 6/15/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 6/16/2025 00:00 6/16/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 6/17/2025 00:00 6/17/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 6/18/2025 00:00 6/18/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/19/2025 00:00 6/19/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/20/2025 00:00 6/20/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/21/2025 00:00 6/21/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/22/2025 00:00 6/22/2025 19:00 FRAC HES 765 ROGERS, BRENT,Wells Supervisor 6/23/2025 05:30 6/23/2025 19:45 SLICK LINE HES 765 ROGERS, BRENT,Wells Supervisor 6/24/2025 05:30 6/24/2025 12:30 SLICK LINE AES DHD RICHWINE, BRUCE,DHD Field Supervisor 6/26/2025 06:00 6/26/2025 18:00 WELL INTEGRITY HES 046 ROGERS, BRENT,Wells Supervisor 6/27/2025 05:30 6/27/2025 19:30 SLICK LINE Offline Activities Type Subtype Des Start Date End Date PUMPING 38 6/12/2025 14:30 6/12/2025 20:00 PUMPING 38 6/13/2025 07:30 6/18/2025 20:00 PUMPING 38 6/23/2025 08:00 6/24/2025 12:30 PUMPING 66 6/27/2025 07:00 6/27/2025 18:00 Page 1/2 3T-613 Report Printed: 7/9/2025 Daily STIM Report ORIG SPUD DATE: [ 5/4/2025 ] DRLG RIG RELEASE: [ 6/5/2025 ] CMPLT JOB START [ 6/12/2025 ] ON PRODUCTION: [ ] DAYS FROM SPUD: [ 41.24 ] REPORT # [ 5] REPORT DATE: [ 6/14/2025] API / UWI 5010320914 Original KB/RT Elevation (ft) 51.00 Ground Elevation (ft) 12.00 Original Spud Date 5/4/2025 Job Category COMPLETIONS Primary Job Type INITIAL COMPLETION Total AFE (Cost) 7,944,313.57 AFE / RFE / Maint.# GKA.00044.E.W007.CO.I S;GKA.00044.E.W007.C O.IF;GKA.00044.E.W007. CO.IW Network/Order Number 11005807;11005806;1100 5808 AFE+Supp Amt (Cost) 7,944,313.57 Daily Cost Total (Cost) 95,060.00 Cumulative Cost (Cost) 275,160.00 Weather Temperature (°F) Road Condition Wind Last 24hr Summary BURST DISK PUMPED 5.25 BBLS DSLTO BURST DISK @ 5000 PSI, THEN PUMPED 3.3 BBLS DSL AT @ 6300 PSI TO SHIFT SLEEVE. CONDUCTED INJECTIVITY TEST BY PUMPING 25 BBLS DSL @ 2 BPM @1900 PSI JOB COMPLETE 24hr Forecast HAL - 15/3 General Remarks INITIAL T/I/O= 25/25/350 FINAL T/I/O=1400/25/350 ZX Code ZX03 General Pumping (Load Well / Freeze Protect / Contact Name Title Mobile COOK, GREG Pump Operator N/A Time Log Start Time Dur (hr) Phase Activity Code Time P-T-X Operation Start Depth (ftKB) End Depth (ftKB) 05:30 1.00 COMPZN, STIM TRAV P TRAVEL TO LOCATION SPOT UNIT 06:30 3.50 COMPZN, STIM WOPT T WAITING ON SCAFFOLD INSPECTION AND HARDLINE CREW FOR HARDLINE. 10:00 0.75 COMPZN, STIM RURD P PJSM RU TO FLOWCROSS WITH HARD LINE PT SURFACE LINES 10000 PSI (PASSED) 10:45 1.00 COMPZN, STIM PUMP P PUMPED 3.75 BLS DSL TO BURST DISK @ 5000 PSI, THEN PUMPED 3.3 BBSL TO SHIFT SLEEVE @ 6300 PSI. PUMPED 25 BBLS DSL @2 BPM FOR INJECTIVITY TEST. START PRESSURING UP IA 0 BBLS, 1 BPM, DSL, 0/0/350 2.3 BBLS, 1 BPM, DSL, 0/2000/350 SD BRING UP TBG 0 BBLS, 1 BPM, DSL, 0/2000/350 1.2 BBLS, 1 BPM, DSL, 2000/2000/350 SD BRING UP IA 2.3 BBLS, 1 BPM, DSL, 2000/2000/350 3.8 BBLS, 1 BPM, DSL, 2000/3500/350 SD BRING UP TBG TO BURST DISK 1.2 BBLS, .75 BPM, 2000/3500/350 5.25 BBLS, .75 BPM, 5000/3500/350- BURST DISK START DOWN TBG FOR SLEEVE 5.25 BBLS, .75 BPM, 3000/3500/0350 8.55 BBLS, .75 BPM, 6300/3500/350- SLIDE SLEEVE START INJECTIVITY TEST 0 BBLS, 2 BPM, DSL, 1900/2000/350 10 BBLS, 2 BPM, DSL, 1900/2000/350 25 BBLS, 2 BPM, DSL, 1900/2000/350 SD FWP=1400/25/350 Page 2/2 3T-613 Report Printed: 7/9/2025 Daily STIM Report ORIG SPUD DATE: [ 5/4/2025 ] DRLG RIG RELEASE: [ 6/5/2025 ] CMPLT JOB START [ 6/12/2025 ] ON PRODUCTION: [ ] DAYS FROM SPUD: [ 41.24 ] REPORT # [ 5] REPORT DATE: [ 6/14/2025] Time Log Start Time Dur (hr) Phase Activity Code Time P-T-X Operation Start Depth (ftKB) End Depth (ftKB) 11:45 1.25 COMPZN, STIM RURD P FINISH PAPERWORK RDMO Report Fluids Summary Fluid To well (bbl) Cum to Well (bbl) DIESEL 38.0 44.0 Contractor Rig Name/# Rig Supervisor Rig Accept Date RR Date Rig Type HES Frac Equipment FAUR, DAN,Wells Supervisor 6/12/2025 00:00 6/12/2025 23:59 FRAC HES 765 FERGUSON, SID,Wells Supervisor 6/12/2025 14:30 6/12/2025 21:00 SLICK LINE HES Frac Equipment FAUR, DAN,Wells Supervisor 6/13/2025 00:00 6/13/2025 23:59 FRAC HES 765 FERGUSON, SID,Wells Supervisor 6/13/2025 05:30 6/13/2025 22:15 SLICK LINE LRS 74-H FAUR, DAN,Wells Supervisor 6/14/2025 05:30 6/14/2025 13:00 PUMPING HES Frac Equipment FAUR, DAN,Wells Supervisor 6/15/2025 00:00 6/15/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 6/16/2025 00:00 6/16/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 6/17/2025 00:00 6/17/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 6/18/2025 00:00 6/18/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/19/2025 00:00 6/19/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/20/2025 00:00 6/20/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/21/2025 00:00 6/21/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/22/2025 00:00 6/22/2025 19:00 FRAC HES 765 ROGERS, BRENT,Wells Supervisor 6/23/2025 05:30 6/23/2025 19:45 SLICK LINE HES 765 ROGERS, BRENT,Wells Supervisor 6/24/2025 05:30 6/24/2025 12:30 SLICK LINE AES DHD RICHWINE, BRUCE,DHD Field Supervisor 6/26/2025 06:00 6/26/2025 18:00 WELL INTEGRITY HES 046 ROGERS, BRENT,Wells Supervisor 6/27/2025 05:30 6/27/2025 19:30 SLICK LINE Offline Activities Type Subtype Des Start Date End Date PUMPING 38 6/12/2025 14:30 6/12/2025 20:00 PUMPING 38 6/13/2025 07:30 6/18/2025 20:00 PUMPING 38 6/23/2025 08:00 6/24/2025 12:30 PUMPING 66 6/27/2025 07:00 6/27/2025 18:00 Page 1/1 3T-613 Report Printed: 7/9/2025 Daily STIM Report ORIG SPUD DATE: [ 5/4/2025 ] DRLG RIG RELEASE: [ 6/5/2025 ] CMPLT JOB START [ 6/12/2025 ] ON PRODUCTION: [ ] DAYS FROM SPUD: [ 42.70 ] REPORT # [ 6] REPORT DATE: [ 6/15/2025] API / UWI 5010320914 Original KB/RT Elevation (ft) 51.00 Ground Elevation (ft) 12.00 Original Spud Date 5/4/2025 Job Category COMPLETIONS Primary Job Type INITIAL COMPLETION Total AFE (Cost) 7,944,313.57 AFE / RFE / Maint.# GKA.00044.E.W007.CO.I S;GKA.00044.E.W007.C O.IF;GKA.00044.E.W007. CO.IW Network/Order Number 11005807;11005806;1100 5808 AFE+Supp Amt (Cost) 7,944,313.57 Daily Cost Total (Cost) 97,292.33 Cumulative Cost (Cost) 372,452.33 Weather Temperature (°F) Road Condition Wind Last 24hr Summary CONTINUE TO LOAD/HEAT SW, MIRU SAND BIN, STAGE PROPPANT JOB VOL, FINISH PLACING MATS ON PAD EXPANSION, NIPPLE UP LAUNCH STACK AND REVOLVER, TIE IN TREATING LINE AND HANG DART DROP EQUALIZATION LINE. RUN RESTRAINTS ON TREATING LINES. VALVE SHOP GREASE TREE AND LAUNCH STACK 3T-612 SHUT IN @0615 6/15/25 AS PER RISK ASSESSMENT/PROCEDURE 24hr Forecast HAL - 15/3 General Remarks ZX Code ZX02 Fracturing Contact Name Title Mobile CAMPBELL, JAMES Frac Supervisor 661-203-1472 CHERRY, JACOB Supervisor 907-953-9294 Time Log Start Time Dur (hr) Phase Activity Code Time P-T-X Operation Start Depth (ftKB) End Depth (ftKB) 00:00 23.9 9 COMPZN, STIM RURD P CONTINUE TO LOAD/HEAT SW, MIRU SAND BIN, STAGE PROPPANT JOB VOL, FINISH PLACING MATS ON PAD EXPANSION, NIPPLE UP LAUNCH STACK AND REVOLVER, TIE IN TREATING LINE AND HANG DART DROP EQUALIZATION LINE. RUN RESTRAINTS ON TREATING LINES GREASE TREE/LAUNCH STACK 3T-612 SHUT IN @0615 6/15/25 AS PER RISK ASSESSMENT Report Fluids Summary Fluid To well (bbl) Cum to Well (bbl) DIESEL 44.0 Contractor Rig Name/# Rig Supervisor Rig Accept Date RR Date Rig Type HES Frac Equipment FAUR, DAN,Wells Supervisor 6/12/2025 00:00 6/12/2025 23:59 FRAC HES 765 FERGUSON, SID,Wells Supervisor 6/12/2025 14:30 6/12/2025 21:00 SLICK LINE HES Frac Equipment FAUR, DAN,Wells Supervisor 6/13/2025 00:00 6/13/2025 23:59 FRAC HES 765 FERGUSON, SID,Wells Supervisor 6/13/2025 05:30 6/13/2025 22:15 SLICK LINE LRS 74-H FAUR, DAN,Wells Supervisor 6/14/2025 05:30 6/14/2025 13:00 PUMPING HES Frac Equipment FAUR, DAN,Wells Supervisor 6/15/2025 00:00 6/15/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 6/16/2025 00:00 6/16/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 6/17/2025 00:00 6/17/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 6/18/2025 00:00 6/18/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/19/2025 00:00 6/19/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/20/2025 00:00 6/20/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/21/2025 00:00 6/21/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/22/2025 00:00 6/22/2025 19:00 FRAC HES 765 ROGERS, BRENT,Wells Supervisor 6/23/2025 05:30 6/23/2025 19:45 SLICK LINE HES 765 ROGERS, BRENT,Wells Supervisor 6/24/2025 05:30 6/24/2025 12:30 SLICK LINE AES DHD RICHWINE, BRUCE,DHD Field Supervisor 6/26/2025 06:00 6/26/2025 18:00 WELL INTEGRITY HES 046 ROGERS, BRENT,Wells Supervisor 6/27/2025 05:30 6/27/2025 19:30 SLICK LINE Offline Activities Type Subtype Des Start Date End Date PUMPING 38 6/12/2025 14:30 6/12/2025 20:00 PUMPING 38 6/13/2025 07:30 6/18/2025 20:00 PUMPING 38 6/23/2025 08:00 6/24/2025 12:30 PUMPING 66 6/27/2025 07:00 6/27/2025 18:00 Page 1/2 3T-613 Report Printed: 7/9/2025 Daily STIM Report ORIG SPUD DATE: [ 5/4/2025 ] DRLG RIG RELEASE: [ 6/5/2025 ] CMPLT JOB START [ 6/12/2025 ] ON PRODUCTION: [ ] DAYS FROM SPUD: [ 43.70 ] REPORT # [ 7] REPORT DATE: [ 6/16/2025] API / UWI 5010320914 Original KB/RT Elevation (ft) 51.00 Ground Elevation (ft) 12.00 Original Spud Date 5/4/2025 Job Category COMPLETIONS Primary Job Type INITIAL COMPLETION Total AFE (Cost) 7,944,313.57 AFE / RFE / Maint.# GKA.00044.E.W007.CO.I S;GKA.00044.E.W007.C O.IF;GKA.00044.E.W007. CO.IW Network/Order Number 11005807;11005806;1100 5808 AFE+Supp Amt (Cost) 7,944,313.57 Daily Cost Total (Cost) 491,045.79 Cumulative Cost (Cost) 863,498.12 Weather Temperature (°F) Road Condition Wind Last 24hr Summary STIMULATE STAGE 1- 2 PER DESIGN w/ 9000 LBS OF 100 MESH & 349884 LBS OF 16/20 PROPPANT UP TO 5.5 PPG, TOTAL JOB PROPPANT 358884 LB, JOB CLEAN VOLUME PUMPED 6636 BBL (PATINA TRACER ADDED PER SCHEDULE, NO RESMETRIC TRACER ADDED) DUE TO PUMP ISSUES/UNABLE TO ACHIEVE 37 BPM. STAGE 2 CUT SHORT, SHUT DOWN FOR PUMP MAINTENANCE. RESTART STAGE, PUMPED AS DESIGNED. 24hr Forecast HAL - 14/4 General Remarks INITIAL T/I/O=510 / 0 / 331 FINAL T/I/O=1450 / 700 / 469 ZX Code ZX02 Fracturing Contact Name Title Mobile CAMPBELL, JAMES Frac Supervisor 661-203-1472 CHERRY, JACOB Supervisor 907-953-9294 Time Log Start Time Dur (hr) Phase Activity Code Time P-T-X Operation Start Depth (ftKB) End Depth (ftKB) 00:00 6.50 COMPZN, STIM WAIT T MIX CHEMICALS, START EQUIPMENT FOR DAY SHIFT, SPOT CRANE TO LOAD 100M BAGS. 06:30 0.50 COMPZN, STIM WAIT T PJSM 07:00 2.00 COMPZN, STIM WAIT T HIGH CAL/LOW CAL DENSOMETER, FLOOD/PRIME EQUIPMENT, BUCKET TEST LA'S, FUNCTION TEST ePRV'S, PRESSURE TEST. PT MAX-9456 PSI PT 5 MIN - 9170 PSI GOOD TEST VERIFY/LOAD DARTS LRS PT IA HARDLINE WALK VALVE ALIGNMENT DOWN 09:00 0.50 COMPZN, STIM WAIT T HAL SWAP OUT ACID PUMP/DART PUMP DUE TO THROTTLE ISSUE RESPOT LRS AND PT LINE. 09:30 2.75 COMPZN, STIM PUMP P EQUALIZE TO 994 PSI, OPEN AT 510 PSI PERFORMED DFIT AT 10 BPM, SHUT IN MONITOR PSI FOR 41 MIN. CLOSURE 3142 PSI PERFORMED SRT IN 1 BBL INCREMENTS TO A MAX RATE OF 15 BPM STAGE 1 PUMPED THROUGH ALPHA SLEEVE, TOTAL CLEAN VOLUME PUMPED 2544 BBL, TOTAL PROPPANT PLACED 169940 LB, 100 MESH 3000 LB, 16/20 166940 LB, AVG PSI 4074, AVG BHP 5542 PSI, AVG RATE 36.0 BPM 12:15 0.90 COMPZN, STIM PUMP P LAUNCHED DART 1 FOR STAGE 2 @ 2727 JSV, LANDED 19 BBL EARLY @ 3055 JSV, SURFACE PEAK 6471 PSI, SURFACE DIFFERENTIAL 3324 PSI, BHP PEAK 7458 PSI, BHP DIFFERENTIAL 3195 PSI, TOTAL CLEAN VOLUME PUMPED 1611 BBL, TOTAL PROPPANT PLACED 115414 LB, 100 MESH 3000 LB, 16/20 12414 LB, AVG PSI 4235, AVG BHP 5085 PSI, AVG RATE 28.4 BPM 13:09 2.90 COMPZN, STIM WAIT T SHUT DOWN TO WORK ON PUMPS, UNABLE TO ACHIEVE 37 BPM. LOST 3/6 PUMPS PUMP #670 ENGINE KEEPS SHUTTING DOWN PUMP #621 RADIATOR CAP/OVER HEAT PUMP #584 ENGINE KEEPS SHUTTING DOWN Page 2/2 3T-613 Report Printed: 7/9/2025 Daily STIM Report ORIG SPUD DATE: [ 5/4/2025 ] DRLG RIG RELEASE: [ 6/5/2025 ] CMPLT JOB START [ 6/12/2025 ] ON PRODUCTION: [ ] DAYS FROM SPUD: [ 43.70 ] REPORT # [ 7] REPORT DATE: [ 6/16/2025] Time Log Start Time Dur (hr) Phase Activity Code Time P-T-X Operation Start Depth (ftKB) End Depth (ftKB) 16:03 2.10 COMPZN, STIM PUMP P PRIME PUMPS, PRESSURE TEST PT MAX - 9480 PSI PT 5 MIN - 9210 PSI GOOD TEST LRS BRING UP IA TO 3400 PSI EQUALIZE TO 1100 PSI, OPEN AT 1220 PSI STAGE 2 ( RESTART) - TOTAL CLEAN VOLUME PUMPED 4091 BBL, TOTAL PROPPANT PLACED 189652 LB, 100 MESH 3000 LB, 16/20 186652 LB, AVG PSI 4969, AVG BHP 5530 PSI, AVG RATE 35.9 BPM 18:09 0.90 COMPZN, STIM PUMP P ISIP-3725 PSI 5 MIN-3553 PSI 10 MIN-3533 PSI 15 MIN-3519 PSI FRREZE PROTECT TUBING - 35 BBLS DIESEL 19:03 4.94 COMPZN, STIM WAIT T PUMP MAINTENANCE, MIX CHEMICALS, LOAD GEL Report Fluids Summary Fluid To well (bbl) Cum to Well (bbl) DIESEL 35.0 79.0 FRAC FLUID 6,636.0 6,636.0 Contractor Rig Name/# Rig Supervisor Rig Accept Date RR Date Rig Type HES Frac Equipment FAUR, DAN,Wells Supervisor 6/12/2025 00:00 6/12/2025 23:59 FRAC HES 765 FERGUSON, SID,Wells Supervisor 6/12/2025 14:30 6/12/2025 21:00 SLICK LINE HES Frac Equipment FAUR, DAN,Wells Supervisor 6/13/2025 00:00 6/13/2025 23:59 FRAC HES 765 FERGUSON, SID,Wells Supervisor 6/13/2025 05:30 6/13/2025 22:15 SLICK LINE LRS 74-H FAUR, DAN,Wells Supervisor 6/14/2025 05:30 6/14/2025 13:00 PUMPING HES Frac Equipment FAUR, DAN,Wells Supervisor 6/15/2025 00:00 6/15/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 6/16/2025 00:00 6/16/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 6/17/2025 00:00 6/17/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 6/18/2025 00:00 6/18/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/19/2025 00:00 6/19/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/20/2025 00:00 6/20/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/21/2025 00:00 6/21/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/22/2025 00:00 6/22/2025 19:00 FRAC HES 765 ROGERS, BRENT,Wells Supervisor 6/23/2025 05:30 6/23/2025 19:45 SLICK LINE HES 765 ROGERS, BRENT,Wells Supervisor 6/24/2025 05:30 6/24/2025 12:30 SLICK LINE AES DHD RICHWINE, BRUCE,DHD Field Supervisor 6/26/2025 06:00 6/26/2025 18:00 WELL INTEGRITY HES 046 ROGERS, BRENT,Wells Supervisor 6/27/2025 05:30 6/27/2025 19:30 SLICK LINE Offline Activities Type Subtype Des Start Date End Date PUMPING 38 6/12/2025 14:30 6/12/2025 20:00 PUMPING 38 6/13/2025 07:30 6/18/2025 20:00 PUMPING 38 6/23/2025 08:00 6/24/2025 12:30 PUMPING 66 6/27/2025 07:00 6/27/2025 18:00 Stimulation Intervals Interval Number Start Date End Date Top (ftKB) Btm (ftKB) Proppant Designed (lb) Proppant Total (lb) Volume Clean Total (bbl) Volume Slurry Total (bbl) 1 6/16/2025 09:40 6/16/2025 12:12 23,276.8 23,281.2 173,000.0 169,232.0 2,557.93 2,737.71 2 6/16/2025 12:12 6/16/2025 18:08 22,818.9 22,823.2 186,200.0 189,652.0 4,126.48 4,328.01 Page 1/2 3T-613 Report Printed: 7/9/2025 Daily STIM Report ORIG SPUD DATE: [ 5/4/2025 ] DRLG RIG RELEASE: [ 6/5/2025 ] CMPLT JOB START [ 6/12/2025 ] ON PRODUCTION: [ ] DAYS FROM SPUD: [ 44.70 ] REPORT # [ 8] REPORT DATE: [ 6/17/2025] API / UWI 5010320914 Original KB/RT Elevation (ft) 51.00 Ground Elevation (ft) 12.00 Original Spud Date 5/4/2025 Job Category COMPLETIONS Primary Job Type INITIAL COMPLETION Total AFE (Cost) 7,944,313.57 AFE / RFE / Maint.# GKA.00044.E.W007.CO.I S;GKA.00044.E.W007.C O.IF;GKA.00044.E.W007. CO.IW Network/Order Number 11005807;11005806;1100 5808 AFE+Supp Amt (Cost) 7,944,313.57 Daily Cost Total (Cost) 865,551.19 Cumulative Cost (Cost) 1,729,049.31 Weather Temperature (°F) Road Condition Wind Last 24hr Summary STIMULATE STAGE 3- 6 PER DESIGN w/ 12000 LBS OF 100 MESH & 682055 LBS OF 16/20 PROPPANT UP TO 7 PPG, TOTAL JOB PROPPANT 694055 LB, JOB CLEAN VOLUME PUMPED 8101 BBL (NO RESMETRICS TRACER ADDED) JOB ON HOLD UNTIL HALLIBURTON BREAKER ARRIVES 24hr Forecast HAL - 14/4 General Remarks INITIAL T/I/O=694 / 0 / 313 FINAL T/I/O=1114 / 700 / 540 ZX Code ZX02 Fracturing Contact Name Title Mobile CAMPBELL, JAMES Frac Supervisor 661-203-1472 CHERRY, JACOB Supervisor 907-953-9294 Time Log Start Time Dur (hr) Phase Activity Code Time P-T-X Operation Start Depth (ftKB) End Depth (ftKB) 00:00 6.50 COMPZN, STIM WAIT T START EQUIPMENT FOR DAY SHIFT, MIX CHEMICALS, PUMP MAINTENANCE 06:30 0.50 COMPZN, STIM WAIT T PJSM 07:00 0.84 COMPZN, STIM WAIT T HIGH/LOW CAL DENSOMETER, BUCKET TEST LA'S, FUNCTIONS TEST EQUIPMENT, FLOOD/PRIME EQUIPMENT 07:50 1.10 COMPZN, STIM WAIT T WORK ON PUMP 177, WILL NOT PRIME. UNIT FOUND TO HAVE WASHED SEAT, PUMP BEING SWAPPED OUT 08:56 0.81 COMPZN, STIM WAIT T PRIME EQUIPMENT, FUNCTION TEST ePRV'S, PRESSURE TEST. PT MAX - 9503 PSI PT 5 MIN - 9315 PSI GOOD TEST VERIFY/LOAD DARTS, WALK OFF VALVE ALIGNMENT 09:45 1.96 COMPZN, STIM PUMP P EQUALIZE TO 1000 PSI, OPEN AT 694 PSI ESTABLISH RATE TO 15 BPM TO LAUNCH DART LAUNCHED DART 2 FOR STAGE 3 @ 27 JSV, LANDED 7 BBL EARLY @ 360 JSV, SURFACE PEAK 4173 PSI, SURFACE DIFFERENTIAL 1249 PSI, BHP PEAK 5306 PSI, BHP DIFFERENTIAL 1258 PSI, TOTAL CLEAN VOLUME PUMPED 2864 BBL, TOTAL PROPPANT PLACED 173152 LB, 100 MESH 3000 LB, 16/20 170152 LB, AVG PSI 5146, AVG BHP 5944 PSI, AVG RATE 26.5 BPM 11:42 0.98 COMPZN, STIM PUMP P LAUNCHED DART 3 FOR STAGE 4 @ 3052 JSV, LANDED 18 BBL EARLY @ 3366 JSV, SURFACE PEAK 6484 PSI, SURFACE DIFFERENTIAL 3326 PSI, BHP PEAK 7572 PSI, BHP DIFFERENTIAL 3236 PSI, TOTAL CLEAN VOLUME PUMPED 1872 BBL, TOTAL PROPPANT PLACED 173963 LB, 100 MESH 3000 LB, 16/20 170963 LB, AVG PSI 5240, AVG BHP 5647 PSI, AVG RATE 36.1 BPM 12:41 0.82 COMPZN, STIM PUMP P LAUNCHED DART 4 FOR STAGE 5 @ 5105 JSV, LANDED 20 BBL EARLY @ 5410 JSV, SURFACE PEAK 5889 PSI, SURFACE DIFFERENTIAL 3060 PSI, BHP PEAK 6723 PSI, BHP DIFFERENTIAL 2688 PSI, TOTAL CLEAN VOLUME PUMPED 1522 BBL, TOTAL PROPPANT PLACED 173488 LB, 100 MESH 3000 LB, 16/20 170488 LB, AVG PSI 5604, AVG BHP 5849 PSI, AVG RATE 35.9 BPM 13:30 0.96 COMPZN, STIM PUMP P LAUNCHED DART 5 FOR STAGE 6 @ 6830 JSV, LANDED 18 BBL EARLY @ 7129 JSV, SURFACE PEAK 6223 PSI, SURFACE DIFFERENTIAL 3571 PSI, BHP PEAK 7115 PSI, BHP DIFFERENTIAL 3161 PSI, TOTAL CLEAN VOLUME PUMPED 1844 BBL, TOTAL PROPPANT PLACED 173451 LB, 100 MESH 3000 LB, 16/20 170451 LB, AVG PSI 5114, AVG BHP 5527 PSI, AVG RATE 36.4 BPM Page 2/2 3T-613 Report Printed: 7/9/2025 Daily STIM Report ORIG SPUD DATE: [ 5/4/2025 ] DRLG RIG RELEASE: [ 6/5/2025 ] CMPLT JOB START [ 6/12/2025 ] ON PRODUCTION: [ ] DAYS FROM SPUD: [ 44.70 ] REPORT # [ 8] REPORT DATE: [ 6/17/2025] Time Log Start Time Dur (hr) Phase Activity Code Time P-T-X Operation Start Depth (ftKB) End Depth (ftKB) 14:28 0.82 COMPZN, STIM PUMP P ISIP-3367 PSI 5 MIN-3420 PSI 10 MIN-3403 PSI 15 MIN-3390 PSI FREEZE PROTECT TUBING - 35 BBLS DIESEL 15:17 8.70 COMPZN, STIM WAIT T STANDBY FOR OPTI BREAKER Report Fluids Summary Fluid To well (bbl) Cum to Well (bbl) DIESEL 35.0 114.0 FRAC FLUID 8,101.0 14,737.0 Contractor Rig Name/# Rig Supervisor Rig Accept Date RR Date Rig Type HES Frac Equipment FAUR, DAN,Wells Supervisor 6/12/2025 00:00 6/12/2025 23:59 FRAC HES 765 FERGUSON, SID,Wells Supervisor 6/12/2025 14:30 6/12/2025 21:00 SLICK LINE HES Frac Equipment FAUR, DAN,Wells Supervisor 6/13/2025 00:00 6/13/2025 23:59 FRAC HES 765 FERGUSON, SID,Wells Supervisor 6/13/2025 05:30 6/13/2025 22:15 SLICK LINE LRS 74-H FAUR, DAN,Wells Supervisor 6/14/2025 05:30 6/14/2025 13:00 PUMPING HES Frac Equipment FAUR, DAN,Wells Supervisor 6/15/2025 00:00 6/15/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 6/16/2025 00:00 6/16/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 6/17/2025 00:00 6/17/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 6/18/2025 00:00 6/18/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/19/2025 00:00 6/19/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/20/2025 00:00 6/20/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/21/2025 00:00 6/21/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/22/2025 00:00 6/22/2025 19:00 FRAC HES 765 ROGERS, BRENT,Wells Supervisor 6/23/2025 05:30 6/23/2025 19:45 SLICK LINE HES 765 ROGERS, BRENT,Wells Supervisor 6/24/2025 05:30 6/24/2025 12:30 SLICK LINE AES DHD RICHWINE, BRUCE,DHD Field Supervisor 6/26/2025 06:00 6/26/2025 18:00 WELL INTEGRITY HES 046 ROGERS, BRENT,Wells Supervisor 6/27/2025 05:30 6/27/2025 19:30 SLICK LINE Offline Activities Type Subtype Des Start Date End Date PUMPING 38 6/12/2025 14:30 6/12/2025 20:00 PUMPING 38 6/13/2025 07:30 6/18/2025 20:00 PUMPING 38 6/23/2025 08:00 6/24/2025 12:30 PUMPING 66 6/27/2025 07:00 6/27/2025 18:00 Stimulation Intervals Interval Number Start Date End Date Top (ftKB) Btm (ftKB) Proppant Designed (lb) Proppant Total (lb) Volume Clean Total (bbl) Volume Slurry Total (bbl) 3 6/17/2025 09:45 6/17/2025 11:42 22,324.9 22,329.3 173,000.0 172,757.0 2,877.29 3,060.81 4 6/17/2025 11:42 6/17/2025 12:40 21,829.6 21,833.9 173,000.0 174,116.0 1,871.93 2,056.89 5 6/17/2025 12:40 6/17/2025 13:29 21,331.6 21,336.0 173,000.0 173,488.0 1,521.64 1,705.94 6 6/17/2025 13:29 6/17/2025 14:27 20,834.2 20,838.5 173,000.0 173,731.0 1,857.26 2,041.82 Page 1/2 3T-613 Report Printed: 7/9/2025 Daily STIM Report ORIG SPUD DATE: [ 5/4/2025 ] DRLG RIG RELEASE: [ 6/5/2025 ] CMPLT JOB START [ 6/12/2025 ] ON PRODUCTION: [ ] DAYS FROM SPUD: [ 45.70 ] REPORT # [ 9] REPORT DATE: [ 6/18/2025] API / UWI 5010320914 Original KB/RT Elevation (ft) 51.00 Ground Elevation (ft) 12.00 Original Spud Date 5/4/2025 Job Category COMPLETIONS Primary Job Type INITIAL COMPLETION Total AFE (Cost) 7,944,313.57 AFE / RFE / Maint.# GKA.00044.E.W007.CO.I S;GKA.00044.E.W007.C O.IF;GKA.00044.E.W007. CO.IW Network/Order Number 11005807;11005806;1100 5808 AFE+Supp Amt (Cost) 7,944,313.57 Daily Cost Total (Cost) 293,209.53 Cumulative Cost (Cost) 2,022,258.84 Weather Temperature (°F) Road Condition Wind Last 24hr Summary JOB ON HOLD - WAIT FOR HALLIBURTON BREAKER TO ARRIVE STIMULATE STAGE 7 PER DESIGN w/ 3000 LBS OF 100 MESH & 169776 LBS OF 16/20 PROPPANT UP TO 7 PPG, TOTAL JOB PROPPANT 172776 LB, JOB CLEAN VOLUME PUMPED 2374 BBL (NO RESMETRICS TRACER ADDED) STAGE 8 LOST 3 PUMPS AND UNABLE TO ACHIEVE 37 BPM, LANDED DART AND PERFORMED MINI FRAC. 24hr Forecast HAL - 14/4 General Remarks INITIAL T/I/O=995 / 0 / 330 FINAL T/I/O=1200 / 700 / 388 ZX Code ZX02 Fracturing Contact Name Title Mobile CAMPBELL, JAMES Frac Supervisor 661-203-1472 CHERRY, JACOB Supervisor 907-953-9294 Time Log Start Time Dur (hr) Phase Activity Code Time P-T-X Operation Start Depth (ftKB) End Depth (ftKB) 00:00 16.0 0 COMPZN, STIM WAIT T JOB ON HOLD, WAIT FOR HALLIBURTON BREAKER TO ARRIVE FROM DH. HIGH/LOW CAL DENSOMETER, BUCKET TEST LA'S, FLOOD/PRIME EQUIPMENT 16:00 1.00 COMPZN, STIM WAIT T PJSM, FUNCTION TEST ePRV'S, PRESSURE TEST PT MAX - 9520 PSI PT 5 MIN - 9516 PSI GOOD TEST VERIFY/LOAD DARTS, WALK OFF VALVE ALIGNMENT LOAD CHEMICALS ONTO BLENDER AND MIX GEL 17:00 1.00 COMPZN, STIM PUMP P EQUALIZE TO 1283 PSI, OPEN AT 995 PSI LAUNCHED DART 7 FOR STAGE 8 @ 22 JSV, LANDED 13 BBL EARLY @ 319 JSV, SURFACE PEAK 5825 PSI, SURFACE DIFFERENTIAL 3085 PSI, BHP PEAK 6437 PSI, BHP DIFFERENTIAL 2554 PSI, TOTAL CLEAN VOLUME PUMPED 855 BBL, TOTAL PROPPANT PLACED 172776 LB, 100 MESH 3000 LB, 16/20 169776 LB, AVG PSI 4740, AVG BHP 5218 PSI, AVG RATE 36.1 BPM 18:00 0.44 COMPZN, STIM PUMP P LAUNCHED DART 7 FOR STAGE 8 @ 1709 JSV, LANDED 20 BBL EARLY @ 1990 JSV, SURFACE PEAK 6191 PSI, SURFACE DIFFERENTIAL 3322PSI, BHP PEAK 7136 PSI, BHP DIFFERENTIAL 3220 PSI, TOTAL CLEAN VOLUME PUMPED 855 BBL, AVG PSI 4740, AVG BHP 5218 PSI, AVG RATE 36.1 BPM LOST PUMP #670 DUE TO RADIATOR ISSUE , DECK ENGINE SHUT DOWN LOST PUMP #621 INTAKE MANIFOLD TOO HOT LOST PUMP #579 HOLE IN SUCTION MANIFOLD DUE TO PUMP/RATE ISSUES MINI FRAC PUMPED. PERFORMED MINI-FRAC, SHUT MONITORED PSI FOR 20 MIN 18:26 1.25 COMPZN, STIM PUMP P ISIP-3207 PSI 5 MIN-3343 PSI 10 MIN-3336 PSI 15 MIN-3324 PSI FREEZE PROTECT TUBING - 35 BBLS DIESEL 19:41 4.30 COMPZN, STIM WAIT T WORK ON PUMP ISSUES, TRANSFER CHEMICALS Report Fluids Summary Fluid To well (bbl) Cum to Well (bbl) DIESEL 35.0 149.0 Page 2/2 3T-613 Report Printed: 7/9/2025 Daily STIM Report ORIG SPUD DATE: [ 5/4/2025 ] DRLG RIG RELEASE: [ 6/5/2025 ] CMPLT JOB START [ 6/12/2025 ] ON PRODUCTION: [ ] DAYS FROM SPUD: [ 45.70 ] REPORT # [ 9] REPORT DATE: [ 6/18/2025] Report Fluids Summary Fluid To well (bbl) Cum to Well (bbl) FRAC FLUID 2,374.0 17,111.0 Contractor Rig Name/# Rig Supervisor Rig Accept Date RR Date Rig Type HES Frac Equipment FAUR, DAN,Wells Supervisor 6/12/2025 00:00 6/12/2025 23:59 FRAC HES 765 FERGUSON, SID,Wells Supervisor 6/12/2025 14:30 6/12/2025 21:00 SLICK LINE HES Frac Equipment FAUR, DAN,Wells Supervisor 6/13/2025 00:00 6/13/2025 23:59 FRAC HES 765 FERGUSON, SID,Wells Supervisor 6/13/2025 05:30 6/13/2025 22:15 SLICK LINE LRS 74-H FAUR, DAN,Wells Supervisor 6/14/2025 05:30 6/14/2025 13:00 PUMPING HES Frac Equipment FAUR, DAN,Wells Supervisor 6/15/2025 00:00 6/15/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 6/16/2025 00:00 6/16/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 6/17/2025 00:00 6/17/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 6/18/2025 00:00 6/18/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/19/2025 00:00 6/19/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/20/2025 00:00 6/20/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/21/2025 00:00 6/21/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/22/2025 00:00 6/22/2025 19:00 FRAC HES 765 ROGERS, BRENT,Wells Supervisor 6/23/2025 05:30 6/23/2025 19:45 SLICK LINE HES 765 ROGERS, BRENT,Wells Supervisor 6/24/2025 05:30 6/24/2025 12:30 SLICK LINE AES DHD RICHWINE, BRUCE,DHD Field Supervisor 6/26/2025 06:00 6/26/2025 18:00 WELL INTEGRITY HES 046 ROGERS, BRENT,Wells Supervisor 6/27/2025 05:30 6/27/2025 19:30 SLICK LINE Offline Activities Type Subtype Des Start Date End Date PUMPING 38 6/12/2025 14:30 6/12/2025 20:00 PUMPING 38 6/13/2025 07:30 6/18/2025 20:00 PUMPING 38 6/23/2025 08:00 6/24/2025 12:30 PUMPING 66 6/27/2025 07:00 6/27/2025 18:00 Stimulation Intervals Interval Number Start Date End Date Top (ftKB) Btm (ftKB) Proppant Designed (lb) Proppant Total (lb) Volume Clean Total (bbl) Volume Slurry Total (bbl) 7 6/18/2025 17:05 6/18/2025 18:00 20,336.3 20,340.7 173,000.0 172,746.0 1,531.45 1,714.96 8 6/18/2025 18:00 6/19/2025 10:54 19,795.4 19,799.8 193,000.0 192,471.0 2,453.98 2,658.43 Page 1/2 3T-613 Report Printed: 7/9/2025 Daily STIM Report ORIG SPUD DATE: [ 5/4/2025 ] DRLG RIG RELEASE: [ 6/5/2025 ] CMPLT JOB START [ 6/12/2025 ] ON PRODUCTION: [ ] DAYS FROM SPUD: [ 46.70 ] REPORT # [ 10] REPORT DATE: [ 6/19/2025] API / UWI 5010320914 Original KB/RT Elevation (ft) 51.00 Ground Elevation (ft) 12.00 Original Spud Date 5/4/2025 Job Category COMPLETIONS Primary Job Type INITIAL COMPLETION Total AFE (Cost) 7,944,313.57 AFE / RFE / Maint.