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225-003
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 Stratigraphic Service 6. API Number: 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 18732 feet feet true vertical 5204 feet feet Effective Depth measured 18723 feet 6861 / 6973 feet true vertical 5204 feet 5106 / 5138 feet Perforation depth Measured depth NA feet True Vertical depth NA feet Tubing (size, grade, measured and true vertical depth)4.5" 12.6# L80 6981' MD 5134' TVD Baker SLZXP 6973' MD 5138' TVD Packers and SSSV (type, measured and true vertical depth)HAL TNT 6861' MD 5106' 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:Manabu Nozaki 5/13/2025 Contact Name:Manabu Nozaki Contact Email:Manabu.Nozaki@ConocoPhillips.com Authorized Title:Completions Engineer Contact Phone:907-265-6519 325-163 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. 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 7,400' MD to 18671' MD Size 117 52102930 7-5/8" 11590 7-5/8" 4790 7850 6890 10860 TBD N/A STATE OF ALASKA ALASKA OIL AND GAS CONSERVATION COMMISSION REPORT OF SUNDRY WELL OPERATIONS 225-003 50-103-20906-00-00 P.O. Box 100360 Anchorage, AK 99510-03603. Address: Job logs attached 5. Permit to Drill Number:2. Operator Name 4. Well Class Before Work: ADL380107 / ADL380106 / ADL393883 Kuparuk Field / Torok Oil Pool KRU 3S-602 Plugs Junk measured 4,183,700 lbs 16/20 WanLi Light weight ceramic proppant, 69,000 lbs of 100 Mesh, and 3500 psi avg treating pressure/4500 psi avg BHG pressure. Length 77 2890 117Conductor Surface Intermediate 20" 10-3/4" measured TVD Intermediate Liner 4739 969 11750 Casing Structural 4778 5181 4-1/2" 6160 7129 18723 5204 2527 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 11:18 am, May 13, 2025 DSR-6/3/25 RBDMS JSB 051525 CDW 05/13/2025 7/30/2025 Sales Order# Prepared By: William Martin Creighton Moore Nannook Crew 0910002608 Intervals 1-23 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. 3S-602 Conoco Phillips Harrison Bay County, AK Post Job Report Stimulation Treatment API: 50-103-20906 Prepared for: Manabu Nozaki April 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 Interval 22 Plots Interval 23 Plots Appendix Well Summary Chemical Summary Planned Design Water Straps 4.13 Water Straps 4.14 Water Straps 4.15 Water Straps 4.20 Water Straps 4.21 Water Analysis 4.12 Water Analysis 4.14 Water Analysis 4.15 Water Analysis 4.20 Water Analysis 4.21 Real-Time QC Event Log 4.13 Event Log 4.14 Event Log 4.15 Event Log 4.20 Event Log 4.21 Prejob Break Test Fann 15 Min Test Interval 1 Zone 1 Zone 2 Zone 3 Zone 4 Zone 5 Zone 6 Zone 7 Zone 8 Zone 9 Zone 10 Zone 11 Zone 12 Zone 13 Zone 14 Zone 15 Zone 16 Zone 17 Zone 18 Zone 19 Zone 20 Zone 21 Zone 22 Zone 23 Sand Sieve Analysis 202 203 204 205 206 197 198 199 200 201 192 193 194 195 196 187 188 189 190 191 182 183 184 185 186 177 178 179 180 181 172 173 174 175 176 167 168 169 170 171 158 159 160 - 164 165 166 141 - 144 145 - 148 149 - 152 153 - 156 157 117 - 120 121 - 124 125 - 128 129 - 136 137 - 140 11 - 35 36 37 - 48 49 - 52 3 4 - 9 10 113 - 116 69 - 72 73 - 80 101 - 112 53 - 56 57 - 64 65 - 68 81 - 84 85 - 88 89 - 92 93 - 96 97 - 100 Conoco Phillips - 3S-602 TOC 2 78,346 gallons of 30# Linear 14,852 gallons of Freeze Protect 1,539,598 gallons of 30# Hybor G-i 4,120,000 pounds of Wanli 16/20 Ceramic 69,000 pounds of 100M 78,624 gallons of 30# Linear 18,564 gallons of Freeze Protect 1,526,695 gallons of 30# Hybor G-i 4,183,700 pounds of Wanli 16/20 Ceramic 69,000 pounds of 100M Thank you, William Martin Senior Technical Professional 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. EngineeringExecutiveSummary On April 13, 2025 a stimulation treatment was performed in the Moraine formation on the 3S-602 well in Harrison Bay County, AK. The 3S-602 was a 23 stage Horizontal Sleeve Design. The proposed treatment consisted of: The actual treatment fully completed 23 of 23 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: Pumping started on April 13th and finished on April 21st, there was no pumping on April 16th for a slickline run to replace the ISO sleeve and there was no pumping from the 17th through 19th due to winter weather. All 23 stages were pumped to design. Patina tracer was pumped on the first stage and Resmetrics tracer on all of the stages. 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. Raw MO-67 was pumped from the downhole blender at a setpoint of 0.6 gal/Mgal. LoSurf was pumped from the ADP. Conoco Phillips - 3S-602 Executive Summary 3 CUSTOMERConoco Phillips API BFD (lb/gal)8.48LAT 70.39430569LEASE3S-602SALES ORDEBHST (°F)141LONG-150.1949722FORMATIONMoraineDATE 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 2,142 51 511-3 Shut-In Shut-In-1-4 30# Linear Arsenal Sleeve Shift 5.0 1,260 102 2 21.00 30.00 1.75 1.75 0.151-5 30# Linear DFIT 10.0 2,100 2,099 50 501.00 30.00 1.75 1.75 0.151-6 Shut-In Shut-In-1-7 30# Linear Step Rate Test 15.0 8,400 1,359 32 321.00 30.00 1.75 1.75 0.151-8 30# Hybor G-i Establish Stable Fluid 15.0 8,400 3,954 94 94 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.151-9 30# Hybor G-i Pad 37.0 24,250 24,251 577 577 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.151-10 30# Hybor G-i