# GKA.00044.E.W007.CO.I S;GKA.00044.E.W007.C O.IF;GKA.00044.E.W007. CO.IW Network/Order Number 11005807;11005806;1100 5808 AFE+Supp Amt (Cost) 7,944,313.57 Daily Cost Total (Cost) 1,430,475.81 Cumulative Cost (Cost) 3,452,734.65 Weather Temperature (°F) Road Condition Wind Last 24hr Summary COMPLETE STAGE 8-13 TOTAL PROPPANT PUMPED 1,156,087 LB, TOTAL CLEAN VOLUME 10,941 BBL, TOTAL SLURRY VOLUME 12,169 BBL 24hr Forecast HAL - 14/4 General Remarks INITIAL T/I/O=956 / 0 / 388 FINAL T/I/O=1108 / 700 / 403 ZX Code ZX02 Fracturing Contact Name Title Mobile CAMPBELL, JAMES Frac Supervisor 661-203-1472 LAWSON, JACOB Supervisor 971-606-0075 Time Log Start Time Dur (hr) Phase Activity Code Time P-T-X Operation Start Depth (ftKB) End Depth (ftKB) 00:00 8.00 COMPZN, STIM WAIT P LOAD PROPPANT, HEAT WATER 08:00 0.50 COMPZN, STIM WAIT P SAFETY MEETING 08:30 1.52 COMPZN, STIM WAIT P PRIME EQUIPMENT PSI TEST, STARTING PSI 9500, 5 MINUTE GOOD TEST,LOAD DARTS 8-12, WALK THE LINES CHECK PRVs, BRING UP IA PSI TO 3000 10:01 1.01 COMPZN, STIM PUMP P OPENING PSI 956,COMPLETED STAGE AS DESIGNED TOTAL CLEAN VOLUME PUMPED 2593 BBL, TOTAL PROPPANT PLACED 192,471 LB, 100 MESH 3000 LB, 189,471 16/20 LB, AVG PS 4961 I, AVG BHP PSI 5339, AVG RATE 35.2 BPM LAUNCHED DART FOR STAGE 9 @ 1796 JSV 11:01 0.92 COMPZN, STIM PUMP P DART LANDED @ 2079 11 BBL EARLY, SURFACE DIFF: 3255, BH DIFF: 3286, SURFACE PEAK: 5916, BH PEAK: 7142, TOTAL CLEAN VOLUME PUMPED BBL 1652, TOTAL PROPPANT PLACED 192,693 LB, 100 MESH 3000 LB, 16/20 189,693 LB, AVG PSI 4390, AVG BHP PSI 5016, AVG RATE BPM 36.4, LAUCHED DART FOR STAGE 10 @ 3661 JSV 11:57 0.86 COMPZN, STIM PUMP P DART LANDED @ 3936 12 BBL EARLY, SURFACE DIFF: 3197, BH DIFF: 3295, SURFACE PEAK: 5609, BH PEAK: 7019, TOTAL CLEAN VOLUME PUMPED BB 1639L, TOTAL PROPPANT PLACED LB 192200, 100 MESH 3000 LB, 16/20 186200 LB, AVG PSI 4186 , AVG BHP PSI 4835, AVG RATE BPM 36.6 ,DART FOR STAGE 11 LAUNCHED @ 5513 JSV 12:48 0.88 COMPZN, STIM PUMP P DART LANDED @ 5782 10 BBL EARLY, SURFACE DIFF: 3124, BH DIFF: 2928, SURFACE PEAK: 5633,BH PEAK: 6700, TOTAL CLEAN VOLUME PUMPED BBL, TOTAL PROPPANT PLACED 193,482 LB, 100 MESH 3000 LB, 16/20 190,482 LB, AVG PSI 1226 , AVG BHP PSI 4794, AVG RATE BPM 36.3, DART FOR STAGE 12 LAUNCHED @ 7378 JSV 13:41 0.85 COMPZN, STIM PUMP P DART LANDED @ 7638 BBL EARLY,SURFACE DIFF: 2637, BH DIFF: 2911, SURFACE PEAK: 5031, BH PEAK: 6602, TOTAL CLEAN VOLUME PUMPED BBL 1639, TOTAL PROPPANT PLACED LB 192,510, 100 MESH 3000 LB, 16/20 LB 189,250, AVG PSI 4086 , AVG BHP PSI 4649 , AVG RATE BPM 36.7, DART FOR STAGE 13 LAUNCHED @ 9230 JSV 14:32 0.85 COMPZN, STIM PUMP P DART LANDED @ 9486, 8 BBL EARLY,SURFACE DIFF: 2918, BH DIFF: 2944, SURFACE PEAK: 5220, BH PEAK: 6616 TOTAL CLEAN VOLUME PUMPED BBL, TOTAL PROPPANT PLACED LB 192,731, 100 MESH 3000 LB, 16/20 LB 189,731, AVG PSI 3,759 , AVG BHP PSI 4,4987, AVG RATE BPM 36.9, AFTER STAGE COMPLETION, HYDRAULIC AND IA WING VALVE WAS CLOSED FOR 15 MINUTE PSI MONITORING. 15:23 0.25 COMPZN, STIM PUMP P MONITORED BHG PSI FOR 15 MINUTES, FANNED OUT BLEW DOWN PUMPS, AND SUCK SIDE 15:38 0.50 COMPZN, STIM WAIT P LRS BLED DOWN IA TO 700 PSI CLOSED IN RIGGED OFF, SWAPPED TO THE TUBING LINE FOR FREEZE PROTECT PUMPING. 16:08 0.75 COMPZN, STIM PUMP P LRS PUMPED 37 BBL FREEZE PROTECT 16:53 7.10 COMPZN, STIM WAIT RELOADING WATER/ HEATING WATER, PUMP MAINTENANCE Page 2/2 3T-613 Report Printed: 7/9/2025 Daily STIM Report ORIG SPUD DATE: [ 5/4/2025 ] DRLG RIG RELEASE: [ 6/5/2025 ] CMPLT JOB START [ 6/12/2025 ] ON PRODUCTION: [ ] DAYS FROM SPUD: [ 46.70 ] REPORT # [ 10] REPORT DATE: [ 6/19/2025] Report Fluids Summary Fluid To well (bbl) Cum to Well (bbl) DIESEL 35.0 184.0 FRAC FLUID 10,941.0 28,052.0 Contractor Rig Name/# Rig Supervisor Rig Accept Date RR Date Rig Type HES Frac Equipment FAUR, DAN,Wells Supervisor 6/12/2025 00:00 6/12/2025 23:59 FRAC HES 765 FERGUSON, SID,Wells Supervisor 6/12/2025 14:30 6/12/2025 21:00 SLICK LINE HES Frac Equipment FAUR, DAN,Wells Supervisor 6/13/2025 00:00 6/13/2025 23:59 FRAC HES 765 FERGUSON, SID,Wells Supervisor 6/13/2025 05:30 6/13/2025 22:15 SLICK LINE LRS 74-H FAUR, DAN,Wells Supervisor 6/14/2025 05:30 6/14/2025 13:00 PUMPING HES Frac Equipment FAUR, DAN,Wells Supervisor 6/15/2025 00:00 6/15/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 6/16/2025 00:00 6/16/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 6/17/2025 00:00 6/17/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 6/18/2025 00:00 6/18/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/19/2025 00:00 6/19/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/20/2025 00:00 6/20/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/21/2025 00:00 6/21/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/22/2025 00:00 6/22/2025 19:00 FRAC HES 765 ROGERS, BRENT,Wells Supervisor 6/23/2025 05:30 6/23/2025 19:45 SLICK LINE HES 765 ROGERS, BRENT,Wells Supervisor 6/24/2025 05:30 6/24/2025 12:30 SLICK LINE AES DHD RICHWINE, BRUCE,DHD Field Supervisor 6/26/2025 06:00 6/26/2025 18:00 WELL INTEGRITY HES 046 ROGERS, BRENT,Wells Supervisor 6/27/2025 05:30 6/27/2025 19:30 SLICK LINE Offline Activities Type Subtype Des Start Date End Date PUMPING 38 6/12/2025 14:30 6/12/2025 20:00 PUMPING 38 6/13/2025 07:30 6/18/2025 20:00 PUMPING 38 6/23/2025 08:00 6/24/2025 12:30 PUMPING 66 6/27/2025 07:00 6/27/2025 18:00 Stimulation Intervals Interval Number Start Date End Date Top (ftKB) Btm (ftKB) Proppant Designed (lb) Proppant Total (lb) Volume Clean Total (bbl) Volume Slurry Total (bbl) 9 6/19/2025 10:54 6/19/2025 11:47 19,337.1 19,341.4 193,000.0 192,693.0 1,652.21 1,856.91 10 6/19/2025 11:47 6/19/2025 12:39 18,837.9 18,842.2 193,000.0 192,200.0 1,639.10 1,843.26 11 6/19/2025 12:39 6/19/2025 13:32 18,339.1 18,343.4 193,000.0 193,482.0 1,652.12 1,857.65 12 6/19/2025 13:32 6/19/2025 14:24 17,840.8 17,845.1 193,000.0 192,510.0 1,639.26 1,843.76 13 6/19/2025 14:24 6/19/2025 15:23 17,341.8 17,346.1 193,000.0 192,731.0 1,904.19 2,108.92 Page 1/2 3T-613 Report Printed: 7/9/2025 Daily STIM Report ORIG SPUD DATE: [ 5/4/2025 ] DRLG RIG RELEASE: [ 6/5/2025 ] CMPLT JOB START [ 6/12/2025 ] ON PRODUCTION: [ ] DAYS FROM SPUD: [ 47.70 ] REPORT # [ 11] REPORT DATE: [ 6/20/2025] API / UWI 5010320914 Original KB/RT Elevation (ft) 51.00 Ground Elevation (ft) 12.00 Original Spud Date 5/4/2025 Job Category COMPLETIONS Primary Job Type INITIAL COMPLETION Total AFE (Cost) 7,944,313.57 AFE / RFE / Maint.# GKA.00044.E.W007.CO.I S;GKA.00044.E.W007.C O.IF;GKA.00044.E.W007. CO.IW Network/Order Number 11005807;11005806;1100 5808 AFE+Supp Amt (Cost) 7,944,313.57 Daily Cost Total (Cost) 1,510,014.00 Cumulative Cost (Cost) 4,962,748.65 Weather Temperature (°F) Road Condition Wind Last 24hr Summary COMPLETED STAGES 14-19 TO DESIGN, TOTAL PROPPANT PLACED LB 1,203,842. TOTAL CLEAN VOLUME BBL 11,466, TOTAL SLURRY VOLUME BBL,12,316, 24hr Forecast HAL-16/4 General Remarks INITIAL T/I/O=956 / 0 / 303 FINAL T/I/O=1203 / 700 / 458 ZX Code ZX02 Fracturing Contact Name Title Mobile CAMPBELL, JAMES Frac Supervisor 661-203-1472 LAWSON, JACOB Supervisor 971-606-0075 Time Log Start Time Dur (hr) Phase Activity Code Time P-T-X Operation Start Depth (ftKB) End Depth (ftKB) 00:00 6.50 COMPZN, STIM WAIT P LOAD/HEAT WATER, GREASE THE FRAC STACK 06:30 0.50 COMPZN, STIM WAIT P SAFETY MEETING 07:00 1.75 COMPZN, STIM WAIT T WORKING ON LA PUMP FOR BC 140 08:45 0.50 COMPZN, STIM WAIT P PRIME UP PT, PT STARTING PSI 9539, 5 MINUTE ENDING PSI 9478 GOOD TEST. 09:15 0.25 COMPZN, STIM WAIT P MIX GEL, LOAD DARTS, 09:30 0.25 COMPZN, STIM PUMP P EQUALIZED TO 1500, OPENING PSI 386, ESTABLISHED INJECTION , BROUGHT RATE TO 15, DROPPED DART FOR STAGE 14 @ 15 JSV, DART LANDED @ 260 JSV, 11 BBL EARLY, SURFACE DIFF: 2637, BH DIFF: 2911, SURFACE PEAK: 5031, BH PEAK: 6602, DROPPED RATE TO 10 BPM. -40 BBL DISPLACEMENT FOR THE DFIT, HARD SHUT DOWN, CLOSE IN. 09:45 1.00 COMPZN, STIM WAIT P DFIT DATA ANALYZING, CLOSURE FOUND @ 2854 10:45 1.03 COMPZN, STIM PUMP P EQUALIZED OPENED WELL RESUMED STAGE, TOTAL CLEAN VOLUME PUMPED BBL 1910, TOTAL SLURRY VOLUME BBL 2,115, TOTAL PROPPANT PLACED LB 192080, 100 MESH 3000 LB, 16/20 LB 189080, AVG PSI 4,138 , AVG BHP PSI,4,607 , AVG RATE BPM 34.9 , LAUNCHED DART FOR STAGE 15 @ 2108JSV 11:46 0.93 COMPZN, STIM PUMP P STAGE 15 DART LANDED @ 2608 BBL, 11 BBL EARLY,SURFACE DIFF: 3311, BH DIFF: 2732, SURFACE PEAK: 5865, BH PEAK: 6514, TOTAL CLEAN VOLUME PUMPED BBL 1,748, TOTAL SLURRY VOLUME BBL 1,744 TOTAL PROPPANT PLACED LB 204,861, 100 MESH 3000 LB, 16/20 LB 201,461 , AVG PSI 3,939 , AVG BHP 4,465PSI , AVG RATE BPM 36.6, DART FOR STAGE 16 LAUNCHED @ 4078 JSV 12:42 0.90 COMPZN, STIM PUMP P STAGE 16 DART LANDED @ 4311 BBL, 8 BBL EARLY,SURFACE DIFF: 2636, BH DIFF: 2791, SURFACE PEAK: 5015, BH PEAK: 6502 , TOTAL CLEAN VOLUME PUMPED BBL 1,753, TOTAL SLURRY VOLUME BBL TOTAL PROPPANT PLACED LB 201,701 100 MESH 3000 LB, 16/20 LB 198,701 , AVG PSI 3,840 , AVG BHP PSI 4,317, AVG RATE BPM 36.4 , DART FOR STAGE 17 LAUNCHED @ 6054 JSV 13:36 0.96 COMPZN, STIM PUMP P STAGE 17 DART LANDED @ 6278 BBL, 10 BBL EARLY, SURFACE DIFF: 3126, BH DIFF: 2652, SURFACE PEAK: 5541, BH PEAK: 6295, TOTAL CLEAN VOLUME PUMPED BBL 1,748, TOTAL SLURRY VOLUME BBL 1,962 TOTAL PROPPANT PLACED LB 201,692 , 100 MESH 3000 LB, 16/20 LB 198,692, AVG PSI 3,621 , AVG BHP PSI 4,151, AVG RATE BPM 36.5, DART FOR STAGE 18 LAUNCHED @ 8024 JSV LOIL HAD LOADING BELT ISSUES, SHUTTING DOWN FOR THEM TO CONTINUE STEADY LOADING, BUILT IN A DFIT TO UTILIZE THE SHUT DOWN TIME. 14:34 0.60 COMPZN, STIM WAIT P DFIT, PSI MONITOURING LOIL CONTIUING TO LOAD PROPPANT Page 2/2 3T-613 Report Printed: 7/9/2025 Daily STIM Report ORIG SPUD DATE: [ 5/4/2025 ] DRLG RIG RELEASE: [ 6/5/2025 ] CMPLT JOB START [ 6/12/2025 ] ON PRODUCTION: [ ] DAYS FROM SPUD: [ 47.70 ] REPORT # [ 11] REPORT DATE: [ 6/20/2025] Time Log Start Time Dur (hr) Phase Activity Code Time P-T-X Operation Start Depth (ftKB) End Depth (ftKB) 15:10 1.00 COMPZN, STIM PUMP P RESUMED STAGE 18 TREATMENT, TOTAL CLEAN VOLUME PUMPED BBL 1,936, TOTAL SLURRY VOLUME BBL 2,151, TOTAL PROPPANT PLACED LB 201,933, 100 MESH 3000 LB, 16/20 LB 198,933, AVG PSI 3,589, AVG BHP PSI 4,167 , AVG RATE BPM 35.5, DART FOR STAGE 19 LAUNCHED @ 10182 JSV 16:10 0.88 COMPZN, STIM PUMP P STAGE 19 DART LANDED @ BBL 10,393, 7 BBL EARLY,SURFACE DIFF: 3038, BH DIFF: 2558, SURFACE PEAK: 3038, BH PEAK: 6196 , TOTAL CLEAN VOLUME PUMPED BBL 1,945, TOTAL SLURRY VOLUME BBL 2,159, TOTAL PROPPANT PLACED LB 201,575 , 100 MESH 3000 LB, 16/20 LB 198,575 , AVG PSI 3,551, AVG BHP PSI 4,030, AVG RATE BPM 36.4, CLOSED HYDRAULIC VALVE, BLOCKED IN THE IA FOR THE 15 MINUTE PSI MONITORING 17:03 0.25 COMPZN, STIM WAIT P MONITOR PRESSURE FOR 15 MINUTES, FAN OUT , BLOW DOWN EQUIPMENT 17:18 0.30 COMPZN, STIM WAIT P CONTINUE EQUIPMENT CLEANUP, LRS RIG OFF THE IA AND RIG UP TO THE TUBING FOR FREEZE PROTECT 17:36 0.50 COMPZN, STIM PUMP P LRS PUMPED 35 BBL FREEZE PROTECT 18:06 5.89 COMPZN, STIM WAIT P RELOAD HEAT/WATER, PUMP MAINTENANCE Report Fluids Summary Fluid To well (bbl) Cum to Well (bbl) DIESEL 35.0 219.0 FRAC FLUID 10,466.0 38,518.0 Contractor Rig Name/# Rig Supervisor Rig Accept Date RR Date Rig Type HES Frac Equipment FAUR, DAN,Wells Supervisor 6/12/2025 00:00 6/12/2025 23:59 FRAC HES 765 FERGUSON, SID,Wells Supervisor 6/12/2025 14:30 6/12/2025 21:00 SLICK LINE HES Frac Equipment FAUR, DAN,Wells Supervisor 6/13/2025 00:00 6/13/2025 23:59 FRAC HES 765 FERGUSON, SID,Wells Supervisor 6/13/2025 05:30 6/13/2025 22:15 SLICK LINE LRS 74-H FAUR, DAN,Wells Supervisor 6/14/2025 05:30 6/14/2025 13:00 PUMPING HES Frac Equipment FAUR, DAN,Wells Supervisor 6/15/2025 00:00 6/15/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 6/16/2025 00:00 6/16/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 6/17/2025 00:00 6/17/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 6/18/2025 00:00 6/18/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/19/2025 00:00 6/19/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/20/2025 00:00 6/20/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/21/2025 00:00 6/21/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/22/2025 00:00 6/22/2025 19:00 FRAC HES 765 ROGERS, BRENT,Wells Supervisor 6/23/2025 05:30 6/23/2025 19:45 SLICK LINE HES 765 ROGERS, BRENT,Wells Supervisor 6/24/2025 05:30 6/24/2025 12:30 SLICK LINE AES DHD RICHWINE, BRUCE,DHD Field Supervisor 6/26/2025 06:00 6/26/2025 18:00 WELL INTEGRITY HES 046 ROGERS, BRENT,Wells Supervisor 6/27/2025 05:30 6/27/2025 19:30 SLICK LINE Offline Activities Type Subtype Des Start Date End Date PUMPING 38 6/12/2025 14:30 6/12/2025 20:00 PUMPING 38 6/13/2025 07:30 6/18/2025 20:00 PUMPING 38 6/23/2025 08:00 6/24/2025 12:30 PUMPING 66 6/27/2025 07:00 6/27/2025 18:00 Stimulation Intervals Interval Number Start Date End Date Top (ftKB) Btm (ftKB) Proppant Designed (lb) Proppant Total (lb) Volume Clean Total (bbl) Volume Slurry Total (bbl) 14 6/20/2025 09:30 6/20/2025 11:39 16,843.2 16,847.5 193,000.0 192,080.0 1,910.48 2,114.52 15 6/20/2025 11:39 6/20/2025 12:34 16,349.4 16,353.8 203,000.0 204,861.0 1,744.21 1,961.83 16 6/20/2025 12:34 6/20/2025 13:30 15,850.5 15,854.9 203,000.0 201,701.0 1,753.10 1,967.35 17 6/20/2025 13:30 6/20/2025 14:26 15,352.2 15,356.5 203,000.0 201,692.0 1,748.07 1,962.32 18 6/20/2025 14:26 6/20/2025 16:04 14,854.3 14,858.6 203,000.0 201,933.0 1,936.40 2,150.91 19 6/20/2025 16:04 6/20/2025 17:05 14,356.4 14,360.7 203,000.0 201,575.0 1,944.71 2,158.84 Page 1/2 3T-613 Report Printed: 7/9/2025 Daily STIM Report ORIG SPUD DATE: [ 5/4/2025 ] DRLG RIG RELEASE: [ 6/5/2025 ] CMPLT JOB START [ 6/12/2025 ] ON PRODUCTION: [ ] DAYS FROM SPUD: [ 48.70 ] REPORT # [ 12] REPORT DATE: [ 6/21/2025] API / UWI 5010320914 Original KB/RT Elevation (ft) 51.00 Ground Elevation (ft) 12.00 Original Spud Date 5/4/2025 Job Category COMPLETIONS Primary Job Type INITIAL COMPLETION Total AFE (Cost) 7,944,313.57 AFE / RFE / Maint.# GKA.00044.E.W007.CO.I S;GKA.00044.E.W007.C O.IF;GKA.00044.E.W007. CO.IW Network/Order Number 11005807;11005806;1100 5808 AFE+Supp Amt (Cost) 7,944,313.57 Daily Cost Total (Cost) 603,852.04 Cumulative Cost (Cost) 5,566,600.69 Weather Temperature (°F) Road Condition Wind Last 24hr Summary COMPLETED STAGES 20-21 TO DESIGN, TOTAL PROPPANT PLACED LB 261,195 TOTAL CLEAN VOLUME BBL 5,052, TOTAL SLURRY VOLUME BBL 5,330, 24hr Forecast HAL-16/4 General Remarks INITIAL T/I/O=956 / 0 / 375 FINAL T/I/O=1308 / 700 / 496 ZX Code ZX02 Fracturing Contact Name Title Mobile CAMPBELL, JAMES Frac Supervisor 661-203-1472 LAWSON, JACOB Supervisor 971-606-0075 Time Log Start Time Dur (hr) Phase Activity Code Time P-T-X Operation Start Depth (ftKB) End Depth (ftKB) 00:00 6.50 COMPZN, STIM WAIT P REPLACED VALVES ON ALL PUMPS AND 2 SEATS, TOPED OFF NEEDED WATER FOR THE DAY 06:30 0.50 COMPZN, STIM WAIT P SAFETY MEETING 07:00 0.34 COMPZN, STIM WAIT P BUCKET TESTING, FUNCTION TESTING EQUIPMENT 07:20 0.50 COMPZN, STIM WAIT P PRIME EQUIPMENT, TEST PRV'S, PRESSURE TEST, STARTING PSI 9543, 5 MINUTE ENDING 9478 PSI GOOD TEST 07:50 1.40 COMPZN, STIM WAIT T BC 140 LA PUMP ISSUES 09:14 0.60 COMPZN, STIM PUMP P EQUALIZE TO 1200 PSI, OPENING PSI 443, ROLLED PUMP ESTABLISHED INJECTION, DROPPED DART FOR STAGE 20 @ 16 BBL JSV, DART LANDED @ 214 BBL JSV, 13 BBL SURFACE DIFF: 2874, BH DIFF: 2641, SURFACE PEAK: 4668, BH PEAK: 6136, ESTABLISHED FLUID @22 BPM, GOOD XL, BROUGHT RATE TO 37 BPM, PERFORMED MINI-FRAC, SHUT DOWN FOR PSI MONITORING 09:50 2.20 COMPZN, STIM PUMP P CLOSURE FOUND @3010 PSI RESUMED STAGE 20 TREATMENT, TOTAL CLEAN VOLUME PUMPED BBL 3,570, TOTAL SLURRY VOLUME BBL 3,786, TOTAL PROPPANT PLACED LB 202,999, 100 MESH 3000 LB, 16/20 LB 1199,999, AVG PSI 3,482, AVG BHP PSI 3,973, AVG RATE BPM 35.9, DART FOR STAGE 21 LAUNCHED @ 3778 JSV 12:02 1.50 COMPZN, STIM PUMP P STAGE 21 DART LANDED @ 3978 BBL , 3 BBL EARLY,SURFACE DIFF: 3127, BH DIFF: 2623, SURFACE PEAK: 5449, BH PEAK: 6248, MINI FRAC COMPLETED, SHUT DOWN FOR CLOSURE, PSI MONITORING 13:32 1.30 COMPZN, STIM WAIT P MONITOURING PSI 14:50 0.50 COMPZN, STIM PUMP P RESUMED STAGE 21, TOTAL CLEAN VOLUME PUMPED BBL 1,482, TOTAL SLURRY VOLUME BBL 1,544, TOTAL PROPPANT PLACED LB 16/20 58,196, AVG PSI 3,203, AVG BHP PSI 3,858, AVG RATE BPM35.2, CLOSED HYDRAULIC VALVE, BLOCKED IN THE IA FOR THE 15 MINUTE PSI MONITORING 15:20 1.00 COMPZN, STIM WAIT P 15 MINUTE PSI MONITOURING, FANNING OUT, BLOWING DOWN. 16:20 0.65 COMPZN, STIM PUMP P LRS PUMPE 35 BBL FREEZE PROTECT, CONTINUE EQUIPMENT CLEANUP 16:59 7.00 COMPZN, STIM DMOB P BEGIN RIGGING DOWN Report Fluids Summary Fluid To well (bbl) Cum to Well (bbl) DIESEL 35.0 254.0 FRAC FLUID 5,052.0 43,570.0 Contractor Rig Name/# Rig Supervisor Rig Accept Date RR Date Rig Type HES Frac Equipment FAUR, DAN,Wells Supervisor 6/12/2025 00:00 6/12/2025 23:59 FRAC HES 765 FERGUSON, SID,Wells Supervisor 6/12/2025 14:30 6/12/2025 21:00 SLICK LINE HES Frac Equipment FAUR, DAN,Wells Supervisor 6/13/2025 00:00 6/13/2025 23:59 FRAC HES 765 FERGUSON, SID,Wells Supervisor 6/13/2025 05:30 6/13/2025 22:15 SLICK LINE LRS 74-H FAUR, DAN,Wells Supervisor 6/14/2025 05:30 6/14/2025 13:00 PUMPING Page 2/2 3T-613 Report Printed: 7/9/2025 Daily STIM Report ORIG SPUD DATE: [ 5/4/2025 ] DRLG RIG RELEASE: [ 6/5/2025 ] CMPLT JOB START [ 6/12/2025 ] ON PRODUCTION: [ ] DAYS FROM SPUD: [ 48.70 ] REPORT # [ 12] REPORT DATE: [ 6/21/2025] Contractor Rig Name/# Rig Supervisor Rig Accept Date RR Date Rig Type HES Frac Equipment FAUR, DAN,Wells Supervisor 6/15/2025 00:00 6/15/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 6/16/2025 00:00 6/16/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 6/17/2025 00:00 6/17/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 6/18/2025 00:00 6/18/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/19/2025 00:00 6/19/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/20/2025 00:00 6/20/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/21/2025 00:00 6/21/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/22/2025 00:00 6/22/2025 19:00 FRAC HES 765 ROGERS, BRENT,Wells Supervisor 6/23/2025 05:30 6/23/2025 19:45 SLICK LINE HES 765 ROGERS, BRENT,Wells Supervisor 6/24/2025 05:30 6/24/2025 12:30 SLICK LINE AES DHD RICHWINE, BRUCE,DHD Field Supervisor 6/26/2025 06:00 6/26/2025 18:00 WELL INTEGRITY HES 046 ROGERS, BRENT,Wells Supervisor 6/27/2025 05:30 6/27/2025 19:30 SLICK LINE Offline Activities Type Subtype Des Start Date End Date PUMPING 38 6/12/2025 14:30 6/12/2025 20:00 PUMPING 38 6/13/2025 07:30 6/18/2025 20:00 PUMPING 38 6/23/2025 08:00 6/24/2025 12:30 PUMPING 66 6/27/2025 07:00 6/27/2025 18:00 Stimulation Intervals Interval Number Start Date End Date Top (ftKB) Btm (ftKB) Proppant Designed (lb) Proppant Total (lb) Volume Clean Total (bbl) Volume Slurry Total (bbl) 20 6/21/2025 09:15 6/21/2025 13:25 13,859.4 13,863.7 203,000.0 202,999.0 3,569.98 3,785.61 21 6/21/2025 13:25 6/21/2025 15:18 13,361.0 13,365.4 51,500.0 58,196.0 1,482.48 1,544.27 Page 1/1 3T-613 Report Printed: 7/9/2025 Daily STIM Report ORIG SPUD DATE: [ 5/4/2025 ] DRLG RIG RELEASE: [ 6/5/2025 ] CMPLT JOB START [ 6/12/2025 ] ON PRODUCTION: [ ] DAYS FROM SPUD: [ 49.49 ] REPORT # [ 13] REPORT DATE: [ 6/22/2025] API / UWI 5010320914 Original KB/RT Elevation (ft) 51.00 Ground Elevation (ft) 12.00 Original Spud Date 5/4/2025 Job Category COMPLETIONS Primary Job Type INITIAL COMPLETION Total AFE (Cost) 7,944,313.57 AFE / RFE / Maint.# GKA.00044.E.W007.CO.I S;GKA.00044.E.W007.C O.IF;GKA.00044.E.W007. CO.IW Network/Order Number 11005807;11005806;1100 5808 AFE+Supp Amt (Cost) 7,944,313.57 Daily Cost Total (Cost) 187,092.26 Cumulative Cost (Cost) 5,753,692.95 Weather Temperature (°F) Road Condition Wind Last 24hr Summary CONTINUE RIGGING DOWN, START EQUIPMENT MOVEMENT TO 2S 24hr Forecast General Remarks ZX Code ZX02 Fracturing Contact Name Title Mobile CAMPBELL, JAMES Frac Supervisor 661-203-1472 LAWSON, JACOB Supervisor 971-606-0075 Time Log Start Time Dur (hr) Phase Activity Code Time P-T-X Operation Start Depth (ftKB) End Depth (ftKB) 00:00 7.00 COMPZN, STIM DMOB P CONTINUE RIGGING EQUIPMENT DOWN, TRANSPORT RIG MATS TO 2S, EVACUATING TANK FARM, 07:00 5.00 COMPZN, STIM DMOB P COMPLETE RIGGING IRON DOWN, START STAGING EQUIPMENT FOR MOVE, BROKE DOWN NEEDED TANKS 12:00 7.00 COMPZN, STIM DMOB P HAUL PROPPANT DEBRIS TO DUMP. START EQUIPMENT MOVE OFF PAD, CHEM INVENTORY, MOVE OFF PAD Report Fluids Summary Fluid To well (bbl) Cum to Well (bbl) DIESEL 254.0 FRAC FLUID 43,570.0 Contractor Rig Name/# Rig Supervisor Rig Accept Date RR Date Rig Type HES Frac Equipment FAUR, DAN,Wells Supervisor 6/12/2025 00:00 6/12/2025 23:59 FRAC HES 765 FERGUSON, SID,Wells Supervisor 6/12/2025 14:30 6/12/2025 21:00 SLICK LINE HES Frac Equipment FAUR, DAN,Wells Supervisor 6/13/2025 00:00 6/13/2025 23:59 FRAC HES 765 FERGUSON, SID,Wells Supervisor 6/13/2025 05:30 6/13/2025 22:15 SLICK LINE LRS 74-H FAUR, DAN,Wells Supervisor 6/14/2025 05:30 6/14/2025 13:00 PUMPING HES Frac Equipment FAUR, DAN,Wells Supervisor 6/15/2025 00:00 6/15/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 6/16/2025 00:00 6/16/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 6/17/2025 00:00 6/17/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 6/18/2025 00:00 6/18/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/19/2025 00:00 6/19/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/20/2025 00:00 6/20/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/21/2025 00:00 6/21/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/22/2025 00:00 6/22/2025 19:00 FRAC HES 765 ROGERS, BRENT,Wells Supervisor 6/23/2025 05:30 6/23/2025 19:45 SLICK LINE HES 765 ROGERS, BRENT,Wells Supervisor 6/24/2025 05:30 6/24/2025 12:30 SLICK LINE AES DHD RICHWINE, BRUCE,DHD Field Supervisor 6/26/2025 06:00 6/26/2025 18:00 WELL INTEGRITY HES 046 ROGERS, BRENT,Wells Supervisor 6/27/2025 05:30 6/27/2025 19:30 SLICK LINE Offline Activities Type Subtype Des Start Date End Date PUMPING 38 6/12/2025 14:30 6/12/2025 20:00 PUMPING 38 6/13/2025 07:30 6/18/2025 20:00 PUMPING 38 6/23/2025 08:00 6/24/2025 12:30 PUMPING 66 6/27/2025 07:00 6/27/2025 18:00 Page 1/2 3T-613 Report Printed: 7/9/2025 Daily STIM Report ORIG SPUD DATE: [ 5/4/2025 ] DRLG RIG RELEASE: [ 6/5/2025 ] CMPLT JOB START [ 6/12/2025 ] ON PRODUCTION: [ ] DAYS FROM SPUD: [ 50.52 ] REPORT # [ 14] REPORT DATE: [ 6/23/2025] API / UWI 5010320914 Original KB/RT Elevation (ft) 51.00 Ground Elevation (ft) 12.00 Original Spud Date 5/4/2025 Job Category COMPLETIONS Primary Job Type INITIAL COMPLETION Total AFE (Cost) 7,944,313.57 AFE / RFE / Maint.# GKA.00044.E.W007.CO.I S;GKA.00044.E.W007.C O.IF;GKA.00044.E.W007. CO.IW Network/Order Number 11005807;11005806;1100 5808 AFE+Supp Amt (Cost) 7,944,313.57 Daily Cost Total (Cost) Cumulative Cost (Cost) 5,753,692.95 Weather Temperature (°F) Road Condition Wind Last 24hr Summary BRUSH & FLUSH TBG DWN TO 4031' RKB , DRIFT W/ DMY 3.78'' RBP TO 3800' RKB , SET 3.76'' QUADCO P2P RBP MID-ELEMENT @ 3410' RKB , OBTAIN PASSING 2500 PSI MITT , OBTAIN PASSING 0 PSI DDT. JOB IN PROGRESS 24hr Forecast General Remarks INITIAL T/I/O=450/ VAC / 325 FINAL T/I/O=0 / VAC / 325 ZX Code ZX72 Secure / Unsecure Well Contact Name Title Mobile ORNDORFF, JAMES SLICKLINE SUPERVISOR Time Log Start Time Dur (hr) Phase Activity Code Time P-T-X Operation Start Depth (ftKB) End Depth (ftKB) 05:30 1.50 TRAV P HAL MEETING, MEET W/ CWG, GRAB WELL FILE, SYNC CPU, CONTACT DSO, TRVL TO 3T-613 07:00 2.00 WOCP P ARRIVE , SIGN IN @ SIMOPS SHACK, PJSM , WAIT ON DSM & CRANE TO MOVE WELL HOUSE *** START TICKET @ 0800 *** 09:00 1.25 RURD P SPOT EQUIP , MU 6.5 SECTION LUB , RU .125'' WIRE & 2.125'' RLLR TS= RS , QC , 5' , QC , KJ , 5' , QC , OJS , QC , KJ , LSS ( OAL 28' ) 10:15 1.00 SLKL P PT W/ LRS TO 3000 PSI , RIH W/ QC , 3' x 1.875'' WB , BLB , 3.79'' G. RING , BOL LRS, BRUSH TUBING DOWN TO 4000' SLM, MULTIPLE PASSES TO 3100' SLM, PUMPED 28 BBLS, POOH 11:15 1.50 SLKL P PT W/ LRS TO SAME , RIH W/ QC , 3.78'' DMY RBP DRIFT , BOL LRS 22 BBLS , DRIFT DWN TO 3770' SLM , POOH 12:45 1.25 SLKL P SWAP TO 2.625'' RLLR TS= RS, QC ,5' , QC , KJ , 5' , LSS ( OAL 23' ) PT W/ LRS TO 3000PSI , ZERO BTM OF SPANGS , RIH W/ QC , KJ , 4.5'' OMK & 7'' EXT , 1.40'' LIB , LOC & SD @ 3301' SLM/ 3331' RKB, FLAG WIRE, POOH 14:00 2.50 SLKL P PT W/ LRS TO 3000PSI , RIH W/ QC , 4.5'' GR & BAITED , XO , 2.75'' DPU W/ 3.76'' QUADCO RBP ( OAL 8' ) , STOP @ 3366' SLM/ 3397' RKB, SET RBP , POOH INSTALL TREE CAP 16:30 2.00 SLKL P LRS START 2500 PSI MITT , FAILS FIRST 15MINS TBG DWN 2550PSI TO 2350PSI , BUMP PRESSURE UP , STARTING T/IA/OA = 2600 / 0 / 350 , 15 MINS T/IA/OA = 2525 / 0/ 350 , 30 MINS = 2500 / 0/ 350 ( PASS ) , BLEED TBG TO 0 PSI , 18:30 0.50 RURD P LDFN , SECURE WELL , PJSM , CONTACT DSO *** END TICKET @ 1800 *** 19:00 0.75 TRAV P TRV TO F-WING , SYNC CPU / TURN IN WELL FILE Report Fluids Summary Fluid To well (bbl) Cum to Well (bbl) DIESEL 55.0 309.0 FRAC FLUID 43,570.0 Contractor Rig Name/# Rig Supervisor Rig Accept Date RR Date Rig Type HES Frac Equipment FAUR, DAN,Wells Supervisor 6/12/2025 00:00 6/12/2025 23:59 FRAC HES 765 FERGUSON, SID,Wells Supervisor 6/12/2025 14:30 6/12/2025 21:00 SLICK LINE HES Frac Equipment FAUR, DAN,Wells Supervisor 6/13/2025 00:00 6/13/2025 23:59 FRAC HES 765 FERGUSON, SID,Wells Supervisor 6/13/2025 05:30 6/13/2025 22:15 SLICK LINE LRS 74-H FAUR, DAN,Wells Supervisor 6/14/2025 05:30 6/14/2025 13:00 PUMPING HES Frac Equipment FAUR, DAN,Wells Supervisor 6/15/2025 00:00 6/15/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 6/16/2025 00:00 6/16/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 6/17/2025 00:00 6/17/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 6/18/2025 00:00 6/18/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/19/2025 00:00 6/19/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/20/2025 00:00 6/20/2025 23:59 FRAC Page 2/2 3T-613 Report Printed: 7/9/2025 Daily STIM Report ORIG SPUD DATE: [ 5/4/2025 ] DRLG RIG RELEASE: [ 6/5/2025 ] CMPLT JOB START [ 6/12/2025 ] ON PRODUCTION: [ ] DAYS FROM SPUD: [ 50.52 ] REPORT # [ 14] REPORT DATE: [ 6/23/2025] Contractor Rig Name/# Rig Supervisor Rig Accept Date RR Date Rig Type HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/21/2025 00:00 6/21/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/22/2025 00:00 6/22/2025 19:00 FRAC HES 765 ROGERS, BRENT,Wells Supervisor 6/23/2025 05:30 6/23/2025 19:45 SLICK LINE HES 765 ROGERS, BRENT,Wells Supervisor 6/24/2025 05:30 6/24/2025 12:30 SLICK LINE AES DHD RICHWINE, BRUCE,DHD Field Supervisor 6/26/2025 06:00 6/26/2025 18:00 WELL INTEGRITY HES 046 ROGERS, BRENT,Wells Supervisor 6/27/2025 05:30 6/27/2025 19:30 SLICK LINE Offline Activities Type Subtype Des Start Date End Date PUMPING 38 6/12/2025 14:30 6/12/2025 20:00 PUMPING 38 6/13/2025 07:30 6/18/2025 20:00 PUMPING 38 6/23/2025 08:00 6/24/2025 12:30 PUMPING 66 6/27/2025 07:00 6/27/2025 18:00 Page 1/2 3T-613 Report Printed: 7/9/2025 Daily STIM Report ORIG SPUD DATE: [ 5/4/2025 ] DRLG RIG RELEASE: [ 6/5/2025 ] CMPLT JOB START [ 6/12/2025 ] ON PRODUCTION: [ ] DAYS FROM SPUD: [ 51.22 ] REPORT # [ 15] REPORT DATE: [ 6/24/2025] API / UWI 5010320914 Original KB/RT Elevation (ft) 51.00 Ground Elevation (ft) 12.00 Original Spud Date 5/4/2025 Job Category COMPLETIONS Primary Job Type INITIAL COMPLETION Total AFE (Cost) 7,944,313.57 AFE / RFE / Maint.# GKA.00044.E.W007.CO.I S;GKA.00044.E.W007.C O.IF;GKA.00044.E.W007. CO.IW Network/Order Number 11005807;11005806;1100 5808 AFE+Supp Amt (Cost) 7,944,313.57 Daily Cost Total (Cost) Cumulative Cost (Cost) 5,753,692.95 Weather Temperature (°F) Road Condition Wind Last 24hr Summary SET 3.78'' CATCHER/ P2P STINGER ASSEMBLY ON TOP OF P2P PACKER @ 3410' RKB , PULLED 1'' INCONEL BTM LATCH DMY VLV ( MODERATE EROSION ) FROM ST # 1 @ 2313' RKB . READY FOR DHD 24hr Forecast General Remarks INITIAL T/I/O=0/0/325 FINAL T/I/O=0/0/325 ZX Code ZX72 Secure / Unsecure Well Contact Name Title Mobile ORNDORFF, JAMES SLICKLINE SUPERVISOR Time Log Start Time Dur (hr) Phase Activity Code Time P-T-X Operation Start Depth (ftKB) End Depth (ftKB) 05:30 1.25 TRAV P HAL MEETING, MEET W/ CWG, GRAB WELL FILE, SYNC CPU, CONTACT DSO, TRVL TO 3T-613 06:45 1.00 RURD P ARRIVE, SIGN IN @ SIMOPS SHACK, PJSM, RU .125'' WIRE & 2.625'' RLLR TS= RS , QC , 5' , QC , KJ , 5' , QC , KJ , LSS ( OAL 23' ) *** START TICKET @ 0800 *** 07:45 1.00 SLKL P PT W/ LRS TO 3000PSI , RIH W/ QC , 4.5'' GS & 3.78'' CATCHER / P2P STINGER ( OAL 51'' ) , SD @ 3379, TAP DOWN, SHEAR OFF, POOH 08:45 1.00 SLKL P PT W/ LRS TO SAME , RIH W/ QC , KJ , 4.5'' OMK & 1.25'' JD , LOCATE, UNABLE TO SIT DOWN, POOH 09:45 1.00 SLKL P PT W/ LRS TO SAME, RIH W/ QC , 4.5'' OK -6 & 1.25'' JD , SD ST # 1 @2285' SLM ( 2313' RKB ), HIT 1 OJ LICK, SIT BACK DOWN, PU FREELY, POOH, OOH W/ VLV 10:45 1.00 RURD P RDMO , SECURE WELL , PJSM , CONTACT DSO 11:45 0.75 TRAV P TRV TO 1B-04 *** END TICKET @ 1300 *** Report Fluids Summary Fluid To well (bbl) Cum to Well (bbl) DIESEL 309.0 FRAC FLUID 43,570.0 Contractor Rig Name/# Rig Supervisor Rig Accept Date RR Date Rig Type HES Frac Equipment FAUR, DAN,Wells Supervisor 6/12/2025 00:00 6/12/2025 23:59 FRAC HES 765 FERGUSON, SID,Wells Supervisor 6/12/2025 14:30 6/12/2025 21:00 SLICK LINE HES Frac Equipment FAUR, DAN,Wells Supervisor 6/13/2025 00:00 6/13/2025 23:59 FRAC HES 765 FERGUSON, SID,Wells Supervisor 6/13/2025 05:30 6/13/2025 22:15 SLICK LINE LRS 74-H FAUR, DAN,Wells Supervisor 6/14/2025 05:30 6/14/2025 13:00 PUMPING HES Frac Equipment FAUR, DAN,Wells Supervisor 6/15/2025 00:00 6/15/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 6/16/2025 00:00 6/16/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 6/17/2025 00:00 6/17/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 6/18/2025 00:00 6/18/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/19/2025 00:00 6/19/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/20/2025 00:00 6/20/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/21/2025 00:00 6/21/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/22/2025 00:00 6/22/2025 19:00 FRAC HES 765 ROGERS, BRENT,Wells Supervisor 6/23/2025 05:30 6/23/2025 19:45 SLICK LINE HES 765 ROGERS, BRENT,Wells Supervisor 6/24/2025 05:30 6/24/2025 12:30 SLICK LINE AES DHD RICHWINE, BRUCE,DHD Field Supervisor 6/26/2025 06:00 6/26/2025 18:00 WELL INTEGRITY HES 046 ROGERS, BRENT,Wells Supervisor 6/27/2025 05:30 6/27/2025 19:30 SLICK LINE Offline Activities Type Subtype Des Start Date End Date PUMPING 38 6/12/2025 14:30 6/12/2025 20:00 PUMPING 38 6/13/2025 07:30 6/18/2025 20:00 Page 2/2 3T-613 Report Printed: 7/9/2025 Daily STIM Report ORIG SPUD DATE: [ 5/4/2025 ] DRLG RIG RELEASE: [ 6/5/2025 ] CMPLT JOB START [ 6/12/2025 ] ON PRODUCTION: [ ] DAYS FROM SPUD: [ 51.22 ] REPORT # [ 15] REPORT DATE: [ 6/24/2025] Offline Activities Type Subtype Des Start Date End Date PUMPING 38 6/23/2025 08:00 6/24/2025 12:30 PUMPING 66 6/27/2025 07:00 6/27/2025 18:00 Page 1/2 3T-613 Report Printed: 7/9/2025 Daily STIM Report ORIG SPUD DATE: [ 5/4/2025 ] DRLG RIG RELEASE: [ 6/5/2025 ] CMPLT JOB START [ 6/12/2025 ] ON PRODUCTION: [ ] DAYS FROM SPUD: [ 53.45 ] REPORT # [ 16] REPORT DATE: [ 6/26/2025] API / UWI 5010320914 Original KB/RT Elevation (ft) 51.00 Ground Elevation (ft) 12.00 Original Spud Date 5/4/2025 Job Category COMPLETIONS Primary Job Type INITIAL COMPLETION Total AFE (Cost) 7,944,313.57 AFE / RFE / Maint.# GKA.00044.E.W007.CO.I S;GKA.00044.E.W007.C O.IF;GKA.00044.E.W007. CO.IW Network/Order Number 11005807;11005806;1100 5808 AFE+Supp Amt (Cost) 7,944,313.57 Daily Cost Total (Cost) Cumulative Cost (Cost) 5,753,692.95 Weather Temperature (°F) Road Condition Wind Last 24hr Summary (MISC)TEST BPV TO 1520 PSI (PASSED), T POT (PASSED), SWAP FRAC TREE TO 5K PRODUCTION TREE (COMPLETE), SHELL TEST PRODUCTION TREE TO 5K (PASSED) 24hr Forecast General Remarks Initial T/I/O = SI Vac/Vac/300 Final T/I/O = SI 0/0/300 ZX Code ZX08 Ann-Comm Evaluation / Leak Detection Contact Name Title Mobile KIRK, JAMES DHD Tech 832-540-0631 AREND,GRANT DHD Tech N/A Time Log Start Time Dur (hr) Phase Activity Code Time P-T-X Operation Start Depth (ftKB) End Depth (ftKB) 06:00 1.00 TRAV P Travel from KOC to 3T-613 07:00 0.25 RURD P R/u manifold & gauges 07:15 9.50 DHD P (MISC)TEST BPV TO 1520 PSI (PASSED), T POT (PASSED), SWAP FRAC TREE TO 5K PRODUCTION TREE (COMPLETE), SHELL TEST PRODUCTION TREE TO 5K (PASSED) Initial T/I/O = SI Vac/Vac/300, T & IA FL NS. Stung into T PO w/ 0 psi. Valve crew & crane on location Valve crew set BPV in frac tree, pressured IA to 1520 psi w/ 0.8 bbls diesel to test under BPV. Start T/I/O = 0/1520/425 15 min = 0/1491/425 (-29) 30 min = 0/1481/163 (-10) No pressure on T PO during BPV test. Bled IA to 0 psi (fluid) in 5 min, Held IA open. Tree evacuated of fluid to BPV. Rig up crane and remove Frac tree. Install cross over and 5k production tree. (new BX-155 & R-39 gaskets) SI IA open bleed. Valve crew removed BPV and set 2 way check. Shell test 5k production tree to 5000 psi Monitor for 15 min No external leaks, bleed tree to 0 psi. Valve crew remove 2 way check. Final T/I/O = SI 0/0/300 16:45 0.25 RURD P R/d manifold & gauges 17:00 1.00 TRAV P Travel to KOC Report Fluids Summary Fluid To well (bbl) Cum to Well (bbl) DIESEL 309.0 FRAC FLUID 43,570.0 Contractor Rig Name/# Rig Supervisor Rig Accept Date RR Date Rig Type HES Frac Equipment FAUR, DAN,Wells Supervisor 6/12/2025 00:00 6/12/2025 23:59 FRAC HES 765 FERGUSON, SID,Wells Supervisor 6/12/2025 14:30 6/12/2025 21:00 SLICK LINE HES Frac Equipment FAUR, DAN,Wells Supervisor 6/13/2025 00:00 6/13/2025 23:59 FRAC HES 765 FERGUSON, SID,Wells Supervisor 6/13/2025 05:30 6/13/2025 22:15 SLICK LINE LRS 74-H FAUR, DAN,Wells Supervisor 6/14/2025 05:30 6/14/2025 13:00 PUMPING HES Frac Equipment FAUR, DAN,Wells Supervisor 6/15/2025 00:00 6/15/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 6/16/2025 00:00 6/16/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 6/17/2025 00:00 6/17/2025 23:59 FRAC Page 2/2 3T-613 Report Printed: 7/9/2025 Daily STIM Report ORIG SPUD DATE: [ 5/4/2025 ] DRLG RIG RELEASE: [ 6/5/2025 ] CMPLT JOB START [ 6/12/2025 ] ON PRODUCTION: [ ] DAYS FROM SPUD: [ 53.45 ] REPORT # [ 16] REPORT DATE: [ 6/26/2025] Contractor Rig Name/# Rig Supervisor Rig Accept Date RR Date Rig Type HES Frac Equipment FAUR, DAN,Wells Supervisor 6/18/2025 00:00 6/18/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/19/2025 00:00 6/19/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/20/2025 00:00 6/20/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/21/2025 00:00 6/21/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/22/2025 00:00 6/22/2025 19:00 FRAC HES 765 ROGERS, BRENT,Wells Supervisor 6/23/2025 05:30 6/23/2025 19:45 SLICK LINE HES 765 ROGERS, BRENT,Wells Supervisor 6/24/2025 05:30 6/24/2025 12:30 SLICK LINE AES DHD RICHWINE, BRUCE,DHD Field Supervisor 6/26/2025 06:00 6/26/2025 18:00 WELL INTEGRITY HES 046 ROGERS, BRENT,Wells Supervisor 6/27/2025 05:30 6/27/2025 19:30 SLICK LINE Offline Activities Type Subtype Des Start Date End Date PUMPING 38 6/12/2025 14:30 6/12/2025 20:00 PUMPING 38 6/13/2025 07:30 6/18/2025 20:00 PUMPING 38 6/23/2025 08:00 6/24/2025 12:30 PUMPING 66 6/27/2025 07:00 6/27/2025 18:00 Page 1/2 3T-613 Report Printed: 7/9/2025 Daily STIM Report ORIG SPUD DATE: [ 5/4/2025 ] DRLG RIG RELEASE: [ 6/5/2025 ] CMPLT JOB START [ 6/12/2025 ] ON PRODUCTION: [ ] DAYS FROM SPUD: [ 54.51 ] REPORT # [ 17] REPORT DATE: [ 6/27/2025] API / UWI 5010320914 Original KB/RT Elevation (ft) 51.00 Ground Elevation (ft) 12.00 Original Spud Date 5/4/2025 Job Category COMPLETIONS Primary Job Type INITIAL COMPLETION Total AFE (Cost) 7,944,313.57 AFE / RFE / Maint.# GKA.00044.E.W007.CO.I S;GKA.00044.E.W007.C O.IF;GKA.00044.E.W007. CO.IW Network/Order Number 11005807;11005806;1100 5808 AFE+Supp Amt (Cost) 7,944,313.57 Daily Cost Total (Cost) Cumulative Cost (Cost) 5,753,692.95 Weather Temperature (°F) Road Condition Wind Last 24hr Summary SET 1'' LGLV (PORT= 1/4'', TRO= 1320) IN ST#1 @ 2331' RKB, PULL 1'' DMY IN ST#2 @ 3331' RKB, SET 1'' OV (PORT= 5/16'') IN ST#2 @ 3331' RKB, LRS PERFORM MIT-T TO 1500 PSI (GOOD MIT-T), PULL CATCHER @ 3402' RKB, PULL RBP @ 3407' RKB, READY FOR COIL. 24hr Forecast General Remarks INITIAL T/I/O 0/0/325 FINAL T/I/O 500/50/325 ZX Code ZX50 Slickline / DSL Misc. (or Multiple Operations Contact Name Title Mobile BUQUET, JONATHAN Slickline Operator 985-232-2439 Time Log Start Time Dur (hr) Phase Activity Code Time P-T-X Operation Start Depth (ftKB) End Depth (ftKB) 05:30 1.50 SLKL P HAL MEETING, MEET W/ CWG, GRAB WELL FILE, SYNC CPU, CONTACT DSO, TRVL TO 3T-613 w/ EQUIPMENT 07:00 1.25 RURD P ARRIVE, SIGN IN @ SIMOPS SHACK, SPOT IN EQUIPMENT, PJSM, RU .125'' WIRE & 2.625'' RLLR TS= RS , QC , 5' , QC , KJ , 5' , QC , KJ , LSS ( OAL 23' ), PT w/ LRS= 250L / 2500H, INSTALL FUSIBLE, NOTIFY DSO, ***START TICKET @ 08:00*** 08:15 1.25 SLKL P RIH w/ QC, KJ, 4-1/2 OK-1, JK R/T, 1'' LGLV (PORT= 1/4'', TRO= 1320), SET IN ST#1 @ 2282' SLM / 2331' RKB, PRESSURE UP ON TUBING TO 1000 PSI, SHEAR OFF, POOH 09:30 1.25 SLKL P RIH w/ QC, KJ, 4-1/2 BLB, QC, 4-1/2 OMK-1, 1-1/4 JDC (steel), LATCH & PULL 1'' DMY IN ST#2 @ 3305' SLM / 3331' RKB, POOH 10:45 1.25 SLKL P RIH w/ QC, KJ, 4-1/2 OK-1, JK R/T, 1'' OV (PORT= 5/16''), SET IN ST#2 @ 3305' SLM / 3331' RKB, PRESSURE UP ON TUBING TO 1000 PSI, SHEAR OFF, POOH 12:00 1.25 SLKL P LRS PERFORM MIT-T TO 1500 PSI (GOOD MIT-T), RIH w/ QC, 4-1/2 GR (steel), LATCH & PULL CATCHER @ 3371' SLM / 3402' RKB, POOH PRE MIT T/I/O 1000/50/340 INITIAL T/I/O 1525/50/340 15 MIN T/I/O 1460/50/340 30 MIN T/I/O 1450/50/340 13:15 1.00 SLKL P RIH w/ QC, 2.79'' CENT, 4-1/2 RBP EQ PRONG, PRESSURE UP ON TUBING TO 1000 PSI, EQUALIZE RBP @ 3376' SLM, 3407' RKB, 14:15 3.25 SLKL P RIH w/ QC, 4-1/2 GR (steel), 4-1/2 TTS P/T, LATCH RBP @ 3376' SLM / 3407' RKB, JAR @ 1500# FOR 1 HR CAME FREE, LET RELAX 30 MINS, POOH, STILL PULLING HEAVY LET RELAX 30 MINS, POOH, ***END TIME @ 18:00*** 17:30 1.00 RURD P R/D LRS & HES, SECURE WELL, TREE CAP PT'd, FUSIBLE REMOVED, NOTIFY DSO, TRAVEL w/ EQUIPMENT, STAGE ON EDGE OF 3S-PAD 18:30 1.00 TRAV P TRAVEL TO F-WING, STOP & RETURN TOOLS @ WLB, RETURN WELL FILE, SYNC CPU Report Fluids Summary Fluid To well (bbl) Cum to Well (bbl) DIESEL 5.0 314.0 FRAC FLUID 43,570.0 Contractor Rig Name/# Rig Supervisor Rig Accept Date RR Date Rig Type HES Frac Equipment FAUR, DAN,Wells Supervisor 6/12/2025 00:00 6/12/2025 23:59 FRAC HES 765 FERGUSON, SID,Wells Supervisor 6/12/2025 14:30 6/12/2025 21:00 SLICK LINE HES Frac Equipment FAUR, DAN,Wells Supervisor 6/13/2025 00:00 6/13/2025 23:59 FRAC HES 765 FERGUSON, SID,Wells Supervisor 6/13/2025 05:30 6/13/2025 22:15 SLICK LINE LRS 74-H FAUR, DAN,Wells Supervisor 6/14/2025 05:30 6/14/2025 13:00 PUMPING HES Frac Equipment FAUR, DAN,Wells Supervisor 6/15/2025 00:00 6/15/2025 23:59 FRAC Page 2/2 3T-613 Report Printed: 7/9/2025 Daily STIM Report ORIG SPUD DATE: [ 5/4/2025 ] DRLG RIG RELEASE: [ 6/5/2025 ] CMPLT JOB START [ 6/12/2025 ] ON PRODUCTION: [ ] DAYS FROM SPUD: [ 54.51 ] REPORT # [ 17] REPORT DATE: [ 6/27/2025] Contractor Rig Name/# Rig Supervisor Rig Accept Date RR Date Rig Type HES Frac Equipment FAUR, DAN,Wells Supervisor 6/16/2025 00:00 6/16/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 6/17/2025 00:00 6/17/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 6/18/2025 00:00 6/18/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/19/2025 00:00 6/19/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/20/2025 00:00 6/20/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/21/2025 00:00 6/21/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 6/22/2025 00:00 6/22/2025 19:00 FRAC HES 765 ROGERS, BRENT,Wells Supervisor 6/23/2025 05:30 6/23/2025 19:45 SLICK LINE HES 765 ROGERS, BRENT,Wells Supervisor 6/24/2025 05:30 6/24/2025 12:30 SLICK LINE AES DHD RICHWINE, BRUCE,DHD Field Supervisor 6/26/2025 06:00 6/26/2025 18:00 WELL INTEGRITY HES 046 ROGERS, BRENT,Wells Supervisor 6/27/2025 05:30 6/27/2025 19:30 SLICK LINE Offline Activities Type Subtype Des Start Date End Date PUMPING 38 6/12/2025 14:30 6/12/2025 20:00 PUMPING 38 6/13/2025 07:30 6/18/2025 20:00 PUMPING 38 6/23/2025 08:00 6/24/2025 12:30 PUMPING 66 6/27/2025 07:00 6/27/2025 18:00 1. Type of Request:Abandon Plug Perforations Fracture Stimulate Repair Well Operations shutdown Suspend Perforate Other Stimulate Pull Tubing Change Approved Program Plug for Redrill Perforate New Pool Re-enter Susp Well Alter Casing Other: ___________________ 2. Operator Name:4. Current Well Class: 5. Permit to Drill Number: Exploratory Development 3. Address:Stratigraphic Service 6. API Number: 7. If perforating:8. Well Name and Number: What Regulation or Conservation Order governs well spacing in this pool?KRU 3T-613 Yes No 9. Property Designation (Lease Number):10. Field: Torok Oil Pool 11. Total Depth MD (ft):Total Depth TVD (ft): Effective Depth MD: Effective Depth TVD: Junk (MD): 23631 5031 23618 5031 2290 None None Casing Collapse Structural Conductor Surface 2470 Intermediate 4790 Intermediate 7850 Liner 9210 Packers and SSSV Type:Packers and SSSV MD (ft) and TVD (ft): 12. Attachments:Proposal Summary Wellbore schematic 13. Well Class after proposed work: Detailed Operations Program BOP Sketch Exploratory Stratigraphic Development Service 14. Estimated Date for 15. Well Status after proposed work: Commencing Operations:OIL WINJ WDSPL Suspended 16. Verbal Approval:Date: GAS WAG GSTOR SPLUG AOGCC Representative: GINJ Op Shutdown Abandoned Contact Name:Manabu Nozaki Manabu Nozaki Contact Email:Manabu.Nozaki@cop.com Contact Phone:907-265-6519 Authorized Title:Staff Completions Engineer Conditions of approval: Notify AOGCC so that a representative may witness Sundry Number: Plug Integrity BOP Test Mechanical Integrity Test Location Clearance Other Conditions of Approval: Post Initial Injection MIT Req'd? Yes No APPROVED BY Approved by: COMMISSIONER THE AOGCC Date: Comm. Comm. Sr Pet Eng Sr Pet Geo Sr Res Eng 1034 4-1/2" 6/12/2025 2361811161 4-1/2" 5031 Halliburton TNT Prod Packer Baker ZXP, No SSSV L-80 10860 Perforation Depth TVD (ft):Perforation Depth MD (ft): 49827-5/8" 20" 10-3/4" 80 7-5/8"11592 2400 12664 11630 MD PRESENT WELL CONDITION SUMMARY 6890 5210 119 2437 4740 119 2695 TVD Burst MPSP (psi):Plugs (MD): STATE OF ALASKA ALASKA OIL AND GAS CONSERVATION COMMISSION APPLICATION FOR SUNDRY APPROVALS 20 AAC 25.280 ADL025528 / ADL393883 / ADL 393884 225-036 P.O. Box 100360, Anchorage, Alaska 99510-0360 50-103-20914-00-00 ConocoPhillips Alaska Inc. Kuparuk Field Will perfs require a spacing exception due to property boundaries? Current Pools: Size Proposed Pools: 6/5/2025 Length AOGCC USE ONLY 11590 Tubing Grade:Tubing MD (ft): TNT Packer: 12349' MD / 4910' TVD ZXP: 12457' MD / 4936' TVD Subsequent Form Required: Suspension Expiration Date: 17. I hereby certify that the foregoing is true and the procedure approved herein will not be deviated from without prior written approval. Authorized Name and Digital Signature with Date: Tubing Size: m n P 2 6 5 6 t _ N Form 10-403 Revised 06/2023 Approved application valid for 12 months from date of approval.Submit PDF to aogcc.permitting@alaska.gov By Grace Christianson at 2:27 pm, Jun 05, 2025 325-345 10-404 6/12/2025 A.Dewhurst 06JUN25 CDW 06/06/2025 VTL 6/10/2025 DSR-6/12/25*&: Jessie L. Chmielowski Digitally signed by Jessie L. Chmielowski Date: 2025.06.12 11:49:20 -08'00' 06/12/25 RBDMS JSB 061625 SECTION 1 - AFFIDAVIT 10 AAC 25.283 (a)(1) Exhibit 1 is an affidavit stating that the owners, landowners, surface owners and operators within one-half mile radius of the current or proposed wellbore trajectory have been provided notice of operations in compliance with 20 AAC 25.283(a)(1). SECTION 2 – PLAT 20 AAC 25.283 (2)(A) Plat 1: Wells within 1/2 mile Table 1: Wells within 1/2 miles (2)(C) 3T-613 Frac Sundry Well - Wells within 1/2 Mile Buffer of Well Track Business Unit ID Business Area ID Field Name API * Well Name Status Symbology Well in Frac Port 1/2 mi Buffer Open Interval in Frac Port 1/2 mi Buffer KUP TOROK TOROK 501032077700 3S-612 ACTIVE Injector Miscible Water Alternating Gas KUP TOROK TOROK 501032084200 3S-625 ACTIVE Injector Produced Water KUP TOROK TOROK 501032086400 3S-617 ACTIVE Injector Produced Water KUP TOROK TOROK 501032088200 3T-621 ACTIVE Injector Produced Water KUP TOROK TOROK 501032089000 3T-608 ACTIVE Injector Produced Water KUP TOROK TOROK 501032089600 3T-612 ACTIVE Injector Produced Water Yes Yes KUP TOROK TOROK 501032084400 3S-615 ACTIVE Oil KUP TOROK TOROK 501032077400 3S-611 ACTIVE Oil KUP TOROK TOROK 501032087500 3S-610 ACTIVE Oil KUP TOROK TOROK 501032087800 3S-626 ACTIVE Oil KUP TOROK TOROK 501032088700 3T-603 ACTIVE Oil KUP TOROK TOROK 501032089900 3T-616 ACTIVE Oil Yes Yes KUP COYOTE COYOTE 501032090500 3T-731 ACTIVE Oil KUP COYOTE COYOTE 501032090700 3T-730 ACTIVE Oil NAK OU OOOGURUK UNIT 507032069200 ODSN-43 ACTIVE Oil NAK OU OOOGURUK UNIT 501032066070 NDST-02PB1 PA Plugged and Abandoned NAK NAK NORTH ALASKA EXPLORATION 501032064570 NUNA 1PB1 PA Plugged and Abandoned KUP TOROK TOROK 501032087870 3S-626PB1 PA Plugged and Abandoned KUP TOROK TOROK 501032089970 3T-616PB1 PROP Proposed Yes Yes KUP TOROK TOROK 501032089971 3T-616PB2 PROP Proposed NAK OU OOOGURUK UNIT 501032066000 NDST-02 SUSP Suspended NAK NAK NORTH ALASKA EXPLORATION 501032064500 NUNA 1 SUSP Suspended Yes - Suspended Yes - Suspended SECTION 3 – FRESHWATER AQUIFERS 20 AAC 25.283(a)(3) There are no freshwater aquifers or underground sources of drinking water within a one-half mile radius of the current or proposed wellbore trajectory. None as per Aquifer Exemption Title 40 CFR 147.102(b)(3), “That portions of the aquifers on the North Slope described by a ¼ mile area beyond and lying directly below the Kuparuk River Unit oil and gas producing field”. SECTION 4 – PLAN FOR BASELINE WATER SAMPLING FOR WATER WELLS 20 AAC 25.283(a)(4) There are no water wells located within one-half mile of the current or proposed wellbore trajectory and fracturing interval. A water well sampling plan is not applicable. SECTION 5 –DETAILED CEMENTING AND CASING INFORMATION 20 AAC 25.283(a)(5) All casing is cemented and tested in accordance with 20 AAC 25.030. See Wellbore schematic for casing details. Intermediate I Casing 7.625"29.7# L80 Hyd563 + 800' 33.7# P110S Hyd563 heavy heel 12664' MD / 4982' TVD Int 1 TOC 500' MD or 250' TVD above the Coyote 6545' MD /3536' TVD Surface Casing 10.75"45.5# L-80 Hyd563 2695’ MD / 2438' TVD Cemented to Surface Lead: 10.7ppg, Tail: 15.8ppg 20" 94# H40 Insulated Conductor 119’ MD/TVD Cemented to Surface Production TOL Liner Top Packer and Hanger Upper Completion 1. 2ea SLB (VanOil) Gas Lift Mandrel 2. HES Opsis Downhole Gauge 3. HES 7-5/8"x4-½” TNT Packer 4. Arsenal Glass Disk (to be shared during frac) 5. HES Self-Aligning Muleshoe with Baker Shear Locator Lower Completion 1. Baker ZXP Packer and Flex-V Lock Hanger 2. 21ea AU Sliding Sleeves 3. Alpha Sleeve (Disc #15) 4. Citadel MOAS Shoe 4.5"12.6# P110S Hyd563 23618 MD / 5031' TVD Cemented to Liner Top 3T-613 Moraine Producer Base Perm 1572' MD / 1539' TVD Top Torok Oil Pool (Moraine) 12620' MD / 4974' TVD Top Coyote 8916' MD / 4099' TVD (All TVDs are TVDRKBs) 6-1/2" Hole TD 23631 MD / 5031' TVD SECTION 6 – ASSESSMENT OF EACH CASING AND CEMENTING OPERATION TO BE PERFORMED TO CONSTRUCT OR REPAIR THE WELL 20 AAC 25.283(a)(6) Casing & Cement Assessments: The 10-3/4” casing cement report on 05/07/2025 was pumped with 408 barrels of 10.7 ppg lead cement and 57 barrels 15.8 ppg tail cement. This was displaced with 231 bbl 9.5 ppg spud mud. The plug bumped and the floats held. The 7-5/8” casing cement report on 05/18/2025 shows that the job was pumped as designed, indicating competent cementing operations. The cement job was pumped with 211 barrels of 14.0 ppg lead cement, followed with 59 barrels of 15.3 ppg tail cement. This was displaced with 568 barrels of 10.0 ppg RheGuard NAF. The plug bumped, pressure was bled off, and floats were confirmed to be holding. A cement bond log indicates competent cement with a cement top @ 6,545 MD (3,536’ TVD). The 4-1/2” liner cement report on 06/02/2025 shows the job was pumped as designed, indicating competent cementing operations. The cement job was pumped with 287 barrels of 13.5 ppg cement. The cement was displaced with 9.5 ppg CI NaCl brine and the plugs bumped and held for 5 minutes. Floats held. Summary All casing is cemented in accordance with 20 AAC 25.030 and each hydrocarbon zone penetrated by the well is isolated. Based on engineering evaluation of the wells referenced in this application, ConocoPhillips has determined that this well can be successfully fractured within its design limits. , @ 6,545 MD (3,536’TVD). SECTION 7 – PRESSURE TEST INFORMATION AND PLANS TO PRESSURE- TEST CASINGS AND TUBINGS INSTALLED IN THE WELL 20 AAC 25.283(a)(7) On 05/08/2025 the 10-3/4” casing was pressure tested to 1,975 psi for 30 minutes On 05/18/2025 the 7-5/8” casing was pressure tested to 4,000 psi for 30 minutes. On 06/04/2025 the 4-1/2” tubing was pressure tested to 4,200 psi. On 06/04/2025 The 7-5/8” casing by 4-1/2” tubing annulus was pressure tested to 3,850 psi. AOGCC Required Pressures [all in psi] Maximum Predicted Treating Pressure (MPTP) 7,050 Annulus pressure during frac 3,500 Annulus PRV setpoint during frac 3,600 7-5/8" Annulus pressure test 3,850 4-1/2" Tubing pressure Test 4,200 Electronic PRV 8,050 Highest pump trip 7,550 SECTION 8 – PRESSURE RATINGS AND SCHEMATICS FOR THE WELLBORE, WELLHEAD, BOPE AND TREATING HEAD 20 AAC 25.283(a)(8) Size Weight, ppf Grade API Burst, psi API Collapse, psi 10-3/4” 45.5 L-80 5,209 2474 7-5/8” 29.7 L-80 6,885 4,789 7-5/8” 33.7 P-110S 10,860 7,870 4-1/2” 12.6 L-80 8,430 7,500 Table 2: Wellbore pressure ratings Stimulation Surface Rig-Up Kuparuk 10K Frac Tree SECTION 9 – DATA FOR FRACTURING ZONE AND CONFINING ZONES 20 AAC 25.283(a)(9) CPAI has formed the opinion, based on seismic, well, and other subsurface information currently available that: The fracturing zone, the Torok Oil Pool, has an average thickness of approximately 219 ft TVD over the course of the lateral section of well 3T-613, from where it intersects the top formation at 12,620’ MD (5,049’ TVDSS) to the TD of the well. The Torok Oil Pool is comprised of thinly interbedded sandstone, siltstone, and silty shale layers. The sandstone and siltstone components are litharenites, moderately to well sorted, and very fine grained. The silty shales are composed of clay-rich, moderately to poorly sorted silt and clay. The estimated fracture pressure for the Moraine interval is approximately 12.5-13.5 ppg. The overlying confining interval of the Torok Formation consists of mudstones and siltstones with a thickness of approximately 815’ TVD along the 3T-613 trajectory. The top of the Torok confining interval in the well starts at 9210’ MD (5,040’ TVDSS). The estimated fracture gradient of the overlying Torok formation is approximately 0.82 psi/ft. The underlying confining zone below the Base Moraine consists of lower Torok, HRZ, and Kalubik shales totaling approximately 500’ TVD. The estimated fracture gradient for this section ranges from 15-18 ppg, with the gradient increasing down section. The Base Moraine is estimated from seismic to be at 5,200 ft TVDSS at the heel while it was intersected at 5,062 ft TVDSS in the toe portion of the well. The estimated formation pressure within the Torok Oil Pool is 2,285psi at a depth of 5,200’ TVDSS. SECTION 10 – LOCATION, ORIENTATION AND A REPORT ON MECHANICAL CONDITION OF EACH WELL THAT MAY TRANSECT CONFINING ZONE 20 AAC 25.283(a)(10) ConocoPhillips has formed the opinion, based on following assessments for each well and seismic, well, and other subsurface information currently available that none of these wells will interfere with containment of the hydraulic fracturing fluid within the one-half mile radius of the proposed wellbore trajectory. Casing & Cement assessments for all wells that transect the confining zone: 3T-612: The 7-5/8” casing cement report on 12/07/2024 shows that the job was pumped as designed, indicating competent cementing operations. The cement job was pumped with 98 barrels of 14.0 ppg lead cement, followed with 58 barrels of 15.3 ppg tail cement. This was displaced with 375 barrels of 9.5 ppg BaraECD NAF. The plug bumped, pressure was bled off, and floats were confirmed to be holding. A cement bond log indicates competent cement with a cement top @ 4,799 MD (3,489’ TVD). Source: 224-128 – Laserfiche WebLink 3T-616/3T-616 PB1: The 7-5/8” casing cement report on 01/24/2024 shows that the job was pumped as designed, indicating competent