Conditioning Pad 100M 0.25 37.0 12,000 12,001 286 289 3,000 3,000 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.151-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.0037.0 12,000 11,997 286 297 12,000 11,115 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.151-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.0037.0 16,000 16,014 381 416 32,000 32,493 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.151-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.0037.0 16,000 16,012 381 433 48,000 48,857 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.151-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.0037.0 10,000 10,025 239 280 40,000 39,296 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.151-15 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.5037.0 8,000 8,001 191 229 36,000 36,644 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.151-16 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.0037.0 6,400 7,134 170 203 32,000 30,855 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.151-17 30# Hybor G-i Spacer and Ball Drop 37.0 2,155 2,160 51 51 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.152-1 30# Hybor G-i Pad 37.0 23,550 23,575 561 561 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.152-2 30# Hybor G-i Conditioning Pad 100M 0.25 37.0 12,000 12,004 286 289 3,000 3,000 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.152-3 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.0037.0 12,000 12,005 286 297 12,000 10,926 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.152-4 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.0037.0 15,000 15,035 358 390 30,000 30,532 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.152-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.0037.0 16,600 16,614 396 451 49,800 51,945 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.152-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.0037.0 7,500 7,481 178 211 30,000 31,187 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.152-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.5037.0 6,200 6,263 149 180 27,900 29,295 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.152-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.0037.0 5,220 5,223 124 145 26,100 19,437 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.152-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.5037.0 4,400 5,860 140 168 24,200 27,026 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.152-10 30# Hybor G-i Spacer and Ball Drop 37.0 2,155 2,158 51 51 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.153-1 30# Linear Displace Ball to Seat 37.0 11,453 11,453 273 2731.00 30.00 1.75 1.75 0.153-2 30# Hybor G-i Establish Stable Fluid 15.0 8,400 3,440 82 82 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.153-3 30# Hybor G-i Pad 37.0 22,650 22,652 539 539 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.153-4 30# Hybor G-i Conditioning Pad 100M 0.25 37.0 12,000 12,069 287 291 3,000 3,000 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.153-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.0037.0 12,000 12,025 286298 12,000 11,401 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.153-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.0037.0 15,000 14,887 354 387 30,000 30,793 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.153-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.0037.0 14,000 14,029 334 380 42,000 43,740 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.153-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.0037.0 10,000 9,994 238 282 40,000 41,363 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.153-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.0037.0 8,000 7,471 178 218 40,000 37,928 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.153-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.0037.0 6,000 6,640 158 194 36,000 33,350 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.153-11 30# Linear Flush 37.0 11,320 12,933 308 3081.00 30.00 1.75 1.75 0.153-12 Freeze Protect Freeze Protect 10.0 1,470 2,100 50 503-13 Shut-In Shut-In-50-103-209060910002608Liquid Additives Dry AdditivesInterval 1Moraine@ 18671.17 - 18675.51 ft 138.8 °FInterval 2Moraine@ 18190.6 - 18194.94 ft 138.9 °FInterval 3Moraine@ 17709.27 - 17713.61 ft 139.6 °FConoco Phillips - 3S-602Actual Design4 CUSTOMERConoco Phillips API BFD (lb/gal)8.48LAT 70.39430569LEASE3S-602SALES ORDEBHST (°F)141LONG-150.1949722FORMATIONMoraineDATE 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)50-103-209060910002608Liquid Additives Dry Additives4-1 Shut-In Shut-In-4-2 Freeze Protect Prime Up Pressure Test 5.0 1,764 1,890 45 454-3 Shut-In Shut-In-4-4 30# Linear Spacer and Dart Drop 15.0 1,260 1,366 33 331.00 30.00 1.75 1.75 0.154-5 30# Hybor G-i Establish Stable Fluid 15.0 8,400 4,807 114 114 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.154-6 30# Hybor G-i Pad 37.0 17,480 17,470 416 416 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.154-7 30# Hybor G-i Conditioning Pad 100M 0.25 37.0 12,000 12,006 286 289 3,000 3,000 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.154-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.0037.0 8,500 8,483 202 209 8,500 