cementing operations. The cement job was pumped with 122 barrels of 14.0 ppg lead cement, followed with 58 barrels of 15.3 ppg tail cement. This was displaced with 415 barrels of 9.5 ppg BaraECD NAF. The plug bumped, pressure was bled off, and floats were confirmed to be holding. A cement bond log indicates competent cement with a cement top @ 5,041 MD (3,422’ TVD). The sidetrack for 3T-616 was made at 9371’ MD of the 3T-616 PB1 off of a cement plug placed at that point. Source: 224-138 – Laserfiche WebLink Nuna 1/Nuna 1PH: According to the Pioneer Natural Resources job log on the AOGCC website, the top plug was pumped in Nuna 1 PB1 on 2/10/2012. The top plug was pumped with 280 sx of Premium Cement. Firm cement was encountered at ~5766’. KOP for the Nuna 1 well is about 111’ MD (70’ TVDSS) below the base of the Coyote interval in Nuna 1 PH. According to the Pioneer Natural Resources job log on the AOGCC website, the 7-5/8” casing was cemented on 2/16/2012. The cement report indicates that the job was pumped with 192 sx 15.8ppg Class G cement. Partial returns were seen. Moraine interval is cement isolated in both wells, but the Coyote interval currently is not. Sundry Application 324-718 proposes perf and wash operations with squeeze perfs from 5,400’ to 5,550’ MD that would isolate the Coyote interval. The operation has not been started yet. Source: 221-155 – Laserfiche WebLink There is a chance to connect to the Nuna-1 wellbore at Frac Stage #21 (the distance along the max. horizonal stress orientation is ~320 ft). The past pressure testing done on Nuna-1 (1700 psi MIT on 12/17/2024) proved that the suspension plug can withstand the maximum fracture treatment pressure (4068 psi downhole; 1415 psi wellhead equivalent). Frac stage 21 is the last stage of the job. Prior to pumping Stage #21 we will pump half the pad volume and monitor Nuna 1. If no pressure communication is confirmed, we will proceed to pump a ~50,000 lb frac job at Stage #21 while continuing to monitor Nuna 1, if a pressure response is seen during the job we will go to flush. We don’t expect to achieve 1 lbs/sq-ft proppant concentration (the cutoff value used to calculate the fracture geometry). The map shows the distances. pjpp Moraine interval is cement isolated in both wells, but the ppg Coyote interval currently is not. There is a chance to connect to the Nuna-1 wellbore at Frac Stage #21 (the distance along the max. horizonal The past pressure testing done on Nuna-1 (1700 psi MIT on 12/17/2024) proved g( g stress orientation is ~320 ft).pp g ( p )p that the suspension plug can withstand the maximum fracture treatment pressure (4068 psi downhole; 1415 psi ) ppg p (p ;p wellhead equivalent). Frac stage 21 is the last stage of the job. Prior to pumping Stage #21 we will pump half q) g g jppgg pp the pad volume and monitor Nuna 1. If no pressure communication is confirmed, we will proceed to pump a pp,p pp ~50,000 lb frac job at Stage #21 while continuing to monitor Nuna 1, if a pressure response is seen during the ,jg g ,pp g job we will go to flush. We don’t expect to achieve 1 lbs/sq-ft proppant concentration (the cutoff value used tojgpqp calculate the fracture geometry). The map shows the distances. SECTION 11 – LOCATION OF, ORIENTATION OF AND GEOLOGICAL DATA FOR FAULTS AND FRACTURES THAT MAY TRANSECT THE CONFINING ZONES 20 AAC 25.283(a)(11) CPAI has formed the opinion, based on seismic, well, and other subsurface information currently available that three faults transect the Torok Oil Pool reservoir within one half mile radius of the 3T-613 wellbore trajectory. These faults all strike NE-SW and are shown in Plat 1. They intersect the 3T-613 well trajectory at 13,500’ MD (Fault 1), 17,141’ MD (Fault 2), and 18,023’ MD (Fault 3), respectively. All faults are upthrown on the northern side, between ~10-90ft. All faults encountered by the well are difficult to trace on the seismic data, due to a) lack of fine-scale resolution at the Torok Oil Pool level and b) lack of reflectivity in the overlying Torok shales, the result of the monotonous shaly lithology. Fault 2 is currently mapped to extend about 200ft into the Torok overburden, whereas faults 1 & 2 have the potential to penetrate through the overburden into the overlying hydrocarbon bearing Coyote Oil Pool. However, due to the shaly overburden and horizontal stress acting on the fault (interpreted to be 15.8 ppg at the fault’s mapped orientation) the presence of the fault will not interfere with containment. If there is any indication that a fracture has intersected any mapped fault (or any other faults unmapped to date) during fracturing operations, ConocoPhillips will go to flush and terminate the stage immediately. SECTION 12 – PROPOSED HYDRAULIC FRACTURING PROGRAM 20 AAC 25.283(a)(12) 3T-613 was completed in June 2025 as a horizontal producer in the Torok formation. The well is completed with a 4.5” tubing upper completion and a cemented 4.5” liner with a dart activated sliding sleeve lower completion. The first stage frac will be pumped through a toe initiator valve in the toe of the lateral. After the 1st stage, a dart will be dropped to shift open the 2nd stage sleeve and isolate the first stage. A frac will then be pumped through the 2nd stage. Darts will continue to be dropped to provide isolation from the previous stage and open each subsequent stage. Proposed Procedure: Halliburton Pumping Services: 1. Conduct Safety Meeting and Identify Hazards. Inspect Wellhead and Pad Condition to identify any pre- existing conditions. 2. Ensure the frac tree was tested to ~10,000 psi at rig. 3. Ensure all pre-frac well work has been completed and confirm the tubing and annulus are filled with a freeze protect fluid to 2,313’ MD / 2,170’ TVD. 4. Ensure the 10-403 Sundry has been reviewed and approved by the AOGCC. 5. MIRU 25 clean insulated Frac tanks (450 bbls usable volume per tank), with a berm surrounding the tanks that can hold a single tank volume plus 10%. Load tanks with either seawater or treated produced water. 6. MIRU HES Frac Equipment. 7. PT Surface lines to ~9,500 psi using a Pressure test fluid. 8. Test IA Pop off system to ensure lines are clear and all components are functioning properly. 9. Bring up pumps and increase annulus pressure to 3,500 psi as the tubing pressures up. 10. Perform DFIT after opening the Alpha Sleeve according to the attached pump schedule. Ensure sufficient volume is pumped to load the well with Frac fluid, prior to shut down. Resume pumping to pump Frac Stage 1. 11. Pump Frac Stages 2 through 21 by following attached pump schedule at ~37 bpm with a maximum expected treating pressure of ~7,050 psi. As described in Section 10 for Stage 21, pressure testing with the cross-linked gel will be performed. 12. The well is ready for Post Frac well prep/production tree installation, coiled tubing cleanout and flowback. SECTION 13 – POST-FRACTURE WELLBORE CLEANUP AND FLUID RECOVERY PLAN 20 AAC 25.283(a)(13) Flowback will be initiated through a de-sander unit until the fluids clean up at which time it will be turned over to production for initial clean up production. Frac Design Attachments: CUSTOMERConoco Phillips FALSEAPIBFD (lb/gal)8.48LAT 70.42061242LEASE3T-613SALES ORDERBHST (°F)139LONG-150.266098FORMATIONMoraineDATE Max Pressure (psi)8500*Exceeds 80% of burst pressure*Prop Slurry Design Clean Design Clean Design Slurry Design Prop Stage Interval CL-28M BC-140X2 Losurf-300D MO-67 Cat-3 BA-20 WG-36 OPTIFLO-IIIOPTIFLO-II BE-6TreatmentStage Fluid Stage Proppant Conc Rate Volume Volume Volume Total Time TimeCrosslinker Crosslinker Surfactant Buffer Catalyst Gel Breaker Breaker BiocideInterval Number Description Description Description(ppg) (bpm) (gal) (bbl) (bbl) (lbs) (hh:mm:ss) (hh:mm:ss)(gpt) (gpt) (gpt) (gpt) (gpt) (gpt) (ppt) (ppt) (ppt) (ppt)1-1 Shut-In Shut-In1:42:46 1-2 Freeze Protect Prime Up Pressure Test 5 1,000 24 24 0:04:46 1:42:46 1-3 Shut-In Shut-In1:38:00 1-4 30# Linear Arsenal Sleeve Shift 5 1,260 30 30 0:06:00 1:38:00 1.00 0.50 30.00 2.00 2.00 0.151-5 30# Linear DFIT 10 1,680 40 40 0:04:00 1:32:00 1.00 0.50 30.00 2.00 2.00 0.151-6 Shut-In Shut-In1:28:00 1-7 Shut-In Step Rate Test 15 8,400 200 200 0:13:20 1:28:00 1-8 30# Hybor G-i Establish Stable Fluid 15 8,400 200 200 0:13:20 1:14:40 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.151-9 30# Hybor G-i Pad 37 16,030 382 382 0:10:19 1:01:20 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.151-10 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:51:01 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.151-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 10,200 243 254 10,200 0:06:52 0:43:13 1.00 0.25 1.00 0.50 30.00 2.00 2.000.151-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 13,600 324 353 27,200 0:09:33 0:36:21 1.00 0.25 1.00 0.50 30.00 2.00 2.000.151-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 13,600 324 367 40,800 0:09:57 0:26:48 1.00 0.25 1.00 0.50 30.00 2.00 2.000.151-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 8,500 202 238 34,000 0:06:28 0:16:51 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.151-15 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 6,800 162 194 30,600 0:05:16 0:10:23 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.151-16 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 5,440 130 158 27,200 0:04:18 0:05:07 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.151-17 30# Linear Spacer and Dart Drop 37 1,260 30 30 0:00:49 0:00:49 1.00 0.50 30.00 2.00 2.00 0.152-1 30# Linear Pre-Pad 37 2,100 50 50 0:01:21 1:06:57 1.00 0.50 30.00 2.00 2.00 0.152-2 30# Hybor G-i Establish Stable Fluid 37 8,400 200 200 0:05:24 1:05:36 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.152-3 30# Hybor G-i Pad 37 15,500 369 369 0:09:58 1:00:11 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.152-4 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:50:13 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.152-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 10,200 243 254 10,200 0:06:52 0:42:24 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.152-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 12,750 304 331 25,500 0:08:57 0:35:32 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.152-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 14,110 336 381 42,330 0:10:19 0:26:35 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.152-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 6,375 152 179 25,500 0:04:51 0:16:16 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.152-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 5,270 125 151 23,715 0:04:05 0:11:25 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.152-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 4,437 106 129 22,185 0:03:30 0:07:20 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.152-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 3,740 89 111 20,570 0:03:01 0:03:49 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.152-12 30# Linear Spacer and Dart Drop 37 1,260 30 30 0:00:49 0:00:49 1.00 0.50 30.00 2.00 2.00 0.153-1 30# Linear Pre-Pad 37 2,100 50 50 0:01:21 1:05:27 1.00 0.50 30.00 2.00 2.00 0.153-2 30# Hybor G-i Establish Stable Fluid 37 8,400 200 200 0:05:24 1:04:06 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.153-3 30# Hybor G-i Pad 37 14,800 352 352 0:09:31 0:58:41 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.153-4 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:49:10 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.153-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 10,200 243 254 10,200 0:06:52 0:41:21 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.153-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 12,750 304 331 25,500 0:08:57 0:34:29 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.153-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 11,900 283 321 35,700 0:08:42 0:25:32 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.153-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 8,500 202 238 34,000 0:06:28 0:16:50 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.153-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 6,800 162 198 34,000 0:05:22 0:10:22 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.153-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 5,100 121 154 30,600 0:04:11 0:04:59 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.153-11 30# Linear Spacer and Dart Drop 37 1,260 30 30 0:00:49 0:00:49 1.00 0.50 30.00 2.00 2.00 0.154-1 30# Linear Pre-Pad 37 2,100 50 50 0:01:21 1:08:31 1.00 0.50 30.00 2.00 2.00 0.154-2 30# Hybor G-i Establish Stable Fluid 37 8,400 200 200 0:05:24 1:07:10 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.154-3 30# Hybor G-i Pad 37 10,785 257 257 0:06:56 1:01:45 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.154-4 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:54:49 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.154-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 7,225 172 180 7,225 0:04:52 0:47:00 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.154-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 7,225 172 187 14,450 0:05:04 0:42:09 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.154-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 6,800 162 184 20,400 0:04:58 0:37:04 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.154-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 7,650 182 215 30,600 0:05:49 0:32:06 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.154-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 6,800 162 198 34,000 0:05:22 0:26:16 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.154-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 5,950 142 180 35,700 0:04:53 0:20:54 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.154-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37 4,250 101 131 27,625 0:03:33 0:16:01 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.154-12 30# Linear Flush 37 13,953 332 332 0:08:59 0:12:29 1.00 0.50 30.00 2.00 2.00 0.154-13 Freeze Protect Freeze Protect 10 1,470 35 35 0:03:30 0:03:30 4-14 Shut-In Shut-InInterval 1Moraine@ 23276.81 - 23281.15 ft 137.3 °F"Alpha SleeveInterval 2Moraine@ 22818.85 - 22823.19 ft 137.4 °F"Frac Sleeve 1Interval 3Moraine@ 22324.92 - 22329.26 ft 137.6 °F"Frac Sleeve 2Interval 4Moraine@ 21829.56 - 21833.9 ft 137.8 °F"Frac Sleeve 3Liquid AdditivesDry Additives50-103-20914Conoco Phillips - 3T-613Planned Design1 CUSTOMERConoco Phillips FALSEAPIBFD (lb/gal)8.48LAT 70.42061242LEASE3T-613SALES ORDERBHST (°F)139LONG-150.266098FORMATIONMoraineDATE Max Pressure (psi)8500*Exceeds 80% of burst pressure*Prop Slurry Design Clean Design Clean Design Slurry Design Prop Stage Interval CL-28M BC-140X2 Losurf-300D MO-67 Cat-3 BA-20 WG-36 OPTIFLO-IIIOPTIFLO-II BE-6TreatmentStage Fluid Stage Proppant Conc Rate Volume Volume Volume Total Time TimeCrosslinker Crosslinker Surfactant Buffer Catalyst Gel Breaker Breaker BiocideInterval Number Description Description Description(ppg) (bpm) (gal) (bbl) (bbl) (lbs) (hh:mm:ss) (hh:mm:ss)(gpt) (gpt) (gpt) (gpt) (gpt) (gpt) (ppt) (ppt) (ppt) (ppt)Liquid AdditivesDry Additives50-103-209145-1 Shut-In Shut-In0:54:18 5-2 Freeze Protect Prime Up Pressure Test 5 1,000 24 24 0:04:46 0:54:18 5-3 Shut-In Shut-In0:49:32 5-4 30# Linear Spacer and Dart Drop 15 1,260 30 30 0:02:00 0:49:32 1.00 0.50 30.00 2.00 2.00 0.155-5 30# Linear Pre-Pad 37 2,100 50 50 0:01:21 0:47:32 1.00 0.50 30.00 2.00 2.00 0.155-6 30# Hybor G-i Establish Stable Fluid 37 8,400 200 200 0:05:24 0:46:11 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.155-7 30# Hybor G-i Pad 37 6,450 154 154 0:04:09 0:40:47 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.155-8 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:36:38 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.155-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 1,700 40 42 1,700 0:01:09 0:28:49 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.155-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 2,175 52 56 4,350 0:01:32 0:27:41 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.155-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 3,400 81 92 10,200 0:02:29 0:26:09 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.155-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 4,100 98 115 16,400 0:03:07 0:23:40 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.155-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 4,240 101 121 19,080 0:03:17 0:20:33 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.155-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00000 37 4,600 110 134 23,000 0:03:38 0:17:15 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.155-15 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 4,680 111 139 25,740 0:03:46 0:13:37 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.155-16 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 4,930 117 149 29,580 0:04:02 0:09:51 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.155-17 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37 3,400 81 104 22,100 0:02:50 0:05:49 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.155-18 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37 2,550 61 80 17,850 0:02:10 0:02:59 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.155-19 30# Linear Spacer and Dart Drop 37 1,260 30 30 0:00:49 0:00:49 1.00 0.50 30.00 2.00 2.00 0.156-1 30# Linear Pre-Pad 37 2,100 50 50 0:01:21 0:47:32 1.00 0.50 30.00 2.00 2.00 0.156-2 30# Hybor G-i Establish Stable Fluid 37 8,400 200 200 0:05:24 0:46:11 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.156-3 30# Hybor G-i Pad 37 6,450 154 154 0:04:09 0:40:47 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.156-4 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:36:38 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.156-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 1,700 40 42 1,700 0:01:09 0:28:49 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.156-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 2,175 52 56 4,350 0:01:32 0:27:41 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.156-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 3,400 81 92 10,200 0:02:29 0:26:09 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.156-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 4,100 98 115 16,400 0:03:07 0:23:40 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.156-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 4,240 101 121 19,080 0:03:17 0:20:33 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.156-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 4,600 110 134 23,000 0:03:38 0:17:15 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.156-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 4,680 111 139 25,740 0:03:46 0:13:37 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.156-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 4,930 117 149 29,580 0:04:02 0:09:51 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.156-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37 3,400 81 104 22,100 0:02:50 0:05:49 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.156-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37 2,550 61 80 17,850 0:02:10 0:02:59 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.156-15 30# Linear Spacer and Dart Drop 37 1,260 30 30 0:00:49 0:00:49 1.00 0.50 30.00 2.00 2.00 0.157-1 30# Linear Pre-Pad 37 2,100 50 50 0:01:21 0:47:32 1.00 0.50 30.00 2.00 2.00 0.157-2 30# Hybor G-i Establish Stable Fluid 37 8,400 200 200 0:05:24 0:46:11 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.157-3 30# Hybor G-i Pad 37 6,450 154 154 0:04:09 0:40:47 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.157-4 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:36:38 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.157-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.0000 37 1,700 40 42 1,700 0:01:09 0:28:49 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.157-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 2,175 52 56 4,350 0:01:32 0:27:41 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.157-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 3,400 81 92 10,200 0:02:29 0:26:09 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.157-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 4,100 98 115 16,400 0:03:07 0:23:40 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.157-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 4,240 101 121 19,080 0:03:17 0:20:33 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.157-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 4,600 110 134 23,000 0:03:38 0:17:15 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.157-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 4,680 111 139 25,740 0:03:46 0:13:37 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.157-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 4,930 117 149 29,580 0:04:02 0:09:51 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.157-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37 3,400 81 104 22,100 0:02:50 0:05:49 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.157-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37 2,550 61 80 17,850 0:02:10 0:02:59 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.157-15 30# Linear Spacer and Dart Drop 37 1,260 30 30 0:00:49 0:00:49 1.00 0.50 30.00 2.00 2.00 0.158-1 30# Linear Pre-Pad 37 2,100 50 50 0:01:21 0:52:12 1.00 0.50 30.00 2.00 2.00 0.158-2 30# Hybor G-i Establish Stable Fluid 37 8,400 200 200 0:05:24 0:50:51 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.158-3 30# Hybor G-i Pad 37 8,610 205 205 0:05:32 0:45:26 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.158-4 30# Hybor G-i Conditioning Pad 100M 0.2500 37 12,000 286 289 3,000 0:07:49 0:39:54 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.158-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 1,900 45 47 1,900 0:01:17 0:32:05 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.158-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 2,375 57 62 4,750 0:01:40 0:30:49 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.158-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 3,800 90 103 11,400 0:02:47 0:29:09 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.158-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 4,570 109 128 18,280 0:03:29 0:26:22 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.158-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 4,760 113 136 21,420 0:03:41 0:22:53 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.158-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 5,140 122 150 25,700 0:04:04 0:19:12 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.158-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 5,200 124 154 28,600 0:04:11 0:15:08 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.158-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 5,550 132 168 33,300 0:04:33 0:10:57 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.158-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37 3,800 90 117 24,700 0:03:10 0:06:24 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.158-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37 2,850 68 89 19,950 0:02:25 0:03:14 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.158-15 30# Linear Spacer and Dart Drop 37 1,260 30 30 0:00:49 0:00:49 1.00 0.50 30.00 2.00 2.00 0.159-1 30# Linear Pre-Pad 37 2,100 50 50 0:01:21 1:02:50 1.00 0.50 30.00 2.00 2.00 0.159-2 30# Hybor G-i Establish Stable Fluid 37 8,400 200 200 0:05:24 1:01:29 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.159-3 30# Hybor G-i Pad 37 8,610 205 205 0:05:32 0:56:05 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.159-4 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:50:33 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.159-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 1,900 45 47 1,900 0:01:17 0:42:44 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.159-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 2,375 57 62 4,750 0:01:40 0:41:27 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.159-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 3,800 90 103 11,400 0:02:47 0:39:47 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.159-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 4,570 109 128 18,280 0:03:29 0:37:00 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.159-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.5000 37 4,760 113 136 21,420 0:03:41 0:33:32 1.00 0.25 1.00 0.50 30.00 2.00 2.000.159-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 5,140 122 150 25,700 0:04:04 0:29:50 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.159-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 5,200 124 154 28,600 0:04:11 0:25:47 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.159-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 5,550 132 168 33,300 0:04:33 0:21:36 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.159-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37 3,800 90 117 24,700 0:03:10 0:17:03 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.159-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37 2,850 68 89 19,950 0:02:25 0:13:52 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.159-15 30# Linear Flush 37 12,360 294 294 0:07:57 0:11:27 1.00 0.50 30.00 2.00 2.00 0.159-16 Freeze Protect Freeze Protect 10 1,470 35 35 0:03:30 0:03:30 9-17 Shut-In Shut-InInterval 9Moraine@ 19337.07 - 19341.41 ft 137.9 °F"Frac Sleeve 8Interval 5Moraine@ 21331.62 - 21335.96 ft 138 °F"Frac Sleeve 4Interval 6Moraine@ 20834.19 - 20838.53 ft 138.3 °F"Frac Sleeve 5Interval 7Moraine@ 20336.33 - 20340.67 ft 138.5 °F"Frac Sleeve 6Interval 8Moraine@ 19795.42 - 19799.76 ft 138.3 °F"Frac Sleeve 7Conoco Phillips - 3T-613Planned Design2 CUSTOMERConoco Phillips FALSEAPIBFD (lb/gal)8.48LAT 70.42061242LEASE3T-613SALES ORDERBHST (°F)139LONG-150.266098FORMATIONMoraineDATE Max Pressure (psi)8500*Exceeds 80% of burst pressure*Prop Slurry Design Clean Design Clean Design Slurry Design Prop Stage Interval CL-28M BC-140X2 Losurf-300D MO-67 Cat-3 BA-20 WG-36 OPTIFLO-IIIOPTIFLO-II