6,759 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.154-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.0037.0 8,500 8,514 203 221 17,000 16,981 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.154-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.0037.0 8,000 8,007 191 217 24,000 24,670 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.154-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.0037.0 9,000 9,015 215 254 36,000 36,737 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.154-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.0037.0 8,000 7,993 190 234 40,000 40,973 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.154-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.0037.0 7,000 6,985 166 211 42,000 42,129 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.154-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.5037.0 5,000 6,209 148 184 32,500 34,461 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.154-15 30# Hybor G-i Spacer and Ball Drop 37.0 2,268 2,336 56 56 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.155-1 30# Hybor G-i Pad 37.0 9,710 9,551 227 227 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.155-2 30# Hybor G-i Conditioning Pad 100M 0.25 37.0 12,000 12,034 287 290 3,000 3,000 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.155-3 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.0037.0 2,000 1,995 48 49 2,000 1,116 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.155-4 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.0037.0 2,500 2,503 60 65 5,000 4,705 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.155-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.0037.0 4,000 3,980 95 107 12,000 11,743 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.155-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.0037.0 4,850 4,843 115 136 19,400 19,558 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.155-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.5037.0 5,000 4,989 119 143 22,500 22,473 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.155-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.0037.0 5,410 5,419 129 158 27,050 27,220 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.155-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.5037.0 5,500 5,451 130 162 30,250 30,125 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.155-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.0037.0 5,800 5,784 138 175 34,800 35,525 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.155-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.5037.0 4,000 5,411 129 158 26,000 27,113 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.155-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.0037.0 3,000 3,895 93 115 21,000 21,418 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.155-13 30# Hybor G-i Spacer and Ball Drop 37.0 2,268 2,175 52 52 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.156-1 30# Hybor G-i Pad 37.0 9,710 9,479 226 226 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.156-2 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 0.60 30.00 1.75 1.75 0.156-3 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.0037.0 2,000 1,942 46 48 2,0001,734 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.156-4 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.0037.0 2,500 2,493 59 65 5,000 4,890 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.156-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.0037.0 4,000 4,029 96 109 12,000 12,422 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.156-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.0037.0 4,850 4,831 115 136 19,400 19,948 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.156-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.5037.0 5,000 4,965 118 143 22,500 22,972 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.156-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.0037.0 5,410 5,382 128 157 27,050 27,250 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.156-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.5037.0 5,500 5,479 130 163 30,250 30,505 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.156-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.0037.0 5,800 5,786 138 175 34,80034,815 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.156-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.5037.0 4,000 3,979 95 122 26,00026,022 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.156-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.0037.0 3,000 3,612 86 107 21,00019,420 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.156-13 30# Hybor G-i Spacer and Ball Drop 37.0 2,268 2,411 57 57 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.157-1 30# Hybor G-i Pad 37.0 9,710 9,563 228 228 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.157-2 30# Hybor G-i Conditioning Pad 100M 0.25 37.0 12,000 11,986 285 289 3,000 3,000 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.157-3 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.0037.0 2,000 1,999 48 49 2,000 1,482 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.157-4 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.0037.0 