BE-6TreatmentStage Fluid Stage Proppant Conc Rate Volume Volume Volume Total Time TimeCrosslinker Crosslinker Surfactant Buffer Catalyst Gel Breaker Breaker BiocideInterval Number Description Description Description(ppg) (bpm) (gal) (bbl) (bbl) (lbs) (hh:mm:ss) (hh:mm:ss)(gpt) (gpt) (gpt) (gpt) (gpt) (gpt) (ppt) (ppt) (ppt) (ppt)Liquid AdditivesDry Additives50-103-2091410-1 Shut-In Shut-In1:34:04 10-2 Freeze Protect Prime Up Pressure Test 5 1,000 24 24 0:04:46 1:34:04 10-3 Shut-In Shut-In1:29:19 10-4 30# Linear Spacer and Dart Drop 15 1,260 30 30 0:02:00 1:29:19 1.00 0.50 30.00 2.00 2.00 0.1510-5 30# Linear Displacement 15 12,041 287 287 0:19:07 1:27:19 1.00 0.50 30.00 2.00 2.00 0.1510-6 30# Linear DFIT 15 1,680 40 40 0:02:40 1:08:12 1.00 0.50 30.00 2.00 2.00 0.1510-7 30# Hybor G-i Establish Stable Fluid 15 8,400 200 200 0:13:20 1:05:32 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1510-8 30# Linear Pre-Pad 37 2,100 50 50 0:01:21 0:52:12 1.00 0.50 30.00 2.00 2.00 0.1510-9 30# Hybor G-i Establish Stable Fluid 37 8,400 200 200 0:05:24 0:50:51 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1510-10 30# Hybor G-i Pad 37 8,610 205 205 0:05:32 0:45:26 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1510-11 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:39:54 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1510-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 1,900 45 47 1,900 0:01:17 0:32:05 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1510-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 2,375 57 62 4,750 0:01:40 0:30:49 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1510-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 3,800 90 103 11,400 0:02:47 0:29:09 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1510-15 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 4,570 109 128 18,280 0:03:29 0:26:22 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1510-16 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 4,760 113 136 21,420 0:03:41 0:22:53 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1510-17 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 5,140 122 150 25,700 0:04:04 0:19:12 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1510-18 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 5,200 124 154 28,600 0:04:11 0:15:08 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1510-19 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 5,550 132 168 33,300 0:04:33 0:10:57 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1510-20 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37 3,800 90 117 24,700 0:03:10 0:06:24 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1510-21 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37 2,850 68 89 19,950 0:02:25 0:03:14 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1510-22 30# Linear Spacer and Dart Drop 37 1,260 30 30 0:00:49 0:00:49 1.00 0.50 30.00 2.00 2.00 0.1511-1 30# Linear Pre-Pad 37 2,100 50 50 0:01:21 0:52:12 1.00 0.50 30.00 2.00 2.00 0.1511-2 30# Hybor G-i Establish Stable Fluid 37 8,400 200 200 0:05:24 0:50:51 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1511-3 30# Hybor G-i Pad 37 8,610 205 205 0:05:32 0:45:26 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1511-4 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:39:54 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1511-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 1,900 45 47 1,900 0:01:17 0:32:05 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1511-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 2,375 57 62 4,750 0:01:40 0:30:49 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1511-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 3,800 90 103 11,400 0:02:47 0:29:09 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1511-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 4,570 109 128 18,280 0:03:29 0:26:22 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1511-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 4,760 113 136 21,420 0:03:41 0:22:53 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1511-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 5,140 122 150 25,700 0:04:04 0:19:12 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1511-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 5,200 124 154 28,600 0:04:11 0:15:08 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1511-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 5,550 132 168 33,300 0:04:33 0:10:57 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1511-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37 3,800 90 117 24,700 0:03:10 0:06:24 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1511-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37 2,850 68 89 19,950 0:02:25 0:03:14 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1511-15 30# Linear Spacer and Dart Drop 37 1,260 30 30 0:00:49 0:00:49 1.00 0.50 30.00 2.00 2.00 0.1512-1 30# Linear Pre-Pad 37 2,100 50 50 0:01:21 0:52:12 1.00 0.50 30.00 2.00 2.00 0.1512-2 30# Hybor G-i Establish Stable Fluid 37 8,400 200 200 0:05:24 0:50:51 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1512-3 30# Hybor G-i Pad 37 8,610 205 205 0:05:32 0:45:26 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1512-4 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:39:54 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1512-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 1,900 45 47 1,900 0:01:17 0:32:05 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1512-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 2,375 57 62 4,750 0:01:40 0:30:49 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1512-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 3,800 90 103 11,400 0:02:47 0:29:09 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1512-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 4,570 109 128 18,280 0:03:29 0:26:22 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1512-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 4,760 113 136 21,420 0:03:41 0:22:53 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1512-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 5,140 122 150 25,700 0:04:04 0:19:12 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1512-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 5,200 124 154 28,600 0:04:11 0:15:08 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1512-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 5,550 132 168 33,300 0:04:33 0:10:57 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1512-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37 3,800 90 117 24,700 0:03:10 0:06:24 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1512-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37 2,850 68 89 19,950 0:02:25 0:03:14 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1512-15 30# Linear Spacer and Dart Drop 37 1,260 30 30 0:00:49 0:00:49 1.00 0.50 30.00 2.00 2.00 0.1513-1 30# Linear Pre-Pad 37 2,100 50 50 0:01:21 0:52:12 1.00 0.50 30.00 2.00 2.00 0.1513-2 30# Hybor G-i Establish Stable Fluid 37 8,400 200 200 0:05:24 0:50:51 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1513-3 30# Hybor G-i Pad 37 8,610 205 205 0:05:32 0:45:26 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1513-4 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:39:54 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1513-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 1,900 45 47 1,900 0:01:17 0:32:05 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1513-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 2,375 57 62 4,750 0:01:40 0:30:49 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1513-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 3,800 90 103 11,400 0:02:47 0:29:09 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1513-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 4,570 109 128 18,280 0:03:29 0:26:22 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1513-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 4,760 113 136 21,420 0:03:41 0:22:53 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1513-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 5,140 122 150 25,700 0:04:04 0:19:12 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1513-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 5,200 124 154 28,600 0:04:11 0:15:08 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1513-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 5,550 132 168 33,300 0:04:33 0:10:57 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1513-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37 3,800 90 117 24,700 0:03:10 0:06:24 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1513-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37 2,850 68 89 19,950 0:02:25 0:03:14 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1513-15 30# Linear Spacer and Dart Drop 37 1,260 30 30 0:00:49 0:00:49 1.00 0.50 30.00 2.00 2.00 0.1514-1 30# Linear Pre-Pad 37 2,100 50 50 0:01:21 1:01:49 1.00 0.50 30.00 2.00 2.00 0.1514-2 30# Hybor G-i Establish Stable Fluid 37 8,400 200 200 0:05:24 1:00:28 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1514-3 30# Hybor G-i Pad 37 8,610 205 205 0:05:32 0:55:04 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1514-4 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:49:31 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1514-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 1,900 45 47 1,900 0:01:17 0:41:42 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1514-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 2,375 57 62 4,750 0:01:40 0:40:26 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1514-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 3,800 90 103 11,400 0:02:47 0:38:46 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1514-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 4,570 109 128 18,280 0:03:29 0:35:59 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1514-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 4,760 113 136 21,420 0:03:41 0:32:30 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1514-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 5,140 122 150 25,700 0:04:04 0:28:49 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1514-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 5,200 124 154 28,600 0:04:11 0:24:45 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1514-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 5,550 132 168 33,300 0:04:33 0:20:34 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1514-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37 3,800 90 117 24,700 0:03:10 0:16:01 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1514-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37 2,850 68 89 19,950 0:02:25 0:12:51 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1514-15 30# Linear Flush 37 10,766 256 256 0:06:56 0:10:26 1.00 0.50 30.00 2.00 2.00 0.1514-16 Freeze Protect Freeze Protect 10 1,470 35 35 0:03:30 0:03:30 14-17 Shut-In Shut-InInterval 10Moraine@ 18837.88 - 18842.22 ft 137.9 °F"Frac Sleeve 9Interval 11Moraine@ 18339.06 - 18343.4 ft 138.1 °F"Frac Sleeve 10Interval 12Moraine@ 17840.76 - 17845.1 ft 138.5 °F"Frac Sleeve 11Interval 13Moraine@ 17341.75 - 17346.09 ft 139 °F"Frac Sleeve 12Interval 14Moraine@ 16843.15 - 16847.49 ft 138.9 °F"Frac Sleeve 13Conoco Phillips - 3T-613Planned Design3 CUSTOMERConoco Phillips FALSEAPIBFD (lb/gal)8.48LAT 70.42061242LEASE3T-613SALES ORDERBHST (°F)139LONG-150.266098FORMATIONMoraineDATE Max Pressure (psi)8500*Exceeds 80% of burst pressure*Prop Slurry Design Clean Design Clean Design Slurry Design Prop Stage Interval CL-28M BC-140X2 Losurf-300D MO-67 Cat-3 BA-20 WG-36 OPTIFLO-IIIOPTIFLO-II BE-6TreatmentStage Fluid Stage Proppant Conc Rate Volume Volume Volume Total Time TimeCrosslinker Crosslinker Surfactant Buffer Catalyst Gel Breaker Breaker BiocideInterval Number Description Description Description(ppg) (bpm) (gal) (bbl) (bbl) (lbs) (hh:mm:ss) (hh:mm:ss)(gpt) (gpt) (gpt) (gpt) (gpt) (gpt) (ppt) (ppt) (ppt) (ppt)Liquid AdditivesDry Additives50-103-2091415-1 Shut-In Shut-In1:01:19 15-2 Freeze Protect Prime Up Pressure Test 5 1,000 24 24 0:04:46 1:01:19 15-3 Shut-In Shut-In0:56:34 15-4 30# Linear Spacer and Dart Drop 15 1,260 30 30 0:02:00 0:56:34 1.00 0.50 30.00 2.00 2.00 0.1515-5 30# Linear Pre-Pad 37 2,100 50 50 0:01:21 0:54:34 1.00 0.50 30.00 2.00 2.00 0.1515-6 30# Hybor G-i Establish Stable Fluid 37 8,400 200 200 0:05:24 0:53:13 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1515-7 30# Hybor G-i Pad 37 9,710 231 231 0:06:15 0:47:48 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1515-8 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:41:33 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1515-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 2,000 48 50 2,000 0:01:21 0:33:45 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1515-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 2,500 60 65 5,000 0:01:45 0:32:24 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1515-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 4,000 95 108 12,000 0:02:56 0:30:39 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1515-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 4,850 115 136 19,400 0:03:41 0:27:43 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1515-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 5,000 119 143 22,500 0:03:53 0:24:02 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1515-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 5,410 129 158 27,050 0:04:17 0:20:09 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1515-15 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 5,500 131 163 30,250 0:04:26 0:15:52 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1515-16 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 5,800 138 175 34,800 0:04:45 0:11:27 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1515-17 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37 4,000 95 123 26,000 0:03:20 0:06:42 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1515-18 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37 3,000 71 94 21,000 0:02:33 0:03:21 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1515-19 30# Linear Spacer and Dart Drop 37 1,260 30 30 0:00:49 0:00:49 1.00 0.50 30.00 2.00 2.00 0.1516-1 30# Linear Pre-Pad 37 2,100 50 50 0:01:21 0:54:34 1.00 0.50 30.00 2.00 2.00 0.1516-2 30# Hybor G-i Establish Stable Fluid 37 8,400 200 200 0:05:24 0:53:13 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1516-3 30# Hybor G-i Pad 37 9,710 231 231 0:06:15 0:47:48 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1516-4 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:41:33 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1516-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 2,000 48 50 2,000 0:01:21 0:33:45 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1516-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 2,500 60 65 5,000 0:01:45 0:32:24 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1516-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 4,000 95 108 12,000 0:02:56 0:30:39 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1516-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 4,850 115 136 19,400 0:03:41 0:27:43 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1516-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 5,000 119 143 22,500 0:03:53 0:24:02 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1516-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 5,410 129 158 27,050 0:04:17 0:20:09 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1516-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 5,500 131 163 30,250 0:04:26 0:15:52 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1516-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00000 37 5,800 138 175 34,800 0:04:45 0:11:27 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1516-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37 4,000 95 123 26,000 0:03:20 0:06:42 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1516-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37 3,000 71 94 21,000 0:02:33 0:03:21 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1516-15 30# Linear Spacer and Dart Drop 37 1,260 30 30 0:00:49 0:00:49 1.00 0.50 30.00 2.00 2.00 0.1517-1 30# Linear Pre-Pad 37 2,100 50 50 0:01:21 0:54:34 1.00 0.50 30.00 2.00 2.00 0.1517-2 30# Hybor G-i Establish Stable Fluid 37 8,400 200 200 0:05:24 0:53:13 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1517-3 30# Hybor G-i Pad 37 9,710 231 231 0:06:15 0:47:48 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1517-4 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:41:33 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1517-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 2,000 48 50 2,000 0:01:21 0:33:45 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1517-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 2,500 60 65 5,000 0:01:45 0:32:24 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1517-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 4,000 95 108 12,000 0:02:56 0:30:39 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1517-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 4,850 115 136 19,400 0:03:41 0:27:43 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1517-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 5,000 119 143 22,500 0:03:53 0:24:02 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1517-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 5,410 129 158 27,050 0:04:17 0:20:09 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1517-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.5000 37 5,500 131 163 30,250 0:04:26 0:15:52 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1517-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 5,800 138 175 34,800 0:04:45 0:11:27 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1517-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37 4,000 95 123 26,000 0:03:20 0:06:42 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1517-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37 3,000 71 94 21,000 0:02:33 0:03:21 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1517-15 30# Linear Spacer and Dart Drop 37 1,260 30 30 0:00:49 0:00:49 1.00 0.50 30.00 2.00 2.00 0.1518-1 30# Linear Pre-Pad 37 2,100 50 50 0:01:21 0:54:34 1.00 0.50 30.00 2.00 2.00 0.1518-2 30# Hybor G-i Establish Stable Fluid 37 8,400 200 200 0:05:24 0:53:13 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1518-3 30# Hybor G-i Pad 37 9,710 231 231 0:06:15 0:47:48 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1518-4 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:41:33 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1518-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 2,000 48 50 2,000 0:01:21 0:33:45 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1518-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 2,500 60 65 5,000 0:01:45 0:32:24 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1518-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 4,000 95 108 12,000 0:02:56 0:30:39 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1518-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 4,850 115 136 19,400 0:03:41 0:27:43 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1518-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 5,000 119 143 22,500 0:03:53 0:24:02 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1518-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 5,410 129 158 27,050 0:04:17 0:20:09 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1518-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 5,500 131 163 30,250 0:04:26 0:15:52 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1518-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 5,800 138 175 34,800 0:04:45 0:11:27 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1518-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37 4,000 95 123 26,000 0:03:20 0:06:42 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1518-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37 3,000 71 94 21,000 0:02:33 0:03:21 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1518-15 30# Linear Spacer and Dart Drop 37 1,260 30 30 0:00:49 0:00:49 1.00 0.50 30.00 2.00 2.00 0.1519-1 30# Linear Pre-Pad 37 2,100 50 50 0:01:21 1:03:09 1.00 0.50 30.00 2.00 2.00 0.1519-2 30# Hybor G-i Establish Stable Fluid 37 8,400 200 200 0:05:24 1:01:48 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1519-3 30# Hybor G-i Pad 37 9,710 231 231 0:06:15 0:56:24 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1519-4 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:50:09 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1519-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 2,000 48 50 2,000 0:01:21 0:42:20 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1519-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 2,500 60 65 5,000 0:01:45 0:41:00 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1519-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 4,000 95 108 12,000 0:02:56 0:39:14 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1519-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 4,850 115 136 19,400 0:03:41 0:36:19 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1519-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 5,000 119 143 22,500 0:03:53 0:32:37 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1519-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 5,410 129 158 27,050 0:04:17 0:28:45 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1519-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 5,500 131 163 30,250 0:04:26 0:24:28 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1519-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 5,800 138 175 34,800 0:04:45 0:20:03 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1519-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37 4,000 95 123 26,000 0:03:20 0:15:17 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1519-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37 3,000 71 94 21,000 0:02:33 0:11:57 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1519-15 30# Linear Flush 37 9,177 218 218 0:05:54 0:09:24 1.00 0.50 30.00 2.00 2.00 0.1519-16 Freeze Protect Freeze Protect 10 1,470 35 35 0:03:30 0:03:30 19-17 Shut-In Shut-InInterval 15Moraine@ 16349.44 - 16353.78 ft 138.9 °F"Frac Sleeve 14Interval 16Moraine@ 15850.53 - 15854.87 ft 138.7 °F"Frac Sleeve 15Interval 17Moraine@ 15352.19 - 15356.53 ft 138.5 °F"Frac Sleeve 16Interval 18Moraine@ 14854.27 - 14858.61 ft 138.3 °F"Frac Sleeve 17Interval 19Moraine@ 14356.39 - 14360.73 ft 138.1 °F"Frac Sleeve 18Conoco Phillips - 3T-613Planned Design4 CUSTOMERConoco Phillips FALSEAPIBFD (lb/gal)8.48LAT 70.42061242LEASE3T-613SALES ORDERBHST (°F)139LONG-150.266098FORMATIONMoraineDATE Max Pressure (psi)8500*Exceeds 80% of burst pressure*Prop Slurry Design Clean Design Clean Design Slurry Design Prop Stage Interval CL-28M BC-140X2 Losurf-300D MO-67 Cat-3 BA-20 WG-36 OPTIFLO-IIIOPTIFLO-II BE-6TreatmentStage Fluid Stage Proppant Conc Rate Volume Volume Volume Total Time TimeCrosslinker Crosslinker Surfactant Buffer Catalyst Gel Breaker Breaker BiocideInterval Number Description Description Description(ppg) (bpm) (gal) (bbl) (bbl) (lbs) (hh:mm:ss) (hh:mm:ss)(gpt) (gpt) (gpt) (gpt) (gpt) (gpt) (ppt) (ppt) (ppt) (ppt)Liquid AdditivesDry Additives50-103-2091420-1 Shut-In Shut-In1:08:06 20-2 Freeze Protect Prime Up Pressure Test 5 1,000 24 24 0:04:46 1:08:06 20-3 Shut-In Shut-In1:03:21 20-4 30# Linear Spacer and Dart Drop 15 1,260 30 30 0:02:00 1:03:21 1.00 0.50 30.00 2.00 2.00 0.1520-5 30# Linear Displacement 37 8,859 211 211 0:05:42 1:01:21 1.00 0.50 30.00 2.00 2.00 0.1520-6 30# Linear DFIT 37 1,680 40 40 0:01:05 0:55:38 1.00 0.50 30.00 2.00 2.00 0.1520-7 30# Linear Pre-Pad 37 2,100 50 50 0:01:21 0:54:34 1.00 0.50 30.00 2.00 2.00 0.1520-8 30# Hybor G-i Establish Stable Fluid 37 8,400 200 200 0:05:24 0:53:13 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1520-9 30# Hybor G-i Pad 37 9,710 231 231 0:06:15 0:47:48 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1520-10 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:41:33 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1520-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 2,000 48 50 2,000 0:01:21 0:33:45 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1520-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 2,500 60 65 5,000 0:01:45 0:32:24 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1520-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 4,000 95 108 12,000 0:02:56 0:30:39 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1520-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 4,850 115 136 19,400 0:03:41 0:27:43 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1520-15 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 5,000 119 143 22,500 0:03:53 0:24:02 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1520-16 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 5,410 129 158 27,050 0:04:17 0:20:09 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1520-17 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 5,500 131 163 30,250 0:04:26 0:15:52 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1520-18 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 5,800 138 175 34,800 0:04:45 0:11:27 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1520-19 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37 4,000 95 123 26,000 0:03:20 0:06:42 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1520-20 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37 3,000 71 94 21,000 0:02:33 0:03:21 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1520-21 30# Linear Spacer and Dart Drop 37 1,260 30 30 0:00:49 0:00:49 1.00 0.50 30.00 2.00 2.00 0.1521-1 30# Hybor G-i Minifrac - Treatment 37 2,900 69 69 0:01:52 0:32:12 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1521-2 30# Linear Minifrac - Flush 37 8,540 203 203 0:05:30 0:30:20 1.00 0.50 30.00 2.00 2.00 0.1521-3 30# Linear Pre-Pad 37 2,100 50 50 0:01:21 0:24:50 1.00 0.50 30.00 2.00 2.00 0.1521-4 30# Hybor G-i Establish Stable Fluid 37 8,400 200 200 0:05:24 0:23:29 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1521-5 30# Hybor G-i Pad 370:18:04 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1521-6 30# Hybor G-i Conditioning Pad Wanli 16/20 Ceramic 0.25 37 5,800 138 140 1,450 0:03:46 0:18:04 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1521-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 1,000 24 25 1,000 0:00:40 0:14:18 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1521-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 1,200 29 31 2,400 0:00:51 0:13:38 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1521-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 1,400 33 38 4,200 0:01:01 0:12:47 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1521-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 1,900 45 53 7,600 0:01:27 0:11:46 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1521-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 2,100 50 61 10,500 0:01:40 0:10:19 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1521-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 2,300 55 69 13,800 0:01:53 0:08:39 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1521-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37 1,500 36 47 10,500 0:01:16 0:06:46 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1521-14 30# Linear Flush 37 8,540 203 203 0:05:30 0:05:30 1.00 0.50 30.00 2.00 2.00 0.1521-15 Shut-In Shut-In1,672,384 39,819 43,889 3,831,450Design Total (gal)Design Total (lbs)CL-28M BC-140X2 Losurf-300D MO-67 Cat-3 BA-20 WG-36 OPTIFLO-III OPTIFLO-II BE-6-3,771,450(gal) (gal) (gal) (gal) (gal) (gal) (lbs) (lbs) (lbs) (lbs)157,73760,000Initial Design Material Volume 1,495.4 373.8 1,653.1 826.6 49,593.1 3,306.2 3,306.2 248.0-10,880-Whole Units to be ordered1,495,367-CL-28M BC-140X2 Losurf-300D MO-67 Cat-3 BA-20 WG-36 OPTIFLO-III OPTIFLO-II BE-6-(gpm) (gpm) (gpm) (gpm) (gpm) (gpm) ppm ppm ppm ppm-Max Additive Rate 1.6 0.4 1.6 0.8 46.6 3.1 3.1 0.2-Min Additive Rate21:09:01 Interval 20Moraine@ 13859.35 - 13863.69 ft 138.1 °F"Frac Sleeve 18Interval 21Moraine@ 13361.01 - 13365.35 ft 137.9 °F"Frac Sleeve 20Proppant TypeWanli 16/20 Ceramic100M---Fluid Type-30# LinearSeawaterFreeze Protect30# Hybor G-i---Conoco Phillips - 3T-613Planned Design5 Hydraulic Fracturing Fluid Product Component Information Disclosure 2025-06-03 Alaska HARRISON BAY 50-103-20914-00-00 CONOCOPHILLIPS 3T 613 -150.26609799 70.42061241 NAD83 none Oil 5090 1588864.8 Hydraulic Fracturing Fluid Composition: Trade Name Supplier Purpose Ingredients Chemical Abstract Service Number (CAS #) Maximum Ingredient Concentration in Additive (% by mass)** Maximum Ingredient Concentration in HF Fluid (% by mass)** Ingredient Mass lbs Comments Company First Name Last Name Email Phone Produced Water (Density 8.5)Operator Base Fluid Density = 8.50 SEAWATER (SG 8.52)Operator Base Fluid Density = 8.52 BA-20 BUFFERING AGENT Halliburton Buffer BC-140 X2 Halliburton Initiator BE-6(TM) Bactericide Halliburton Microbiocide CAT-3 ACTIVATOR Halliburton Activator CL-28M CROSSLINKER Halliburton Crosslinker LoSurf-300D Halliburton Non-ionic Surfactant MO-67 Halliburton pH Control OPTIFLO-II DELAYED RELEASE BREAKER Halliburton Breaker OPTIFLO-III DELAYED RELEASE BREAKER Halliburton Breaker WG-36 GELLING AGENT Halliburton Gelling Agent Ceramic Proppant - Wanli Wanli Proppant SAND, COMMON BROWN 100 MESH Halliburton Proppant Flow Insurance Copper Patina Energy Tracer OPT 2002-2054 ResMetrics Tracer WPT 1001-1052 ResMetrics Tracer Ingredients Water 7732-18-5 95.00%74.45305%13536277 Corundum 1302-74-5 60.00%12.44638%2262870 Mullite 1302-93-8 40.00%8.29758%1508580 Sodium chloride 7647-14-5 5.00%3.91858%712436 Crystalline silica, quartz 14808-60-7 100.00%0.33738%61339 Guar gum 9000-30-0 100.00%0.27277%49593 Water 7732-18-5 100.00%0.11356%20647 Borate salts Proprietary 60.00%0.05225%9500 Denise Tuck, Halliburton, 3000 N. Sam Houston Pkwy E., Houston, TX 77032, 281-871- 6226 Halliburton Denise Tuck Denise.Tuck @Halliburton. com 281-871- 6226 Ethanol 64-17-5 60.00%0.04146%7538 Ammonium persulfate 7727-54-0 100.00%0.03637%6612 Monoethanolamine borate 26038-87-9 100.00%0.02090%3800 Oxyalkylated nonyl phenolic resin Proprietary 30.00%0.02073%3769 Halliburton Denise Tuck Denise.Tuck @Halliburton. com 281-871- 6226 Heavy aromatic petroleum naphtha 64742-94-5 30.00%0.02073%3769 Sodium hydroxide 1310-73-2 30.00%0.01445%2628 Oxylated phenolic resin Proprietary 30.00%0.01091%1984 Halliburton Denise Tuck Denise.Tuck @Halliburton. com 281-871- 6226 Oxyalkylated phenolic resin Proprietary 10.00%0.00691%1257 Halliburton Denise Tuck Denise.Tuck @Halliburton. com 281-871- 6226 Ethylene glycol 107-21-1 30.00%0.00627%1140 Ammonium acetate 631-61-8 100.00%0.00505%919 Water 7732-18-5 100.00%0.00468%850 Potassium chloride 7447-40-7 5.00%0.00435%792 Inorganic mineral 1317-65-3 5.00%0.00435%792 Naphthalene 91-20-3 5.00%0.00345%629 Poly(oxy-1,2-ethanediyl), alpha-(4- nonylphenyl)-omega-hydroxy-, branched 127087-87-0 5.00%0.00345%629 Flow Insurance Copper Proprietary 100.00%0.00243%442 Patina Energy Product Stewardship test@patinae nergy.com 7205324886 Acetic acid 64-19-7 30.00%0.00152%276 EDTA/Copper chelate Proprietary 30.00%0.00138%251 Halliburton Denise Tuck Denise.Tuck @Halliburton. com 281-871- 6226 2-Bromo-2-nitro-1,3-propanediol 52-51-7 100.00%0.00136%248 Gluteraldehyde 111-30-8 1.00%0.00087%159 Polymer Proprietary 1.00%0.00087%159 Halliburton Denise Tuck Denise.Tuck @Halliburton. com 281-871- 6226 Calcium magnesium carbonate 16389-88-1 1.00%0.00087%159 Inorganic mineral Proprietary 1.00%0.00087%159 Halliburton Denise Tuck Denise.Tuck @Halliburton. com 281-871- 6226 Glycol Ether Proprietary 85.00%0.00079%143 ResMetrics Product Stewardship info@resmetri cs.com 8325921900 1,2,4 Trimethylbenzene 95-63-6 1.00%0.00069%126 Sodium chloride 7647-14-5 1.00%0.00048%88 Confidential Proprietary 20.00%0.00028%52 ResMetrics Product Stewardship info@resmetri cs.com 8325921900 Ammonium chloride 12125-02-9 5.00%0.00023%42 Ethylene Glycol 107-21-1 20.00%0.00019%35 C.I. pigment Orange 5 3468-63-1 1.00%0.00018%34 Methanesulfonic acid, 1-hydroxy-, sodium salt 870-72-4 0.10%0.00009%16 Sodium bisulfate 7681-38-1 0.10%0.00009%16 Ammonia 7664-41-7 1.00%0.00005%9 2,7-Naphthalenedisulfonic acid, 3- hydroxy-4-[(4-sulfor-1- naphthalenyl) azo] -, trisodium salt 915-67-3 0.10%0.00002%4 Magnesium nitrate 10377-60-3 0.01%0.00001%2 Magensium chloride 7786-30-3 0.01%0.00001%2 5-Chloro-2-methyl-3(2H)- Isothaiazolone 26172-55-4 0.01%0.00001%2 2-Methyl-4-isothiazolin-3-one 2682-20-4 0.01%0.00001%2 * Total Water Volume sources may include fresh water, produced water, and/or recycled water _ ** Information is based on the maximum potential for concentration and thus the total may be over 100% Note: For Field Development Products (products that begin with FDP), MSDS level only information has been provided.Version web 1.5 All component information listed was obtained from the supplier’s Material Safety Data Sheets (MSDS). As such, the Operator is not responsible for inaccurate and/or incomplete information. Any questions regarding the content of the MSDS should be direct ed to the supplier who provided it. The Occupational Safety and Health Administration’s (OSHA) regulations govern the criteria for the disclosure of this information. Please note that Federal Law protects "proprietary", "trade secret", and "confidential business information" and the criteria for how this information is reported on an MSDS is subject to 29 CFR 1910.1200(i) and Appendix D. Production Type: True Vertical Depth (TVD): Total Water Volume (gal)*: MSDS and Non-MSDS Ingredients are listed below the green line Well Name and Number: Longitude: Latitude: Long/Lat Projection: Indian/Federal: Fracture Date State: County: API Number: Operator Name: 1. Type of Request:Abandon Plug Perforations Fracture Stimulate Repair Well Operations shutdown Suspend Perforate Other Stimulate Pull Tubing Change Approved Program Plug for Redrill Perforate New Pool Re-enter Susp Well Alter Casing Other: ___________________ 2. Operator Name:4. Current Well Class: 5. Permit to Drill Number: Exploratory Development 3. Address:Stratigraphic Service 6. API Number: 7. If perforating:8. Well Name and Number: What Regulation or Conservation Order governs well spacing in this pool? Yes No 9. Property Designation (Lease Number):10. Field: Kuparuk River Field 11. Total Depth MD (ft):Total Depth TVD (ft): Effective Depth MD: Effective Depth TVD: Junk (MD): 20,976 Casing Collapse Structural Conductor Surface Intermediate Production Liner Packers and SSSV Type:Packers and SSSV MD (ft) and TVD (ft): 12. Attachments:Proposal Summary Wellbore schematic 13. Well Class after proposed work: Detailed Operations Program BOP Sketch Exploratory Stratigraphic Development Service 14. Estimated Date for 15. Well Status after proposed work: Commencing Operations:OIL WINJ WDSPL Suspended 16. Verbal Approval:Date: GAS WAG GSTOR SPLUG AOGCC Representative: GINJ Op Shutdown Abandoned Contact Name:Weifeng Dai Contact Email: Contact Phone: 907-265-6936 Authorized Title: Conditions of approval: Notify AOGCC so that a representative may witness Sundry Number: Plug Integrity BOP Test Mechanical Integrity Test Location Clearance Other Conditions of Approval: Post Initial Injection MIT Req'd? Yes No APPROVED BY Approved by: COMMISSIONER THE AOGCC Date: Comm. Comm. Sr Pet Eng Sr Pet Geo Sr Res Eng Wells Engineering Manager Chris Brillon weifeng.dai@conocophillips.com Subsequent Form Required: Suspension Expiration Date: Authorized Name and Digital Signature with Date: MPSP (psi):Plugs (MD): 17. I hereby certify that the foregoing is true and the procedure approved herein will not be deviated from without prior written approval. Tubing Size: PRESENT WELL CONDITION SUMMARY Length Size TVD BurstMD AOGCC USE ONLY Tubing Grade:Tubing MD (ft):Perforation Depth TVD (ft):Perforation Depth MD (ft): STATE OF ALASKA ALASKA OIL AND GAS CONSERVATION COMMISSION APPLICATION FOR SUNDRY APPROVALS 20 AAC 25.280 ADL025528/ADL393883/ADL393844 225-036 P.O. Box 100360 Anchorage, Alaska, 99501-0360 50-103-20914-00-00 ConocoPhillips Alaska. Inc. Proposed Pools: KRU 3T-613 Torok Oil Poll Torok Oil Pool Will perfs require a spacing exception due to property boundaries? Current Pools: 120120 5,205 9,772-8,872 5/31/2025 20"81 mmmm m wn nn P s 2 6 5 6 t y t __ o c N Form 10-403 Revised 06/2023 Approved application valid for 12 months from date of approval.Submit PDF to aogcc.permitting@alaska.gov 325-279 By Grace Christianson at 11:15 am, May 06, 2025 A.Dewhurst 21MAY25 DSR-5/6/25 X Initial BOP test to 5000 psig; subsequent BOP test to 4000 psig Annular preventer test to 2500 psig BOPE testing on a 21-day interval is approved VTL6/4/2025 file w/ PTD 10-407 *&: Jessie L. Chmielowski Digitally signed by Jessie L. Chmielowski Date: 2025.06.05 08:08:59 -08'00'06/05/25 RBDMS JSB 060525 ConocoPhillips Alaska, Inc. Post Office Box 100360 Anchorage, Alaska 99510-0360 Telephone 907-276-1215 May 5th, 2025 Alaska Oil and Gas Conservation Commission 333 West 7th Avenue, Suite 100 Anchorage, Alaska 99501 Re: Sundry to Approved Program for 3T-613 Dear Sir or Madam: ConocoPhillips Alaska, Inc. hereby applies for a Sundry to Change Approved Program for 3T-613, an onshore producer well from the 3T drilling pad currently being drilled with the Doyon 142 drilling rig. 3T-613 is planned to be a fracture stimulated horizontal producer within the Moraine formation. There is a change in the completion design for well 3T-613 from the approved PTD. Instead of the open hole completion design with a liner running frac sleeves and swell packers as stated in the original PTD, ConocoPhillips has decided to cement the liner. This is the same completion design that was implemented in the previous 3T-616 redrill. Additionally, the upper completion will now utilize gas-lift instead of ESP as originally planned. Please find attached the information for your review. Pertinent information attached to this application includes the following: 1. A proposed schematic of the well with new completion design. If you have any questions or require further information, please contact Weifeng Dai at 907-265-6936 (Weifeng.Dai@conocophillips.com) or Chris Brillon at 907-265-6120. Sincerely, cc: 3T-613 Well File / Jenna Taylor ATO 1560 Will Earhart ATO 1552 Chris Brillon ATO 1548 Weifeng Dai Staff Drilling Engineer /ŶƚĞƌŵĞĚŝĂƚĞdKϱϬϬΖDŽƌϮϱϬΖdsďŽǀĞƚŚĞŽLJŽƚĞdŽƉϳϴϲϭΖDͬϯϰϰϴΖds^ƵƌĨĂĐĞĂƐŝŶŐϭϬ͘ϳϱΗϰϱ͘ϱη>ϴϬ,ϱϲϯϮϲϳϬΖDͬϮϰϯϯΖdsĞŵĞŶƚĞĚƚŽ^ƵƌĨĂĐĞ>ĞĂĚ͗ϭϬ͘ϳƉƉŐ͖dĂŝů͗ϭϱ͘ϴƉƉŐŽŶĚƵĐƚŽƌϮϬΗ/ŶƐƵůĂƚĞĚϭϮϬDͬdsĞŵĞŶƚĞĚƚŽ^ƵƌĨĂĐĞhƉƉĞƌŽŵƉůĞƚŝŽŶϭ͘ϮĞĂ'ĂƐ>ŝĨƚDĂŶĚƌĞůϮ͘, ^KƉƐŝƐƵĂůŽǁŶŚŽůĞ'ĂƵŐĞϯ͘, ^ϳͲϱͬϴΗdžϰͲϭͬϮΗdEdWĂĐŬĞƌϰ͘ƌƐĞŶĂů'ůĂƐƐŝƐŬ;ǁŝůůďĞƐŚĂƌĞĚĚƵƌŝŶŐĨƌĂĐͿϱ͘, ^^ĞůĨͲůŝŐŶŝŶŐDƵůĞƐŚŽĞǁŝƚŚĂŬĞƌ^ŚĞĂƌ>ŽĐĂƚŽƌ>ŽǁĞƌŽŵƉůĞƚŝŽŶϭ͘ĂŬĞƌyWWĂĐŬĞƌĂŶĚ&ůĞdžͲ>ŽĐŬ,ĂŶŐĞƌϮ͘ϮϬĞĂĂƌƚͲĐƚŝǀĂƚĞĚ&ƌĂĐ^ůĞĞǀĞƐϯ͘ϮĞĂĂŬĞƌůƉŚĂ^ůĞĞǀĞƐϰ͘ĂŬĞƌ>ĂŶĚŝŶŐŽůůĂƌϱ͘ŝƚĂĚĞůDK^^ŚŽĞϯdͲϲϭϯ^ŝŶŐůĞ>ĂƚĞƌĂůWƌŽĚƵĐĞƌĂƐĞWĞƌŵϭϱϳϬΖDͬϭϱϯϴΖdsdŽƉŽLJŽƚĞϴϵϮϬΖDͬϰϬϵϴΖdsdŽƉdŽƌŽŬKŝůWŽŽů;DŽƌĂŝŶĞͿϭϮϳϳϬΖDͬϱϬϬϮΖds/ŶƚĞƌŵĞĚŝĂƚĞĂƐŝŶŐϳ͘ϲϮϱΗϮϵ͘ϳη>ϴϬ,ϱϲϯнϴϬϬΖϯϯ͘ϳηWϭϭϬ^,ϱϲϯ,ĞĂǀLJ,ĞĞůϭϮϴϭϬΖDͬϱϬϬϵΖdsWƌŽĚƵĐƚŝŽŶdK>>ŝŶĞƌdŽƉWĂĐŬĞƌĂŶĚ,ĂŶŐĞƌϲ͘ϱ͟WƌŽĚƵĐƚŝŽŶ,ŽůĞϮϯϲϯϰΖDͬϱϬϯϭΖdsWƌŽĚƵĐƚŝŽŶ>ŝŶĞƌ ǁͬ&ƌĂĐ^ůĞĞǀĞƐϰ͘ϱΗϭϮ͘ϲηWϭϭϬ^,ϱϲϯĞŵĞŶƚĞĚƚŽƚŽƉŽĨůŝŶĞƌtĞůůWůĂŶ͗tWϭϮhƉĚĂƚĞĚϬϱͬϬϱͬϮϬϮϱ Alaska Oil and Gas Conservation Commission 333 West Seventh Avenue Anchorage, Alaska 99501-3572 Main: 907.279.1433 Fax: 907.276.7542 www.aogcc.alaska.gov Chris Brillon Wells Engineering Manager Conoco Phillips Alaska, Inc. 700 G Street Anchorage, AK, 99501 Re: Kuparuk River Field, Torok Oil Pool, KRU 3T-613 Conoco Phillips Alaska, Inc. Permit to Drill Number: 225-036, Surface Location: 1888' FSL, 513' FWL, SENE S1 T12N R7E, UM Bottomhole Location: 4724' FSL, 3061' FWL, SENW S21 T13N R7E, UM Dear Mr. Brillon: Enclosed is the approved application for the permit to drill the above referenced well. Per Statute AS 31.05.030(d)(2)(B) and Regulation 20 AAC 25.071, composite curves for all well logs run must be submitted to the AOGCC within 90 days after completion, suspension, or abandonment of this well, or within 90 days of acquisition of the data, whichever occurs first. This permit to drill does not exempt you from obtaining additional permits or an approval required by law from other governmental agencies and does not authorize conducting drilling operations until all other required permits and approvals have been issued. In addition, the AOGCC reserves the right to withdraw the permit in the event it was erroneously issued. Operations must be conducted in accordance with AS 31.05 and Title 20, Chapter 25 of the Alaska Administrative Code unless the AOGCC specifically authorizes a variance. Failure to comply with an applicable provision of AS 31.05, Title 20, Chapter 25 of the Alaska Administrative Code, or an AOGCC order, or the terms and conditions of this permit may result in the revocation or suspension of the permit. Sincerely, Jessie L. Chmielowski Commissioner DATED this 24th day of April 2024. Jessie L. Chmielowski Digitally signed by Jessie L. Chmielowski Date: 2025.04.24 13:58:47 -08'00' 1a. Type of Work:1b. Proposed Well Class: Exploratory - Gas Service - WAG Service - Disp 1c. Specify if well is proposed for: Drill Lateral Stratigraphic Test Development - Oil Service - Winj Single Zone Coalbed Gas Gas Hydrates Redrill Reentry Exploratory - Oil Development - Gas Service - Supply Multiple Zone Geothermal Shale Gas 2. Operator Name:5. Bond: Blanket Single Well 11. Well Name and Number: Bond No. 3. Address:6. Proposed Depth: 12. Field/Pool(s): MD: 23634 TVD: 5107 4a. Location of Well (Governmental Section):7. Property Designation: Surface: Top of Productive Horizon:8. DNR Approval Number: 13. Approximate Spud Date: 5/10/2025 Total Depth: 9. Acres in Property: 14. Distance to Nearest Property: 560' to ADL355037 4b. Location of Well (State Base Plane Coordinates - NAD 27):10. KB Elevation above MSL (ft): 51.1 15. Distance to Nearest Well Open Surface: x-467723 y- 6003614 Zone- 4 12 to Same Pool: 770' to 3T-612 16. Deviated wells: Kickoff depth: 300 feet 17. Maximum Potential Pressures in psig (see 20 AAC 25.035) Maximum Hole Angle: 90 degrees Downhole: Surface: Hole Casing Weight Grade Coupling Length MD TVD MD TVD 42"20" 94 H-40 Welded 80.9 39.1 39.1 120 120 13.5"10.75" 45.5 L80 Hyd563 2664.9 39.1 39.1 2704 2449 9.875"7.625" 29.7 L80 Hyd563 12375.9 39.1 39.1 12415 4842 9.875"7.625" 33.7 P110-S Hyd563 800 12415 4841.8 13215 5030 6.5"4.5" 12.6 P110-S Hyd563 10569 13065 5107 23634 5107 19.PRESENT WELL CONDITION SUMMARY (To be completed for Redrill and Re-Entry Operations) Junk (measured): TVD Hydraulic Fracture planned?Yes No 20. Attachments:Property Plat BOP Sketch Drilling Program Time v. Depth Plot Shallow Hazard Analysis Diverter Sketch Seabed Report Drilling Fluid Program 20 AAC 25.050 requirements Contact Name: Weifeng Dai Chris Brillon Contact Email:Weifeng.Dai@cop.com Wells Engineering Manager Contact Phone:907-265-6936 Date: Permit to Drill API Number: Permit Approval Number:Date: Conditions of approval : If box is checked, well may not be used to explore for, test, or produce coalbed methane, gas hydrates, or gas contained in shales: Samples req'd: Yes No Mud log req'd: Yes No H2S measures: Yes No Directional svy req'd: Yes No Spacing exception req'd: Yes No Inclination-only svy req'd: Yes No Post initial injection MIT req'd: Yes No APPROVED BY Approved by: COMMISSIONER THE COMMISSION Date: Comm. Comm. Sr Pet Eng Sr Pet Geo Sr Res Eng 10 yds P.O. Box 100360 Anchorage, Alaska, 99510-0360 Kuparuk River Field Torok Oil Pool 1888' FSL, 513' FWL, SENE S1 T12N R7E ADL025528 / ADL393883 (including stage data) 409' FSL, 273' FWL, NWSE S27 T13N R7E LONS 01-013 4724' FSL, 3061' FWL, SENW S21 T13N R7E 2560 / 5760 GL / BF Elevation above MSL (ft): 2290 1778 18. Casing Program: STATE OF ALASKA ALASKA OIL AND GAS CONSERVATION COMMISSION PERMIT TO DRILL 20 AAC 25.005 ConocoPhillips Alaska Inc.59-52-180 KRU 3T-613 714sks 10.7ppg,280sks 15.8ppg 1344sks 14ppg, 252sks 15.3ppg Specifications Top - Setting Depth - Bottom Cement Quantity, c.f. or sacks Casing Length Size Cement Volume MD Total Depth MD (ft):Total Depth TVD (ft):Plugs (measured):Effect. Depth MD (ft):Effect. Depth TVD (ft): Surface Conductor/Structural Liner Production Intermediate Perforation Depth MD (ft):Perforation Depth TVD (ft): 21. I hereby certify that the foregoing is true and the procedure approved herein will not be deviated from without prior written approval. Authorized Name: Authorized Title: Authorized Signature: Commission Use Only See cover letter for other requirements. es s N yp L l R S oooos N esss No ooo s N ooo D s s sD t 0 ooo : p s G S S 20 S ess s No o o s Nooo S s G y E es ss No ooo s o Form 10-401 Revised 3/2021 This permit is valid for 24 months from the date of approval per 20 AAC 25.005(g) By Grace Christianson at 8:38 am, Mar 12, 2025 A.Dewhurst 23APR25 Initial BOP test to 5000 psig; subsequent BOP test to 4000 psig Annular preventer test to 2500 psig BOPE testing on a 21-day interval is approved with the attached conditions Intermediate I cement evaluation may use SonicScope under the attached Conditions of Approval Surface casing LOT and annular LOT to the AOGCC as soon as available Cement logs must be reviewed with the AOGCC as soon as available and prior to running the production liner. X / ADL393884 5,031' Diverter variance granted per 20 AAC 25.035(h)(2) 50-103-20914-00-00225-036 DSR-3/24/25VTL 04/24/2025 *&: Jessie L. Chmielowski Digitally signed by Jessie L. Chmielowski Date: 2025.04.24 13:59:06 -08'00' 04/24/25 04/24/25 RBDMS JSB 042525 <Zhϯ^ͲϳϮϭ Conditions of Approval: Approval is granted to run the LWD-Sonic on upcoming well with the following provisions: 1. CPAI will provide a written log evaluation/interpretation to the AOGCC along with the log as soon as they become available. The evaluation is to include/highlight the intervals of competent cement that CPAI is using to meet the objective requirements for annular isolation, reservoir isolation, or confining zone isolation etc. Providing the log without an evaluation/interpretation is not acceptable. 2. LWD sonic logs must show free pipe and Top of Cement, just as the e-line log does. CPAI must start the log at a depth to ensure the free pipe above the TOC is captured as well as the TOC. Starting the log below the actual TOC based on calculations predicting a different TOC will not be acceptable. 3. CPAI will provide a cement job summary report and evaluation along with the cement log and evaluation to the AOGCC when they become available 4. CPAI will provide the results of the FIT when available. 5. Depending on the cement job results indicated by the cement job report, the logs and the FIT, remedial measures or additional logging may be required. .58'66 CPAI’s request to allow BOPE testing on a 21-day interval is approved with the following conditions: - CPAI must continue to implement the Between Wells Maintenance Program as approved by AOGCC. - The initial test after rigging up BOPE to drill a well must be to the rated working pressure as provided in API Standard 53. - CPAI is encouraged to take advantage of opportunities to test within the 21-day time limit. - CPAI must adhere to original equipment manufacturer recommendations and replacement parts for BOPE. - Requests for extensions beyond 21 days must include justification with supporting information demonstrating the additional time is necessary for well control purposes or to mitigate a stuck drill string. ConocoPhillips Alaska, Inc. Post Office Box 100360 Anchorage, Alaska 99510-0360 Telephone 907-276-1215 March 11, 2025 Alaska Oil and Gas Conservation Commission 333 West 7th Avenue, Suite 100 Anchorage, Alaska 99501 Re: Application for Permit to Drill 3T-613 Dear Sir or Madam: ConocoPhillips Alaska, Inc. hereby applies for a Permit to Drill an onshore Moraine Producer well from the 3T drilling pad. The intended spud date for this well is 5/10/2025. It is intended that Doyon 142 be used to drill the well. 3T-613 will utilize a 13-1/2” surface hole drilled to TD and 10-3/4” casing will be set and cemented to surface. As noted in section 4 of the attached proposed drilling program, the low maximum anticipated surface pressure of the well allows use of a three preventer BOPE per 20 AAC 25.035 (e) (1) (A) (i-iii). The fourth preventer will contain solid body pipe rams that will be sized for the intermediate casing string. The 9-7/8” intermediate hole will be drilled and topset the Moraine reservoir. A 7- 5/8” casing string will be set and cemented from TD to secure the shoe and cover 500’ or 250’TVD above any hydrocarbon- bearing zones (Torok). The production interval will be comprised of a 6-1/2” horizontal hole that will be landed and geo-steered in the Moraine formation. The well will be completed as an uncemented, fracture stimulated producer with 4-1/2” liner, and frac sleeves. The upper completion will include a production packer with GLM’s and a downhole guage tied back to surface. Please find attached the information required by 20 ACC 25.005 (a) and (c) for your review. Pertinent information attached to this application includes the following: 1. Form 10-401 APPLICATION FOR Permit to Drill per 20 ACC 25.005 (a) 2. A proposed drilling program 3. A proposed completion diagram 4. A drilling fluids program summary 5. Pressure information as required by 20 ACC 25.035 (d)(2) 6. Directional drilling / collision avoidance information as required by 20 ACC 25.050 (b) It is requested that a waiver of the diverter requirement under 20 AAC 25.035 (h) (2) is granted. At 3T, 3 penetrations have been completed and one more penetration is planned prior to 3T-613 and there has not been a significant indication of shallow gas or gas hydrates through the surface hole interval. A variance is also requested for a BOPE test interval of 21 days for this project. Doyon 142 is a strong participant in the CPAI BOPE between well maintenance program reflected by low failure rates in BOP tests since its entry in the CPAI fleet. The variance allows effective drilling and completion of problematic intermediate shale sections and efficient management of losses in the production sections when they are encountered. Information pertinent to the application that is presently on file at the AOGCC: 1. Diagrams of the BOP equipment and choke manifold lay out as required by 20 ACC 25.035 (a) and (b). 2. A description of the drilling fluids handling system. 3. Diagram of riser set up. If you have any questions or require further information, please contact Weifeng Dai at 907-265-6936 (Weifeng.Dai@conocophillips.com) or Greg Hobbs at 907-263-4749. Sincerely, cc: 3T-613 Well File / Jenna Taylor ATO 1560 Will Earhart ATO 1552 Weifeng Dai Chris Brillon ATO 1548 Drilling Engineer Roland Kirschner ATO 636 waiver of the diverter requirement under 20 AAC 25.035 (h) (2) Application for Permit to Drill, 3T-613 Saved: 11-Mar-25 3T-613 PTD Page 1 of 9 Printed: 11-Mar-25 3T-613 Application for Permit to Drill Document Table of Contents 1. Well Name (Requirements of 20 AAC 25.005 (f)) ........................................................................................................ 2 2. Location Summary (Requirements of 20 AAC 25.005(c)(2)) ......................................................................................... 2 3. Proposed Drilling Program (Requirements of 20 AAC 25.005(c)(13)) ........................................................................ 4 4. Blowout Prevention Equipment (Requirements of 20 AAC 25.005(c)(3)) ............................................................. 4 5. Diverter System (Requirements of 20 AAC 25.005(c)(7)) ..................................................................................... 5 6. MASP Calculations (Requirements of 20 AAC 25.005(c)(4)) ................................................................................ 5 7. Procedure for Conducting Formation Integrity Tests (Requirements of 20 AAC 25.005(c)(5)) ............................ 6 8. Casing and Cementing Program (Requirements of 20 AAC 25.005(c)(6)) ........................................................... 