2,500 2,557 61 66 5,000 4,637 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.157-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.0037.0 4,000 3,986 95 108 12,000 12,058 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.157-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.0037.0 4,850 4,845 115 136 19,400 19,885 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.157-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.5037.0 5,000 4,993 119 143 22,500 23,168 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.157-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.0037.0 5,410 5,389 128 158 27,050 27,710 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.157-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.5037.0 5,500 5,494 131 164 30,250 30,871 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.157-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.0037.0 5,800 5,784 138 175 34,80035,364 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.157-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.5037.0 4,000 3,987 95 123 26,00026,332 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.157-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.0037.0 3,000 3,779 90 110 21,00018,909 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.157-13 30# Linear Flush 37.0 11,691 10,966 261 2611.00 30.00 1.75 1.75 0.157-14 Freeze Protect Freeze Protect 5.0 1,680 1,890 45 457-15 Shut-In Shut-In-Interval 4Moraine@ 17229.72 - 17234.06 ft 139.5 °FInterval 6Moraine@ 16184.78 - 16189.12 ft 139.3 °FInterval 7Moraine@ 15662.36 - 15666.7 ft 139.3 °FInterval 5Moraine@ 16707.05 - 16711.39 ft 139.4 °FConoco Phillips - 3S-602Actual Design5 CUSTOMERConoco Phillips API BFD (lb/gal)8.48LAT 70.39430569LEASE3S-602SALES ORDEBHST (°F)141LONG-150.1949722FORMATIONMoraineDATE 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)50-103-209060910002608Liquid Additives Dry Additives8-1 Shut-In Shut-In-8-2 Freeze Protect Prime Up Pressure Test 5.0 1,764 1,848 44 448-3 Shut-In Shut-In-8-4 30# Linear Spacer and Ball Drop 15.0 1,260 902 21 211.00 30.00 1.75 1.75 0.158-5 30# Hybor G-i Establish Stable Fluid 20.0 8,400 3,194 76 76 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.158-6 30# Hybor G-i Pad 37.0 9,710 9,814 234 234 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.158-7 30# Hybor G-i Conditioning Pad 100M 0.25 37.0 12,000 11,924 284 287 3,000 3,000 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.158-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.0037.0 2,000 2,006 48 50 2,000 2,483 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.158-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.0037.0 2,500 2,437 58 63 5,000 4,451 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.158-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.0037.0 4,000 3,988 95 108 12,000 11,964 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.158-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.0037.0 4,850 4,841 115 136 19,400 19,957 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.158-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.5037.0 5,000 4,996 119 143 22,500 22,963 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.158-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.0037.0 5,410 5,386 128 157 27,050 27,523 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.158-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.5037.0 5,500 5,480 130 163 30,250 30,273 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.158-15 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.0037.0 5,800 5,795 138 175 34,800 35,168 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.158-16 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.5037.0 4,000 3,999 95 123 26,000 25,957 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.158-17 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.0037.0 3,000 3,818 91 112 21,000 20,204 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.158-18 30# Hybor G-i Spacer and Ball Drop 37.0 2,268 2,196 52 52 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.159-1 30# Hybor G-i Pad 37.0 9,710 9,560 228 228 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.159-2 30# Hybor G-i Conditioning Pad 100M 0.25 37.0 12,000 12,000 286 289 3,000 3,000 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.159-3 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.0037.0 2,000 1,998 48 49 2,000 1,310 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.159-4 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.0037.0 2,500 2,497 59 65 5,000 4,784 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.159-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.0037.0 4,000 3,993 95 108 12,000 11,894 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.159-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.0037.0 4,850 4,840 115 136 19,400 19,272 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.159-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.5037.0 5,000 4,953 118 142 22,500 22,689 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.159-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.0037.0 5,410 5,499 131 161 27,050 28,158 