6 9. Drilling Fluid Program (Requirements of 20 AAC 25.005(c)(8)) .................................................................................. 7 10. Abnormally Pressured Formation Information (Requirements of 20 AAC 25.005 (c)(9)) ........................................ 8 11. Seismic Analysis (Requirements of 20 AAC 25.005 (c)(10)) ................................................................................... 8 12. Seabed Condition Analysis (Requirements of 20 AAC 25.005 (c)(11)) ................................................................... 8 13. Evidence of Bonding (Requirements of 20 AAC 25.005 (c)(12)) ............................................................................. 8 14. Discussion of Mud and Cuttings Disposal and Annular Disposal (Requirements of 20 AAC 25.005 (c)(14)) ......... 8 15. Drilling Hazards Summary ................................................................................................................................. 8 16. Proposed Completion Schematic ..................................................................................................................... 10 1. Well Name (Requirements of 20 AAC 25.005 (f)) The well for which this application is submitted will be designated as 3T-613 2. Location Summary (Requirements of 20 AAC 25.005(c)(2)) Location at Surface 1,888 FSL, 513 FWL, SENE S1 T12N R7E, UM NAD 1927 Northings: 467723 Eastings:6003614 RKB Elevation 51.1’AMSL Pad Elevation 12’AMSL Top of Productive Horizon (Heel) 409‘ FSL, 273‘ FWL, NWSE S27 T13N R7E, UM NAD 1927 Northings: 460654 Eastings: 6012729 Measured Depth, RKB: 13,706 Total Vertical Depth, RKB: 5,008 Total Vertical Depth, SS: 4,957 Total Depth (Toe) 4724‘ FSL, 3061‘ FWL, SENW S21 T13N R7E, UM NAD 1927 Northings: 458193 Eastings: 6022336 Measured Depth, RKB: 23,634 Total Vertical Depth, RKB: 5,107 Total Vertical Depth, SS: 5,056 Pad Layout 3. Proposed Drilling Program (Requirements of 20 AAC 25.005(c)(13)) The proposed drilling program is listed below. Please refer to Attachment 3: Completion Schematic. 1. MIRU Doyon 142 onto 3T-613 2. Rig up and test diverter and riser, dewater cellar as needed. 3. Drill 13 1/2” hole to the surface casing point as per the directional plan (LWD program:GR/RES/GWD). 4. Run and cement 10 3/4” surface casing to surface. 5. Install BOPE with the following equipment/configuration:13-5/8” annular preventer, 7-5/8” FBR’s, blind ram and 2- 7/8”x5” VBR’s. a. See section 4 for ram configuration justification. 6. Test BOPE to 250 psi low / 5,000 psi high (24-48 hr regulatory notice). 7. Pick up and run in hole with 9 7/8” drilling BHA to drill the intermediate hole section. 8. Chart casing pressure test to 3,000 psi for 30 minutes. 9. Drill out shoe track and 20’ of new hole 10. Perform FIT/LOT. Max FIT to 18.0 ppg. Minimum LOT required to drill ahead is 11.0 ppg EMW. 11. Drill 9 7/8” hole to section TD, setting pipe 5 ft TVD into the top Moraine Reservoir. (LWD Program: GR/RES). 12. Run 7 5/8” casing and cement to a minimum of 250’ TVD above any hydrocarbon bearing zones (cementing schematic attached). Pressure test casing if possible on plug bump to 4000 psi. 13. Test BOPE to 250 psi low / 4,000 psi high (24-48 Regulatory notice). 14. Pick up and run in hole with 6 1/2” drilling BHA. Log top of cement with sonic tool in recorded mode. 15. Chart casing pressure test to 4,000 psi for 30 minutes if not tested on plug bump. 16. Drill out shoe track and 20 feet of new formation. 17. Perform LOT to a maximum of 16.0 ppg. Minimum acceptable leak-off value is 11.0 ppg EMW. 18. Drill 6 1/2” hole to section TD (LWD Program: GR/RES/Den/Neu/Sonic). 19. Pull out of hole with drilling BHA. Review cement job details and sonic log TOC. 20. Run 4 1/2” liner with toe valve, frac sleeves and swell packers and liner hanger to TD. 21. Run 4 1/2” upper completion with glass plug, production packer, chemical injection mandrel with cap string, downhole gauge, and gas lift mandrels. Space out and land tubing hanger with pre-installed and pre-tested BPV. 22. Pressure test hanger seals to 3,850 psi. 23. Pressure test against the glass plug to set production packer, test tubing to 3,850 psi, chart test. 24. Bleed tubing pressure to 2200 psi and test IA to 3,850 psi, chart test. 25. Install HP-BPV and test to 2500 psi. 26. Nipple down BOP. 27. Install tubing head adapter assembly. N/U tree and test to 5000 psi/10 minutes. 28. Freeze protect down tubing and annulus. 29. Secure well. Rig down and move out. Please note – This well will be frac’d 4. Blowout Prevention Equipment (Requirements of 20 AAC 25.005(c)(3)) Please reference BOP schematics on file for Doyon 142. Doyon 142 will use a BOPE stack equipped with an annular preventer, fixed 7 5/8” solid body rams, blind/shear rams and variable rams while drilling and running casing in the intermediate section of 3T-613. 3T-613 has a MASP of 1,773 psi in the intermediate hole section using the methodology in section 6 MASP calculations. With a MASP less than 3000 psi ConocoPhillips classifies the operation as a Class 2. Per 20AAC 25.035.e.a.A: For an operation with a maximum potential surface pressure of 3,000 psi or less, BOPE must have at least three preventers, including: i. One equipped with pipe rams that fit the size of drill pipe, tubing or casing begin used, except that pipe rams need not be sixed to bottom-hole assemblies and drill collars. ii. One with blind rams iii. One annular type Intermediate Drilling/ Casing x Annular Preventer (iii) x 7 5/8 Fixed Rams x Blind/Shear Rams (ii) x VBR’s (i) Production: x Annular Preventer (iii) x VBR’s (i) x Blind/Shear Rams (ii) x VBR’s (i) 5. Diverter System (Requirements of 20 AAC 25.005(c)(7)) It is requested that a waiver of the diverter requirement under 20 AAC 25.035 (h) (2) is granted. At 3T, 3 penetrations have been completed and one more penetration is planned prior to 3T-613 and there has not been a significant indication of shallow gas or gas hydrates through the surface hole interval. 6. MASP Calculations (Requirements of 20 AAC 25.005(c)(4)) (A) maximum downhole pressure and maximum potential surface pressure; Maximum Potential Surface Pressure (MPSP) is determined as the lesser of: Method 1: surface pressure at breakdown of the formation casing seat with a gas gradient to the surface Method 2: formation pore pressure at the next casing point less a gas gradient to the surface Method 2: formation pore pressure at the next casing point less a gas gradient to the surface Recommend granting variance. See attached emails for details. -A.Dewhurst 23APR25 At 3T, 3 penetrationsqq have been completed and one more penetration is planned prior to 3T-613 Method 1 Method 2 ܯܲܵܲ = [(ܨܩ × 0.052 )െ ܩܽݏ ܩݎܽ݀݅݁݊ݐ ] × ܸܶܦ ܯܲܵܲ = ܨܲܲ െ (ܩܽݏ ܩݎܽ݀݅݁݊ݐ) × ܸܶܦ Where: FG –Fracture gradient at the casing seat in lb/gal 0.052 – Conversion from lb/gal to psi/ft Gas Gradient –0.1 psi/ft TVD –True Vertical Depth of casing seat in ft RKB Where: FPP –Formation Pore Pressure at the next casing point Gas Gradient –0.1 psi/ft The following presents data used for calculation of Maximum Potential Surface Pressure (MPSP) while drilling: Section Hole Size Previous CSG Section TD MPSP psi MPSP MPSP Size MD TVD FG ppg Pore Pressure ppg | psi MD TVD Pore Pressure ppg | psi Method 1 psi Method 2 psi SURF 13.5 10.75 2704 2449 10.9 8.6 1,095 2704 2449 8.6 1,095 850 1,143 850 INT1 9 7/8 7.63 13215 5030 13.5 8.6 2,249 13215 5030 8.6 2,249 1,746 3,028 1,746 PROD 6 1/2 12.60 23634 5107 13 8.6 2,284 23634 5107 8.6 2,284 1,773 2,942 1,773 (B) data on potential gas zones; The planned wellbore is expected to enter the gas cap and the area is expected to be normally pressured (8.5-8.9 ppg). (C) data concerning potential causes of hole problems such as abnormally geo-pressured strata, lost circulation zones, and zones that have a propensity for differential sticking; Please see Drilling Hazards Summary 7. Procedure for Conducting Formation Integrity Tests (Requirements of 20 AAC 25.005(c)(5)) Drill out the casing shoe and perform LOT/FIT as per the procedure that ConocoPhillips Alaska has on file with the Commission. 8. Casing and Cementing Program (Requirements of 20 AAC 25.005(c)(6)) Casing and Cementing Program Csg/Tbg OD (in) Hole Size (in) Weight (lb/ft) Grade Conn. Cement Program 20 42 94 H40 Welded Cemented to surface with 10 yds slurry 10 3/4 13 1/2 45.50 L80 Hyd563 Cement to Surface 7 5/8 9 7/8 29.70 33.70 L80 P110-S Hyd563 250’ TVD or 500’ MD, whichever is greater, above upper most producing zone (Coyote) 4 1/2 6 1/2 12.60 P110-S Hyd563 Unemented liner with frac sleeves and swell packers 5107 planned wellbore is expected to enter the gas cap and the area is expected to be normally pressured (8.5-8.9 ppg). Cementing Calculations 10 3/4” Surface Casing run to 2,704’ MD / 2,449 ’ TVD Cement 2,704’ MD to 2,204’ (500’ of tail) with Class G + Add's@ 15.8 PPG, and from 2,204' to surface with 10.7 ppg Arctic Lite Crete. Assume 200% excess annular volume in permafrost and 50% excess below the permafrost (1,560’ MD), zero excess in 20” conductor. Lead 371 bbls => 714 sx of 10.7 ppg Class G + Add's @ 2.92 ft3 /sk Tail 56 bbls => 280 sx of 15.8ppg Class G + Add's @ 1.16 ft3/sk 7 5/8” Intermediate Casing run to 13,235’ MD / 5,015 ’ TVD Top of slurry is designed to be at 8,817’ MD, which is 500’ MD above the prognosis shallowest hydrocarbon bearing zone, Coyote. If a shallower hydrocarbon zone of producible volumes, is encountered while drilling, a 2-stage cement job will be performed to isolate this zone. Assume 40% excess annular volume. Lead 371 bbls => 1344 sx of 14 ppg Class G + Add's @ 1.55 ft3 /sk Tail 56 bbls => 252 sx of 15.3ppg Class G + Add's @ 1.25 ft3/sk 9. Drilling Fluid Program (Requirements of 20 AAC 25.005(c)(8)) Surface Intermediate Production Hole Size in. 13 1/2 9 7/8 6 1/2 Casing Size in. 10 3/4 7 5/8 4 1/2 Density PPG 8.6 – 9.8 9.0 – 9.6 10 – 11 PV cP 20-50 8-15 7-12 YP lb./100 ft2 30 - 80 20 - 30 15 - 30 Funnel Viscosity s/qt. 250 – 300 40-60 35-50 Initial Gels lb./100 ft2 30 - 50 8 - 15 5- 10 10 Minute Gels lb./100 ft2 50 - 70 <20 7 - 15 API Fluid Loss cc/30 min. N.C. – 15.0 < 10.0 < 6.0 HPHT Fluid Loss cc/30 min. N/A < 10.0 < 10.0 pH 9.5 – 10.0 9.5 – 10.0 9.5 – 10.5 Surface Hole: A water based spud mud will be used for the surface interval. Mud engineer to perform regular mud checks to maintain proper specifications The mud weight will be maintained at 9.8 ppg by use of solids control system and dilutions where necessary. Intermediate: Fresh water polymer mud system. Ensure good hole cleaning by pumping regular sweeps and maximizing fluid annular velocity. Maintain mud weight at or below 9.6 ppg for formation stability and be prepared to add loss circulation material if necessary. Good filter cake quality, hole cleaning and maintenance of low drill solids (by diluting as required) will all be important. The mud will be weighted up to 9.5 ppg before pulling out of the hole. Production Hole: The horizontal production interval will be drilled with an NAF mud system weighted to 10 – 11 ppg. MPD will be available for adding backpressure during connections if necessary. Diagram of Doyon 142 Mud System on file. Drilling fluid practices will be in accordance with appropriate regulations stated in 20 AAC 25.033. 10. Abnormally Pressured Formation Information (Requirements of 20 AAC 25.005 (c)(9)) N/A - Application is not for an exploratory or stratigraphic test well. 11. Seismic Analysis (Requirements of 20 AAC 25.005 (c)(10)) N/A - Application is not for an exploratory or stratigraphic test well. 12. Seabed Condition Analysis (Requirements of 20 AAC 25.005 (c)(11)) N/A - Application is not for an offshore well. 13. Evidence of Bonding (Requirements of 20 AAC 25.005 (c)(12)) Evidence of bonding for ConocoPhillips Alaska, Inc. is on file with the Commission. 14. Discussion of Mud and Cuttings Disposal and Annular Disposal (Requirements of 20 AAC 25.005 (c)(14)) Waste fluids and cuttings generated during the drilling process will be disposed of by hauling the fluids to a KRU Class II disposal well at the 1B Facility. If needed, excess cuttings generated will be hauled to Milne Point or Prudhoe Bay Grind and Inject Facility for temporary storage and eventual processing for injection down an approved disposal well, or stored, tested for hazardous substances, and (if free of hazardous substances) used on pads and roads in the Kuparuk area in accordance with a permit from the State of Alaska. 15. Drilling Hazards Summary 13 1/2" Hole / 10 3/4” Casing Interval Event Risk Level Mitigation Strategy Conductor Broach Low Monitor cellar continuously during interval. Well Collision Low Follow real time surveys very closely, gyro survey as needed to ensure survey accuracy. Gas Hydrates Low If observed – control drill, reduce pump rates and circulating time, reduce mud temperatures Hole Swabbing on Trips Moderate Trip speeds, proper hole filling (use of trip sheets), pumping out Washouts/Hole Sloughing Low Cool mud temperatures, minimize circulating times when possible Running sands and gravels Low Maintain planned mud properties, increase mud weight, use weighted sweeps 9 7/8” Hole /7 5/8” Liner - Casing Interval Event Risk Level Mitigation Strategy Sloughing shale / Tight hole / Stuck Pipe Low Good hole cleaning, pre-treatment with LCM, stabilized BHA, maintain planned mud weights and adjust as needed, real time equivalent circulating density (ECD) monitoring Lost circulation Moderate Reduce pump rates, reduce trip speeds, real time ECD monitoring, mud rheology, add lost circulation material Hole swabbing on trips Moderate Reduce trip speeds, condition mud properties, proper hole filling, pump out of hole, real time ECD monitoring, Liner will be in place at TD Abnormal Reservoir Pressure (Coyote / K3) Low Well control drills, check for flow during connections, increase mud weight if necessary 6 1/2” Hole / 4 1/2” Liner - Horizontal Production Hole Event Risk Level Mitigation Strategy Lost circulation Moderate Reduce pump rates, real time ECD monitoring, maintain mud rheology, add lost circulation material Hole swabbing on trips Moderate Reduce trip speeds, condition mud properties, proper hole filling, pump out of hole, real time ECD monitoring Abnormal Reservoir Pressure Low Well control drills, check for flow during connections, increased mud weight Differential Sticking Moderate Uniform reservoir pressure along lateral, keep pipe moving, control mud weight Running Liner to Bottom Moderate Properly clean hole on the trip out with BHA, perform clean out run if necessary, utilize super sliders for weight transfer if needed, monitor T&D real time Well Proximity Risks: 3T is a multi-well pad, with only a few existing wells. Directional drilling / collision avoidance information as required by AOGCC 20 ACC 25.050 (b) is provided in the following attachments. Drilling Area Risks: Reservoir Pressure: Unlikely to encounter any abnormal pressure, however, the rig will be prepared to weight up if required. Weak sand stringers could be present in the overburden. LCM material will be available to seal in losses in the intermediate section. The overburden logs will be evaluated to ensure no hydrocarbon bearing zones are above the known Coyote. If identified, the primary intermediate cement job will be replanned to cover the zone as per the agency regulations. Lost Circulation: Standard LCM material and well bore strengthening pills are expected to be effective in dealing with lost circulation if needed. Good drilling practices will be stressed to minimize the potential of taking swabbed kicks. 16. Proposed Completion Schematic 39 500 500 800 800 1100 1100 1500 1500 2000 2000 3000 3000 5000 5000 8000 8000 12000 12000 16000 16000 19000 19000 23710 3T-613 wp07.1 Plan Summary 0 4 Dogleg Severity0 3500 7000 10500 14000 17500 21000 Measured Depth 10-3/4" Surface Casing 7-5/8" Intermediate Casing 4-1/2" Production Liner 30.0 30.0 60.0 60.0 0 90 180 270 30 210 60 240 120 300 150 330 Travelling Cylinder Azimuth (TFO+AZI) [°] vs Travelling Cylinder Separation [60 usft/in] 39100200300 400 39100200300 400 39100200300 400 39100200300400500600699 798 897 996 1093 1191 1289 3T-612 39100200300 400 3T-616 39100200300 400 39100200300 400 39100200300400500600 3T-610 wp05 391002003004005006006997988979951093 3T-611 wp08.1 39100200300400500 599 697 793 3T-614 wp06 3910020030040050060170180190110011102120213031403150316041705 3T-615 wp05 0 3000 True Vertical Depth0 3000 6000 9000 12000 15000 18000 21000 Vertical Section at 332.77° 10-3/4" Surface Casing 7-5/8" Intermediate Casing 4-1/2" Production Liner 18 35 Centre to Centre Separation0 425 850 1275 1700 2125 2550 2975 Measured Depth Equivalent Magnetic Distance DDI 7.320 SURVEY PROGRAM Date: 2019-07-03T00:00:00 Validated: Yes Version: Depth From Depth To Survey/Plan Tool 39.00 1600.00 3T-613 wp07.1 (3T-613) r.5 SDI_URSA1 1600.00 2390.00 3T-613 wp07.1 (3T-613) MWD+IFR2+SAG+MS 2390.00 13230.00 3T-613 wp07.1 (3T-613) MWD+IFR2+SAG+MS 13230.00 23633.49 3T-613 wp07.1 (3T-613) MWD+IFR2+SAG+MS Ground / 12.00 CASING DETAILS TVD MD Name 2449.09 2704.55 10-3/4" Surface Casing 5015.32 13215.26 7-5/8" Intermediate Casing 5030.97 23633.49 4-1/2" Production Liner Mag Model & Date: BGGM2024 15-May-25 Magnetic North is 13.75° East of True North (Magnetic Declinatio Mag Dip & Field Strength: 80.61° 57175.96nT SECTION DETAILS Sec MD Inc Azi TVD +N/-S +E/-W Dleg TFace VSect Target Annotation 1 39.00 0.00 0.00 39.00 0.00 0.00 0.00 0.00 0.00 2 300.00 0.00 0.00 300.00 0.00 0.00 0.00 0.00 0.00 Start Build 1.00000 3 500.00 2.00 320.00 499.96 2.67 -2.24 1.00 320.00 3.40 Start Build 2.00000 4 1369.95 19.40 320.00 1351.50 125.92 -105.66 2.00 0.00 160.32 Start 106.01880 hold at 1369.94567 MD 5 1475.96 19.40 320.00 1451.50 152.90 -128.30 0.00 0.00 194.66 Start DLS 2.50000 TFO 5.00000 6 2557.78 46.40 323.14 2351.50 612.48 -485.42 2.50 5.00 766.71 Start 20.00000 hold at 2557.77749 MD 7 2577.78 46.40 323.14 2365.29 624.07 -494.11 0.00 0.00 780.99 Start DLS 2.50000 TFO -3.12510 8 3237.78 69.46 321.46 2713.40 1062.93 -834.62 3.50 -4.00 1327.03 9 3445.13 76.71 321.44 2773.69 1217.98 -958.16 3.50 -0.16 1521.42 1012951.13 76.71 321.44 4958.34 8452.45 -6724.78 0.00 0.0010592.73 11 13603.24 81.00 334.00 5084.83 8992.36 -7065.22 2.00 72.1111228.59 1213803.24 86.00 334.00 5107.46 9170.91 -7152.30 2.50 0.0011427.19 3T Flute T01 103124 1313823.24 86.00 334.00 5108.86 9188.84 -7161.05 0.00 0.0011447.14 1414246.05 91.12 345.61 5119.50 9584.74 -7306.62 3.00 66.4111865.77 1515113.21 91.12 345.61 5102.49 10424.54 -7522.07 0.00 0.0012711.09 1615189.45 90.00 345.40 5101.74 10498.35 -7541.15 1.50 -169.3712785.45 3T Flute T02 103124 1715272.57 88.81 345.78 5102.60 10578.85 -7561.84 1.50 162.4112866.49 1816629.60 88.81 345.78 5130.75 11894.00 -7895.19 0.00 0.0014188.42 1916708.91 90.00 345.83 5131.57 11970.88 -7914.63 1.50 2.5614265.68 3T Flute T03 103124 2016792.53 91.25 345.86 5130.66 12051.95 -7935.08 1.50 1.3814347.12 21 17179.92 91.25 345.86 5122.18 12427.52 -8029.69 0.00 0.0014724.36 2217292.23 93.50 345.84 5117.52 12536.32 -8057.12 2.00 -0.5114833.65 3T Flute T04 103124 2317465.10 96.96 345.77 5101.77 12703.19 -8099.34 2.00 -1.2015001.34 2417498.31 96.96 345.77 5097.75 12735.14 -8107.44 0.00 0.0015033.46 2517671.14 93.50 345.78 5082.00 12901.95 -8149.73 2.00 179.7915201.14 3T Flute T05 103124 2617805.18 90.82 345.79 5076.95 13031.78 -8182.62 2.00 179.7915331.62 2721074.41 90.82 345.79 5030.20 16200.65 -8985.08 0.00 0.0018516.49 28 21129.03 90.00 345.79 5029.81 16253.60 -8998.49 1.50 -180.0018569.71 3T Flute T06 103124 29 21203.73 88.88 345.79 5030.54 16326.00 -9016.83 1.50 -180.0018642.48 30 21925.05 88.88 345.79 5044.64 17025.11 -9193.86 0.00 0.0019345.12 31 22037.09 90.00 345.79 5045.74 17133.72 -9221.37 1.00 0.0219454.27 3T Flute T07 103124 32 22076.39 90.39 345.79 5045.61 17171.83 -9231.02 1.00 0.2219492.57 33 23459.70 90.39 345.79 5036.11 18512.78 -9570.54 0.00 0.0020840.27 3423633.50 93.00 345.79 5030.97 18681.17 -9613.18 1.50 -0.0321009.51 3T Flute T09 103124 FORMATION TOP DETAILS TVDPath Formation 1378.00 Top Ugnu C 1596.80 Top Ugnu B 1698.00 Base Perm 1722.70 Top Ugnu A 2017.00 Top West Sak 2432.10 Base West Sak 2550.00 C-80 2617.40 C-50 2875.40 C-40 3791.30 C-35 4123.20 Coyote 4204.90 Base Coyote 5008.10 Top Moraine 5098.60 Moraine Blue By signing this I acknowledge that I have been informed of all risks, checked that the data is correct, ensured it's completeness, and all surroundingwells are assigned to the proper position, and I approve the scan and collision avoidance plan as set out in the audit pack.I approve it as the basiis for the final well plan and wellsite drawings. I also acknowledge that unless notified otherwise all targets have a 100 feet lateral tolerance. Prepared by Checked by Accepted by Approved by Plan 12+39 @ 51.00usft (D142) -3000 0 3000 6000 9000True Vertical Depth0 3000 6000 9000 12000 15000 18000 21000 Vertical Section at 332.77° 10-3/4" Surface Casing 7-5/8" Intermediate Casing 4-1/2" Production Liner 1 0 0 0 2 0 0 0 30004000500060007000800090001000011000120001300014000150001600017000180001900020000210002200023000236330° 3 0 °60°77°90°91°89°91°91°89°90°3T-613 wp07.1Top Ugnu C Top Ugnu B Base PermTop Ugnu A Top West Sak Base West Sak C-80 C-50C-40 C-35 Coyote Base Coyote Top Moraine Moraine Blue 3T-613 wp07.1 9:20, March 11 2025Section View 0 3500 7000 10500 14000 17500 South(-)/North(+)-17500 -14000 -10500 -7000 -3500 0 3500 7000 West(-)/East(+) 10-3/4" Surface Casing 7-5/8" Intermediate Casing 4-1/2" Production Liner 2004006008001000120014001600180020002200240026002800300032003400360038004000420044004600480050005031 3 T -6 1 3 w p 0 7 .1 3T-613 wp07.1 While drilling production section, stay within 100 feet laterally of plan, unless notified otherwise. 9:24, March 11 20253ODQ9LHZ 0.00 0.75 1.50 2.25 3.00 3.75 4.50 5.25 6.00 6.75 7.50 Separation Factor0 1250 2500 3750 5000 6250 7500 8750 10000 11250 12500 13750 15000 16250 17500 18750 20000 21250 22500 Measured Depth (2500 usft/in) 3T-612/3T-612 3T-616/3T-616 3T-616/3T-616PB1 3T-621/3T-621 Plan: 3T-617 Eberly (P)/3T-617 wp07.1 Plan: 3T-619 Grewingk (I)/3T-619 wp07.1 Plan: 3T-622 Hayes (P)/3T-622 wp05 v5 STOP Drilling Take Immediate Action Caution - Monitor Closely Normal Operations Project: Kuparuk River Unit_2 Site: Kuparuk 3T Pad Well: 3T-613 Wellbore: 3T-613 Design: 3T-613 wp07.1 0 35 Centre to Centre Separation0 500 1000 1500 2000 2500 Partial Measured Depth3T-6123T-6163T-616PB13T-616PB23T-610 wp053T-611 wp08.13T-614 wp063T-615 wp053T-6163T-616PB13T-616PB2Equivalent Magnetic Distance 3T-613 wp07.1 Ladder View 0 150 300 Centre to Centre Separation0 3500 7000 10500 14000 17500 21000 Measured DepthNDST-02NDST-02PB1Nuna 13T-6033T-6083T-6123T-6163T-616PB13T-616PB23T-6213T-601 wp05 v53T-602 wp05 v53T-604 wp05 v53T-605 (ST) wp093T-605PH wp033T-606 wp083T-607 wp053T-609 wp063T-610 wp053T-611 wp08.13T-614 wp063T-615 wp053T-617 wp07.13T-618 wp05 v53T-619 wp07.13T-620 wp05 v53T-622 wp05 v53T-6163T-616PB13T-616PB2Equivalent Magnetic Distance SURVEY PROGRAM Depth From Depth To Survey/Plan Tool 39.00 1600.00 3T-613 wp07.1 (3T-613) r.5 SDI_URSA1 1600.00 2390.00 3T-613 wp07.1 (3T-613) MWD+IFR2+SAG+MS 2390.0013230.00 3T-613 wp07.1 (3T-613) MWD+IFR2+SAG+MS 13230.00 23633.49 3T-613 wp07.1 (3T-613) MWD+IFR2+SAG+MS 9:35, March 11 2025 CASING DETAILS TVD MD Name 2449.09 2704.55 10-3/4" Surface Casing 5015.32 13215.26 7-5/8" Intermediate Casing 5030.97 23633.49 4-1/2" Production Liner 39 500 500 800 800 1100 1100 1500 1500 2000 2000 3000 3000 5000 5000 8000 8000 12000 12000 16000 16000 19000 19000 23710 3T-613 wp07.1 TC View 30 30 60 60 90 90 120 120 150 150 0 90 180 270 30 210 60 240 120 300 150 330 Travelling Cylinder Azimuth (TFO+AZI) [°] vs Travelling Cylinder Separation [60 usft/in] 13333 13425 1351613553 Nuna 1 39100200300400499599698797895 993 1091 1188 3T-608 39100200300400500600699 798 897 996 1093 1191 1289 1386 1485 1582 1678 1774 1869 1964 2058 2152 39100200300 400 499 597 694 790 885 977 39100200300 400 499 597 694 790 885 977 39100200300 400 499 597 694 790 885 977 100200300400499 3T-605 (ST) wp09 100200300400499 100200300400499598697 795 3T-606 wp08 39100200300400500599698798896 995 3T-607 wp05 39100200300400500599699798 897995 10931191 1288 1385 3T-609 wp063910020030040050060069979989899810971196 1294 1393 1492 1590 3T-610 wp05 3910020030040050060069979889799510931191128913871486158316791775187119662060 2155 3T-611 wp08.1 39100200300400500 599 697 793 887 978 1065 3T-614 wp06 39100200300400500601701801901100111021202130314031503160417051806190820102111221423162419252226262733 3T-615 wp05 391002003004005016017018029021002110212031303140315031603170318031902 2002 2101 2200 2299 2397 24953T-617 wp07.1 39100200300400501601701802902100311031204130414041504160517051806 3T-618 wp05 v5 39100200300 400 499 597 694 790 885 977 3T-616 39100200300 400 499 597 694 790 885 977 39100200300 400 499 597 694 790 885 977 SURVEY PROGRAM Date: 2019-07-03T00:00:00 Validated: Yes Version: From To Tool 39.00 1600.00 r.5 SDI_URSA1 1600.00 2390.00 MWD+IFR2+SAG+MS 2390.00 13230.00 MWD+IFR2+SAG+MS 13230.00 23633.49 MWD+IFR2+SAG+MS CASING DETAILS TVD MD Name 2449.09 2704.55 10-3/4" Surface Casing 5015.32 13215.26 7-5/8" Intermediate Casing 5030.97 23633.49 4-1/2" Production Liner SECTION DETAILS Sec MD Inc Azi TVD +N/-S +E/-W Dleg TFace VSect Target Annotation 1 39.00 0.00 0.00 39.00 0.00 0.00 0.00 0.00 0.00 2 300.00 0.00 0.00 300.00 0.00 0.00 0.00 0.00 0.00 Start Build 1.00000 3 500.00 2.00 320.00 499.96 2.67 -2.24 1.00 320.00 3.40 Start Build 2.00000 4 1369.95 19.40 320.00 1351.50 125.92 -105.66 2.00 0.00 160.32 Start 106.01880 hold at 1369.94567 MD 5 1475.96 19.40 320.00 1451.50 152.90 -128.30 0.00 0.00 194.66 Start DLS 2.50000 TFO 5.00000 6 2557.78 46.40 323.14 2351.50 612.48 -485.42 2.50 5.00 766.71 Start 20.00000 hold at 2557.77749 MD 7 2577.78 46.40 323.14 2365.29 624.07 -494.11 0.00 0.00 780.99 Start DLS 2.50000 TFO -3.12510 8 3237.78 69.46 321.46 2713.40 1062.93 -834.62 3.50 -4.00 1327.03 9 3445.13 76.71 321.44 2773.69 1217.98 -958.16 3.50 -0.16 1521.42 1012951.13 76.71 321.44 4958.34 8452.45 -6724.78 0.00 0.0010592.73 11 13603.24 81.00 334.00 5084.83 8992.36 -7065.22 2.00 72.1111228.59 1213803.24 86.00 334.00 5107.46 9170.91 -7152.30 2.50 0.0011427.19 3T Flute T01 103124 1313823.24 86.00 334.00 5108.86 9188.84 -7161.05 0.00 0.0011447.14 1414246.05 91.12 345.61 5119.50 9584.74 -7306.62 3.00 66.4111865.77 1515113.21 91.12 345.61 5102.49 10424.54 -7522.07 0.00 0.0012711.09 1615189.45 90.00 345.40 5101.74 10498.35 -7541.15 1.50 -169.3712785.45 3T Flute T02 103124 1715272.57 88.81 345.78 5102.60 10578.85 -7561.84 1.50 162.4112866.49 1816629.60 88.81 345.78 5130.75 11894.00 -7895.19 0.00 0.0014188.42 1916708.91 90.00 345.83 5131.57 11970.88 -7914.63 1.50 2.5614265.68 3T Flute T03 103124 2016792.53 91.25 345.86 5130.66 12051.95 -7935.08 1.50 1.3814347.12 21 17179.92 91.25 345.86 5122.18 12427.52 -8029.69 0.00 0.0014724.36 2217292.23 93.50 345.84 5117.52 12536.32 -8057.12 2.00 -0.5114833.65 3T Flute T04 103124 2317465.10 96.96 345.77 5101.77 12703.19 -8099.34 2.00 -1.2015001.34 2417498.31 96.96 345.77 5097.75 12735.14 -8107.44 0.00 0.0015033.46 2517671.14 93.50 345.78 5082.00 12901.95 -8149.73 2.00 179.7915201.14 3T Flute T05 103124 2617805.18 90.82 345.79 5076.95 13031.78 -8182.62 2.00 179.7915331.62 2721074.41 90.82 345.79 5030.20 16200.65 -8985.08 0.00 0.0018516.49 28 21129.03 90.00 345.79 5029.81 16253.60 -8998.49 1.50 -180.0018569.71 3T Flute T06 103124 29 21203.73 88.88 345.79 5030.54 16326.00 -9016.83 1.50 -180.0018642.48 30 21925.05 88.88 345.79 5044.64 17025.11 -9193.86 0.00 0.0019345.12 31 22037.09 90.00 345.79 5045.74 17133.72 -9221.37 1.00 0.0219454.27 3T Flute T07 103124 32 22076.39 90.39 345.79 5045.61 17171.83 -9231.02 1.00 0.2219492.57 33 23459.70 90.39 345.79 5036.11 18512.78 -9570.54 0.00 0.00 20840.27 34 23633.50 93.00 345.79 5030.97 18681.17 -9613.18 1.50 -0.0321009.51 3T Flute T09 103124 3T-613 wp07.1 AC Flipbook SURVEY PROGRAM Depth From Depth To Tool 39.00 1600.00 r.5 SDI_URSA1 1600.00 2390.00 MWD+IFR2+SAG+MS 2390.00 13230.00 MWD+IFR2+SAG+MS 13230.00 23633.49 MWD+IFR2+SAG+MS CASING DETAILS TVD MD Name 2449.09 2704.55 10-3/4" Surface Casing 5015.32 13215.26 7-5/8" Intermediate Casing 5030.97 23633.49 4-1/2" Production Liner 15 15 30 30 45 45 60 60 75 75 90 90 0 90 180 270 30 210 60 240 120 300 150 330 Travelling Cylinder Azimuth (TFO+AZI) [°] vs Travelling Cylinder Separation [30 usft/in] 39100200300400499 3T-608 39100200300400500 600 699 798 897 996 1093 1191 1289 1386 1485 1582 1678 3T-612 39100200300 400 499 597 694 39100200300 400 499 597 694 39100200300 400 499 597 694 39100200300400500599699 798 897 3T-609 wp06 39100200300400500600699799 898 998 1097 3T-610 wp05 39100200300400500 600 699 798 897 995 1093 1191 1289 1387 1486 3T-611 wp08.1 39100200300400 500 599 697 793 887 3T-614 wp06 39100200300400500601701801901100111021202130314031503160417051806 1908 2010 2111 2214 3T-615 wp05 3910020030040050160170180290210021102120313031403150316031703 1803 3T-617 wp07.1 39100200300400501601 3T-618 wp05 v5 39100200300 400 499 597 694 3T-616 39100200300 400 499 597 694 39100200300 400 499 597 694 39 500 500 800 800 1100 1100 1500 1500 2000 2000 3000 3000 5000 5000 8000 8000 12000 12000 16000 16000 19000 19000 23710 From Colour To MD 39.00 To 2800.00 MD Azi TFace 39.00 0.00 0.00 300.00 0.00 0.00 500.00 320.00 320.00 1369.95 320.00 0.00 1475.96 320.00 0.00 2557.78 323.14 5.00 2577.78 323.14 0.00 3237.78 321.46 -4.00 3445.13 321.44 -0.16 12951.13 321.44 0.00 13603.24 334.00 72.11 13803.24 334.00 0.00 13823.24 334.00 0.00 14246.05 345.61 66.41 15113.21 345.61 0.00 15189.45 345.40 -169.37 15272.57 345.78 162.41 16629.60 345.78 0.00 16708.91 345.83 2.56 16792.53 345.86 1.38 17179.92 345.86 0.00 17292.23 345.84 -0.51 17465.10 345.77 -1.20 17498.31 345.77 0.00 17671.14 345.78 179.79 17805.18 345.79 179.79 21074.41 345.79 0.00 21129.03 345.79 -180.00 21203.73 345.79 -180.00 21925.05 345.79 0.00 22037.09 345.79 0.02 22076.39 345.79 0.22 23459.70 345.79 0.00 23633.50 345.79 -0.03 3T-613 wp07.1 AC Flipbook SURVEY PROGRAM Depth From Depth To Tool 39.00 1600.00 r.5 SDI_URSA1 1600.00 2390.00 MWD+IFR2+SAG+MS 2390.00 13230.00 MWD+IFR2+SAG+MS 13230.00 23633.49 MWD+IFR2+SAG+MS CASING DETAILS TVD MD Name 2449.09 2704.55 10-3/4" Surface Casing 5015.32 13215.26 7-5/8" Intermediate Casing 5030.97 23633.49 4-1/2" Production Liner 45 45 90 90 135 135 180 180 225 225 270 270 0 90 180 270 30 210 60 240 120 300 150 330 Travelling Cylinder Azimuth (TFO+AZI) [°] vs Travelling Cylinder Separation [90 usft/in] 12671 12768 12865 12961 13054 13147Nuna 1 2700 3T-612 27062793288029673053 3T-611 wp08.1 27332841 2950305931683277 3386 3490 3587 3T-615 wp05 2787 2883 2978 3072 3165 3256 3T-617 wp07.1 39 500 500 800 800 1100 1100 1500 1500 2000 2000 3000 3000 5000 5000 8000 8000 12000 12000 16000 16000 19000 19000 23710 From Colour To MD 2700.00 To 13300.00 MD Azi TFace 39.00 0.00 0.00 300.00 0.00 0.00 500.00 320.00 320.00 1369.95 320.00 0.00 1475.96 320.00 0.00 2557.78 323.14 5.00 2577.78 323.14 0.00 3237.78 321.46 -4.00 3445.13 321.44 -0.16 12951.13 321.44 0.00 13603.24 334.00 72.11 13803.24 334.00 0.00 13823.24 334.00 0.00 14246.05 345.61 66.41 15113.21 345.61 0.00 15189.45 345.40 -169.37 15272.57 345.78 162.41 16629.60 345.78 0.00 16708.91 345.83 2.56 16792.53 345.86 1.38 17179.92 345.86 0.00 17292.23 345.84 -0.51 17465.10 345.77 -1.20 17498.31 345.77 0.00 17671.14 345.78 179.79 17805.18 345.79 179.79 21074.41 345.79 0.00 21129.03 345.79 -180.00 21203.73 345.79 -180.00 21925.05 345.79 0.00 22037.09 345.79 0.02 22076.39 345.79 0.22 23459.70 345.79 0.00 23633.50 345.79 -0.03 3T-613 wp07.1 AC Flipbook SURVEY PROGRAM Depth From Depth To Tool 39.00 1600.00 r.5 SDI_URSA1 1600.00 2390.00 MWD+IFR2+SAG+MS 2390.00 13230.00 MWD+IFR2+SAG+MS 13230.00 23633.49 MWD+IFR2+SAG+MS CASING DETAILS TVD MD Name 2449.09 2704.55 10-3/4" Surface Casing 5015.32 13215.26 7-5/8" Intermediate Casing 5030.97 23633.49 4-1/2" Production Liner 45 45 90 90 135 135 180 180 225 225 270 270 0 90 180 270 30 210 60 240 120 300 150 330 Travelling Cylinder Azimuth (TFO+AZI) [°] vs Travelling Cylinder Separation [90 usft/in] 13240 13333 134251351613553 Nuna 1 39 500 500 800 800 1100 1100 1500 1500 2000 2000 3000 3000 5000 5000 8000 8000 12000 12000 16000 16000 19000 19000 23710 From Colour To MD 13200.00 To 23635.00 MD Azi TFace 39.00 0.00 0.00 300.00 0.00 0.00 500.00 320.00 320.00 1369.95 320.00 0.00 1475.96 320.00 0.00 2557.78 323.14 5.00 2577.78 323.14 0.00 3237.78 321.46 -4.00 3445.13 321.44 -0.16 12951.13 321.44 0.00 13603.24 334.00 72.11 13803.24 334.00 0.00 13823.24 334.00 0.00 14246.05 345.61 66.41 15113.21 345.61 0.00 15189.45 345.40 -169.37 15272.57 345.78 162.41 16629.60 345.78 0.00 16708.91 345.83 2.56 16792.53 345.86 1.38 17179.92 345.86 0.00 17292.23 345.84 -0.51 17465.10 345.77 -1.20 17498.31 345.77 0.00 17671.14 345.78 179.79 17805.18 345.79 179.79 21074.41 345.79 0.00 21129.03 345.79 -180.00 21203.73 345.79 -180.00 21925.05 345.79 0.00 22037.09 345.79 0.02 22076.39 345.79 0.22 23459.70 345.79 0.00 23633.50 345.79 -0.03 3T-613 wp07.1 Spider Plot 9:55, March 11 2025 39.00 To 23633.50 Northing (6500 usft/in)Easting (6500 usft/in) 35 40 4550NDST-0235 40 45 50NDST-02PB13 5404550Nuna 13 5404550 Nuna 1PB13 5 4 0 4 5 505560ODSN-4335 4 0455035 4 0455035 4 04550 35 40 45 503T-60335 40 45 5 03T-6083540455 03T-61235 4 045503T-61635 4 045503T-616PB135 4 045503T-616PB2354045505 53T-6213540 3T-730 wp08.13 5 4 0 3T-731 wp09.1354045503T-601 wp05 v5354045503T-602 wp05 v535 40 4 5 503T-604 wp05 v535 40 45 5 03T-605 (ST) wp0935 40 45 503T-605PH wp0335 40 45 503T-606 wp0835 40 45 5 03T-607 wp053 5 4 0 4 5 5 03T-609 wp063 5 4 0 4 5 5 03T-610 wp053540455 03T-611 wp08.135 40 45503T-614 wp0635404550 3T-615 wp053540455 03T-617 wp07.135404550 3T-618 wp05 v5354045503T-619 wp07.135404550 3T-620 wp05 v5354045503T-622 wp05 v535404550 3T-623 wp05 v5354045503T-624 wp05 v5354045503T-625 wp05 v535404550 3T-626 wp05 v535 40 45503T-627 wp05 v5354045503T-628 wp05 v5354045503T-629 wp05 v5354045503T-613 wp07.1 3T-613 wp07.1 Spider Plot 9:59, March 11 2025 39.00 To 23633.50 Northing (2000 usft/in)Easting (2000 usft/in) 25 30 35 40 4550NDST-0225 30 35 40 45 50NDST-02PB12 5 3 0 3 5 4 0 4 550Nuna 12 5 3 0 3 5 4 0 4 5 5 0 Nuna 1PB125 30 35 40 45 503T-6032 5 30 35 40 45 5 03T-60825303540455 03T-6123T-6163T-616PB13T-616PB22530354045505 53T-621253 0353T-730 wp08.12 5 303 53T-731 wp09.12530354045503T-601 wp05 v5253035403T-602 wp05 v525 30 3 5 40 45 503T-604 wp05 v525 30 35 40 45 5 03T-605 (ST) wp0925 30 35 40 45 503T-605PH wp0325 30 35 40 45 503T-606 wp0825 30 35 40 45 5 03T-607 wp052 5 3 0 3 5 4 0 4 5 5 03T-609 wp062 5 3 0 3 5 4 0 4 5 5 03T-610 wp052530354045503T-611 wp08.13T-614 wp06253035404550 3T-615 wp0525303540455 03T-617 wp07.1253035404550 3T-618 wp05 v52 530354045503T-619 wp07.1253035404550 3T-620 wp05 v52530354045503T-622 wp05 v52530354045503T-623 wp05 v52530354045503T-624 wp05 v52530354045503T-625 wp05 v52530354045503T-626 wp05 v53T-627 wp05 v5253035503T-628 wp05 v52530354045503T-629 wp05 v52530354045503T-613 wp07.1 3T-613 wp07.1 Spider Plot 10:01, March 11 2025 39.00 To 23633.50 Northing (650 usft/in)Easting (650 usft/in) 20 22 24 26 28 30 32 NDST-0220 22 24 26 28 30 32 2 0 2 2 2 4 2 6 2 8 3 0 3 2 3 4 3 6 3 8 4 0 4 2 4 4 4 6Nuna 12 0 2 2 2 4 2 6 2 8 3 0 3 2 3 4 3 6 3 8 4 0 4 2 4 4 4 6 4 8 202020 20 22 24 26 28 30 32 343T-60320 2 2 2 4 2 6 2 8 30 32 34 36 383T-608202224262830323436384042443T-612203T-616202020222426283032343638403T-62120222426283 0 32 34 36 38 3T-730 wp08.120 22 2 426 2830323 4 3 6 3 8 4 03T-731 wp09.12 022 2426283T-601 wp05 v520222426283T-602 wp05 v520 22 24 2 6 28 30 323T-604 wp05 v520 22 24 26 28 30 32 3T-605 (ST) wp0920 22 24 26 28 30 323T-605PH wp0320 22 24 26 28 30 32 34 3T-606 wp0820 22 24 26 28 30 32 34 363T-607 wp052 0 2 2 2 4 2 6 2 8 3 0 3 2 3 4 3 6 3 83T-609 wp062 0 2 2 2 4 2 6 2 8 3 0 3 2 3 4 3 6 3 83T-610 wp052 022 2 4 2 62 8303234363840424446483T-611 wp08.1203T-614 wp0620222426283032343T-615 wp052022242628303234363840424446485 03T-617 wp07.120222426283032343T-618 wp05 v5202224262830323436383T-619 wp07.1202224262830323T-620 wp05 v5202224262830323436383T-622 wp05 v5202224262830323T-623 wp05 v520222426283032343T-624 wp05 v520222426283032343T-625 wp05 v52022242628303T-626 wp05 v5203T-627 wp05 v5202224262830323T-628 wp05 v5202224262830323T-629 wp05 v520222426283032343T-613 wp07.1 3T-613 wp07.1 Spider Plot 10:04, March 11 2025 39.00 To 23633.50 Northing (200 usft/in)Easting (200 usft/in) 10 12 14 16 18NDST-0210 12 14 16 18 1 4 1 6 1 8 2 0 2 2Nuna 11 4 1 6 1 8 2 0 2 2 24 6 8 10 12 24 6 8 10 12 24 6 8 10 12 24 6 8 10 12 14 16 18 20 223T-6032 468 1 0 12 14 1 6 18 20 2 2 2 4 2 63T-6082468101214161820222426283T-61224 6 8 10 123T-61624 6 8 10 12 24 6 8 10 122468101214161820223T-62168101214161820222426283 0 32 343T-730 wp08.181012141 61 8 20 22 2 4 262830323 4 3 6 3T-731 wp09.124 6 8 1 0 1 2 1 4 1 6 1 8 3T-601 wp05 v52 46810121416183T-602 wp05 v5246 8 10 12 14 16 18 20 22 3T-604 wp05 v50246 8 10 12 14 16 18 20 223T-605 (ST) wp090246 8 10 12 14 16 18 20 223T-605PH wp0302468 10 12 14 16 18 20 22 24 3T-606 wp082468 10 12 1 4 16 18 20 22 243T-607 wp052468 1 0 1 2 1 4 1 6 1 8 2 0 2 2 2 4 2 63T-609 wp062468 1 0 1 2 1 4 1 6 1 8 2 0 2 2 2 4 2 63T-610 wp0524681012 1 4 1 6 1 8 2 0 2 2 2 4 2 6283T-611 wp08.1246 8 10 12 143T-614 wp06246810121416182022243T-615 wp052468101214161820222426283T-617 wp07.124681012141618202224263T-618 wp05 v524681012141618202224263T-619 wp07.1246810121416182022243T-620 wp05 v524681012141618202224263T-622 wp05 v5246810121416182022243T-623 wp05 v5246810121416182022243T-624 wp05 v52468101214161820223T-625 wp05 v52468101214161820223T-626 wp05 v5246 83T-627 wp05 v52468101214161820223T-628 wp05 v5246810121416182022243T-629 wp05 v524681012141618202224263T-613 wp07.1 3T-613 wp07.1 NDST-02 Nuna 1 3T-6163T-616PB1 3T-612 3T-6163T-616PB1 3T-621 3T-609 wp06 3T-611 wp08.1 3T-614 wp06 3T-617 wp07.1 3T-619 wp07.1 3T-622 wp05 v5 3T-624 wp05 v5 3T-625 wp05 v5 3T-628 wp05 v5 3T-629 wp05 v5 3-D View3T-613 wp07.1 10:47, March 11 2025 3T-613 wp07.1 NDST-02 Nuna 1 Nuna 1PB1 3T-6163T-616PB1 3T-612 3T-6163T-616PB1 3T-621 3T-611 wp08.1 3T-614 wp06 3T-617 wp07.1 3T-619 wp07.1 3T-622 wp05 v5 3T-624 wp05 v5 3T-625 wp05 v5 3T-628 wp05 v53T-629 wp05 v5 3-D View3T-613 wp07.1 10:48, March 11 2025 7500 10000 12500 15000 17500 20000 South(-)/North(+) (2500 usft/in)-17500 -15000 -12500 -10000 -7500 -5000 -2500 0 2500 West(-)/East(+) (2500 usft/in)502050305040505050605070508050905100511051205130NDST-02N una 1ODSN-43502050305040505050605070508050905100511051205130 3 T -6 0 3 5 0 2 05030504050505060507050805090510051105120 5 1 3 0 3 T -6 0 83T-6 1 2 3 T -6 1 6 3 T -6 1 6 P B 1 3 T -6 0 4 w p 0 5 v 5 3 T -6 0 5 (S T ) w p 0 9 3 T -6 0 6 w p 0 8 5 1 2 05130 3 T -6 0 7 w p 0 5 5 1 2 05130 3 T -6 0 9 w p 0 6 5 1 1 051205130 3 T -6 1 0 w p 0 5 3 T -6 1 1 w p 0 8 .1 3 T -6 1 7 w p 0 7 .1 5 1 2 05130 3 T -6 1 9 w p 0 7 .1 3 T -6 2 2 w p 0 5 v 5 3 T -6 2 4 w p 0 5 v 5 3 T -6 2 5 w p 0 5 v 5 3 T -6 2 8 w p 0 5 v 5 3 T -6 2 9 w p 0 5 v 5 7-5/8" Intermediate Casing 4-1/2" Production Liner 50 205 0 3 0504050505060507050805090510051105120 5 1 3 0 3 T -6 1 3 w p 0 7 .1 3T-613 wp07.1 Quarter Mile View 10:15, March 11 2025 WELLBORE TARGET DETAILS (MAP CO-ORDINATES) Name TVD Shape 3T Flute T01 103124 5107.46 Circle (Radius: 100.00) 3T Flute T02 103124 5101.74 Circle (Radius: 100.00) 3T Flute T03 103124 5131.57 Circle (Radius: 100.00) 3T Flute T04 103124 5117.52 Circle (Radius: 100.00) 3T Flute T05 103124 5082.00 Circle (Radius: 100.00) 3T Flute T06 103124 5029.81 Circle (Radius: 100.00) 3T Flute T07 103124 5045.74 Circle (Radius: 100.00) 3T Flute T09 103124 5030.97 Circle (Radius: 100.00) 3T Flute T01 102522 5166.65 Circle (Radius: 100.00) 3T Flute T01 QM 5107.46 Circle (Radius: 1320.00) 3T Flute T02 102522 5030.97 Circle (Radius: 100.00) 3T Flute T05 QM 5082.00 Circle (Radius: 1320.00) 3T Flute T08 103124 5033.40 Circle (Radius: 100.00) 3T Flute T09 QM 5030.97 Circle (Radius: 1320.00) 7500 10000 12500 15000 17500 20000 South(-)/North(+) (2500 usft/in)-17500 -15000 -12500 -10000 -7500 -5000 -2500 0 2500 West(-)/East(+) (2500 usft/in) N una 13 T -6 1 2 3 T -6 1 6 3 T -6 1 6 P B 1 5 1 2 05130 3 T -6 1 9 w p 0 7 .1 7-5/8" Intermediate Casing 4-1/2" Production Liner 50 205 0 3 0504050505060507050805090510051105120 5 1 3 0 3 T -6 1 3 w p 0 7 .1 3T-613 wp07.1 Quarter Mile View 10:17, March 11 2025 WELLBORE TARGET DETAILS (MAP CO-ORDINATES) Name TVD Shape 3T Flute T01 103124 5107.46 Circle (Radius: 100.00) 3T Flute T02 103124 5101.74 Circle (Radius: 100.00) 3T Flute T03 103124 5131.57 Circle (Radius: 100.00) 3T Flute T04 103124 5117.52 Circle (Radius: 100.00) 3T Flute T05 103124 5082.00 Circle (Radius: 100.00) 3T Flute T06 103124 5029.81 Circle (Radius: 100.00) 3T Flute T07 103124 5045.74 Circle (Radius: 100.00) 3T Flute T09 103124 5030.97 Circle (Radius: 100.00) 3T Flute T01 102522 5166.65 Circle (Radius: 100.00) 3T Flute T01 QM 5107.46 Circle (Radius: 1320.00) 3T Flute T02 102522 5030.97 Circle (Radius: 100.00) 3T Flute T05 QM 5082.00 Circle (Radius: 1320.00) 3T Flute T08 103124 5033.40 Circle (Radius: 100.00) 3T Flute T09 QM 5030.97 Circle (Radius: 1320.00) -450 0 450 900 1350 South(-)/North(+) (450 usft/in)-2250 -1800 -1350 -900 -450 0 450 900 1350 West(-)/East(+) (450 usft/in) 2449 3 T -6 0 3 244 9 3 T -6 0 8 24493 T -6 1 2 3 T -6 1 624493T- 6 2 1 24493 T-7 3 0 w p 0 8 .1 2 4 4 9 3 T-7 3 1 w p0 9.1 2 4 4 9 N una 12 4 4 9 10-3/4" Surface Casing 24493 T -6 1 3 w p 0 7 .1 3T-613 wp07.1 Surface Casing 500'r 10:43, March 11 2025 3T-613 wp07.1 Surface Location 3T-613 wp07.1 Surface Location # Schlumberger-Confidential 3T-613 wp07.1 Surface Casing 3T-613 wp07.1 Surface Casing # Schlumberger-Confidential 3T-613 wp07.1 Top Moraine 3T-613 wp07.1 Top Moraine # Schlumberger-Confidential 3T-613 wp07.1 Intermediate Csg 3T-613 wp07.1 Intermediate Csg # Schlumberger-Confidential 3T-613 wp07.1 TD 3T-613 wp07.1 TD # Schlumberger-Confidential Certificate Of Completion Envelope Id: 02416045-1611-4CE3-B789-43E595EDAC31 Status: Completed Subject: Complete with Docusign: 3T-613wp07 PTD Application.pdf Source Envelope: Document Pages: 67 Signatures: 1 Envelope Originator: Certificate Pages: 4 Initials: 0 Weifeng Dai AutoNav: Enabled EnvelopeId Stamping: Disabled Time Zone: (UTC-06:00) Central Time (US & Canada) 925 N Eldridge Pkwy Houston, TX 77079 Weifeng.Dai@conocophillips.com IP Address: 138.32.8.5 Record Tracking Status: Original 3/11/2025 6:52:32 PM Holder: Weifeng Dai Weifeng.Dai@conocophillips.com Location: DocuSign Signer Events Signature Timestamp David Lee David.L.Lee@conocophillips.com Drilling Eng Supervisor ConocoPhillips Security Level: Email, Account Authentication (None) Signature Adoption: Pre-selected Style Using IP Address: 138.32.8.5 Sent: 3/11/2025 6:53:44 PM Viewed: 3/11/2025 8:19:58 PM Signed: 3/11/2025 8:20:43 PM Electronic Record and Signature Disclosure: Accepted: 11/17/2020 2:37:18 PM ID: cf954e37-5da3-4a84-abd1-b4fabfc297ab In Person Signer Events Signature Timestamp Editor Delivery Events Status Timestamp Agent Delivery Events Status Timestamp Intermediary Delivery Events Status Timestamp Certified Delivery Events Status Timestamp Carbon Copy Events Status Timestamp Witness Events Signature Timestamp Notary Events Signature Timestamp Envelope Summary Events Status Timestamps Envelope Sent Hashed/Encrypted 3/11/2025 6:53:44 PM Certified Delivered Security Checked 3/11/2025 8:19:58 PM Signing Complete Security Checked 3/11/2025 8:20:43 PM Completed Security Checked 3/11/2025 8:20:43 PM 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By selecting the check-box next to ‘I agree to use electronic records and signatures’, you confirm that: x You can access and read this Electronic Record and Signature Disclosure; and x You can print on paper this Electronic Record and Signature Disclosure, or save or send this Electronic Record and Disclosure to a location where you can print it, for future reference and access; and x Until or unless you notify ConocoPhillips as described above, you consent to receive exclusively through electronic means all notices, disclosures, authorizations, acknowledgements, and other documents that are required to be provided or made available to you by ConocoPhillips during the course of your relationship with ConocoPhillips. 1 Dewhurst, Andrew D (OGC) From:Dai, Weifeng <Weifeng.Dai@conocophillips.com> Sent:Wednesday, 23 April, 2025 08:45 To:Dewhurst, Andrew D (OGC) Cc:Loepp, Victoria T (OGC); Davies, Stephen F (OGC); Hobbs, Greg S; Guhl, Meredith D (OGC) Subject:RE: [EXTERNAL]KRU 3T-613 PTD (225-036): Questions Good morning Andy, Please see my comments below in green. I hope this clears up any confusion. Weifeng Dai ConocoPhillips Alaska StaƯ Drilling Engineer Cell: 907-346-0324 From: Dewhurst, Andrew D (OGC) <andrew.dewhurst@alaska.gov> Sent: Tuesday, April 22, 2025 6:16 PM To: Dai, Weifeng <Weifeng.Dai@conocophillips.com> Cc: Loepp, Victoria T (OGC) <victoria.loepp@alaska.gov>; Davies, Stephen F (OGC) <steve.davies@alaska.gov>; Hobbs, Greg S <Greg.S.Hobbs@conocophillips.com>; Guhl, Meredith D (OGC) <meredith.guhl@alaska.gov> Subject: [EXTERNAL]KRU 3T-613 PTD (225-036): Questions Weifeng, I am compleƟng my review of the KRU 3T-613 and have a few quesƟons: x Would you please conĮrm the TVD at TD? The form 10-401 and the MASP show 5,107’ TVD, but the direcƟonal plan shows 5,031’ TVD. It looks like the deepest TVD is around 5,132’ TVD. What is the 5,107’ TVD depth? The TVD at TD is 5,031’. 5,107’ TVD is at the proximity of the entering point of upper Moraine sand. x Regarding the diverter variance request, you menƟon that there are 3 penetraƟons at the 3T-pad. Aren’t there more than 3? Which are the speciĮc wells that you are referring to? What are the maximum gas readings observed from the oīset wells? You are right, there are many penetraƟons at 3T already. IniƟally, I believe I menƟoned 3 penetraƟons within a 500’ radius of the surface casing point, but upon further review, it is actually 2 penetraƟons within that radius. These are 3T-612 with a max total gas reading 356 units and 3T-731 with a max total gas reading 122 units. x Would you please conĮrm that the following are typos on the 10-401 form: o Box 1a: Reentry should not be checked Correct o Box 7: ADL393884 should be added Correct o Box 20: Diverter sketch is not included as an aƩachment Correct Thanks, Andy From: Davies, Stephen F (OGC) <steve.davies@alaska.gov> Sent: Tuesday, 22 April, 2025 11:51 To: Dai, Weifeng <Weifeng.Dai@conocophillips.com> Cc: Dewhurst, Andrew D (OGC) <andrew.dewhurst@alaska.gov>; Loepp, Victoria T (OGC) <victoria.loepp@alaska.gov>; 2 Hobbs, Greg S <Greg.S.Hobbs@conocophillips.com>; Guhl, Meredith D (OGC) <meredith.guhl@alaska.gov>; AOGCC Permitting (CED sponsored) <aogcc.permitting@alaska.gov> Subject: RE: [EXTERNAL]RE: 3T-613 PTD Application Hello Weifeng, Thank you for the update. This applica Ɵon is currently in AOGCC’s review process, and we are aware of CPAI’s schedule. Thanks Again and Be Well, Steve Davies Senior Petroleum Geologist AOGCC CONFIDENTIALITY NOTICE: This e-mail message, including any attachments, contains information from the Alaska Oil and Gas Conservation Commission (AOGCC), State of Alaska and is for the sole use of the intended recipient(s). It may contain conƱdential and/or privileged information. The unauthorized review, use or disclosure of such information may violate state or federal law. If you are an unintended recipient of this e-mail, please delete it, without Ʊrst saving or forwarding it, and, so that the AOGCC is aware of the mistake in sending it to you, contact Steve Davies at 907-793-1224 or steve.davies@alaska.gov. From: Dai, Weifeng <Weifeng.Dai@conocophillips.com> Sent: Tuesday, April 22, 2025 10:51 AM To: AOGCC Permitting (CED sponsored) <aogcc.permitting@alaska.gov> Cc: Dewhurst, Andrew D (OGC) <andrew.dewhurst@alaska.gov>; Davies, Stephen F (OGC) <steve.davies@alaska.gov>; Loepp, Victoria T (OGC) <victoria.loepp@alaska.gov>; Hobbs, Greg S <Greg.S.Hobbs@conocophillips.com>; Guhl, Meredith D (OGC) <meredith.guhl@alaska.gov> Subject: RE: [EXTERNAL]RE: 3T-613 PTD Application Good morning, Just check in the status of the PTD as we are about 7-10 days away from spudding the well. Thanks. Weifeng Dai ConocoPhillips Alaska StaƯ Drilling Engineer Cell: 907-346-0324 From: AOGCC Permitting (CED sponsored) <aogcc.permitting@alaska.gov> Sent: Wednesday, March 12, 2025 8:48 AM To: Dai, Weifeng <Weifeng.Dai@conocophillips.com > Cc: Dewhurst, Andrew D (OGC) <andrew.dewhurst@alaska.gov>; Davies, Stephen F (OGC) <steve.davies@alaska.gov>; Loepp, Victoria T (OGC) <victoria.loepp@alaska.gov>; Hobbs, Greg S <Greg.S.Hobbs@conocophillips.com> Subject: [EXTERNAL]RE: 3T-613 PTD Application CAUTION:This email originated from outside of the organization. Do not click links or open attachments unless you recognize the sender and know the content is safe. 3 Hello, This application has been received for processing. Thank you, GGrace Christianson Executive Assistant, Alaska Oil & Gas Conservation Commission (907) 793-1230 CONFIDENTIALITY NOTICE: This e-mail message, including any attachments, contains information from the Alaska Oil and Gas Conservation Commission (AOGCC), State of Alaska, and is for the sole use of the intended recipient(s). It may contain conƱdential and/or privileged information. The unauthorized review, use, or disclosure of such information may violate state or federal law. If you are an unintended recipient of this e-mail, please delete it without Ʊrst saving or forwarding it, and so that the AOGCC is aware of the mistake in sending it to you, contact Grace Christianson at (907-793-1230) or (grace.christianson@alaska.gov). From: Dai, Weifeng <Weifeng.Dai@conocophillips.com> Sent: Wednesday, March 12, 2025 8:33 AM To: AOGCC Permitting (CED sponsored) <aogcc.permitting@alaska.gov> Cc: Dewhurst, Andrew D (OGC) <andrew.dewhurst@alaska.gov>; Davies, Stephen F (OGC) <steve.davies@alaska.gov>; Loepp, Victoria T (OGC) <victoria.loepp@alaska.gov>; Hobbs, Greg S <Greg.S.Hobbs@conocophillips.com> Subject: 3T-613 PTD Application Good morning, Please Ʊnd the attached 3T-613 PTD application, please feel free to reach out if any questions. Weifeng Dai ConocoPhillips Alaska StaƯ Drilling Engineer Cell: 907-346-0324 CAUTION: This email originated from outside the State of Alaska mail system. Do not click links or open attachments unless you recognize the sender and know the content is safe. Revised 7/2022 TRANSMITTAL LETTER CHECKLIST WELL NAME: ______________________________________ PTD: _____________________________________________ ___ Development ___ Service ___ Exploratory ___ Stratigraphic Test ___ Non-Conventional FIELD: __________________________ POOL: ____________________________________ Check Box for Appropriate Letter / Paragraphs to be Included in Transmittal Letter CHECK OPTIONS TEXT FOR APPROVAL LETTER MULTI LATERAL (If last two digits in API number are between 60-69) The permit is for a new wellbore segment of existing well Permit Number _____________, API Number 50-______________________. Production from or injection into this wellbore must be reported under the original API Number stated above. Spacing Exception The permit is approved subject to full compliance with 20 AAC 25.055. Approval to produce or inject is contingent upon issuance of a conservation order approving a spacing exception. The Operator assumes the liability of any protest to the spacing exception that may occur. Dry Ditch Sample All dry ditch sample sets submitted to the AOGCC must be in no greater than 30-foot sample intervals from below the permafrost or from where samples are first caught and 10-foot sample intervals through target zones. Non- Conventional Well Please note the following special condition of this permit: Production or production testing of coal bed methane is not allowed for this well until after the Operator has designed and implemented a water-well testing program to provide baseline data on water quality and quantity. The Operator must contact the AOGCC to obtain advance approval of such a water-well testing program. Well Logging Requirements Regulation 20 AAC 25.071(a) authorizes the AOGCC to specify types of well logs to be run. In addition to the well logging program proposed by the Operator in the attached application, the following well logs are also required for this well: Per Statute AS 31.05.030(d)(2)(B) and Regulation 20 AAC 25.071, composite curves for all well logs run must be submitted to the AOGCC within 90 days after completion, suspension, or abandonment of this well, or within 90 days of acquisition of the data, whichever occurs first. 225-036 KRU 3T-613 TOROK OIL KUPARUK RIVER