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.159-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.5037.0 5,500 5,444 130 162 30,250 30,305 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.159-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.0037.0 5,800 5,789 138 174 34,800 34,503 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.159-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.5037.0 4,000 3,962 94 122 26,000 25,637 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.159-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.0037.0 3,000 3,908 93 115 21,00020,669 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.159-13 30# Hybor G-i Spacer and Ball Drop 37.0 2,268 2,281 54 54 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1510-1 30# Hybor G-i Pad 37.0 9,710 9,510 226 226 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1510-2 30# Hybor G-i Conditioning Pad 100M 0.25 37.0 12,000 12,008 286 289 3,000 3,000 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1510-3 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.0037.0 2,000 1,982 47 49 2,0001,916 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1510-4 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.0037.0 2,500 2,502 60 65 5,0004,711 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1510-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.0037.0 4,000 3,988 95 108 12,00012,110 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1510-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.0037.0 4,850 4,849 115 137 19,400 20,127 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1510-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.5037.0 5,000 4,996 119 144 22,500 23,150 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1510-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.0037.0 5,410 5,406 129 158 27,050 27,558 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1510-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.5037.0 5,500 5,486 131 163 30,250 30,641 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1510-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37.0 5,800 5,788 138 175 34,800 35,222 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1510-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37.0 4,000 4,000 95 123 26,000 26,336 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1510-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37.0 3,000 3,624 86 106 21,000 18,440 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1510-13 30# Hybor G-i Spacer and Ball Drop 37.0 2,268 2,176 52 52 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1511-1 30# Hybor G-i Pad 37.0 9,710 9,644 230 230 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1511-2 30# Hybor G-i Conditioning Pad 100M 0.25 37.0 12,000 12,001 286 289 3,000 3,000 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1511-3 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.0037.0 2,000 2,024 48 50 2,000 2,168 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1511-4 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.0037.0 2,500 2,491 59 65 5,000 4,929 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1511-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.0037.0 4,000 3,990 95 108 12,000 12,332 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1511-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.0037.0 4,850 4,891 116 138 19,400 20,386 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1511-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.5037.0 5,000 4,963 118 142 22,500 22,512 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1511-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.0037.0 5,410 5,418 129 158 27,050 27,542 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1511-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.5037.0 5,500 5,497 131 163 30,250 30,396 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1511-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37.0 5,800 5,792 138 175 34,800 35,134 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1511-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37.0 4,000 4,004 95 124 26,000 26,826 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1511-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37.0 3,000 3,977 95 116 21,000 19,777 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1511-13 30# Hybor G-i Spacer and Ball Drop 37.0 2,268 2,201 52 52 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1512-1 30# Hybor G-i Pad 37.0 9,710 9,576 228 228 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1512-2 30# Hybor G-i Conditioning Pad 100M 0.25 37.0 12,000 12,005 286 289 3,000 3,000 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1512-3 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.0037.0 2,000 1,998 48 50 2,000 2,041 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1512-4 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.0037.0 2,500 2,471 59 64 5,000 4,817 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1512-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.0037.0 4,000 3,962 94 107 12,000 12,174 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1512-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.0037.0 4,850 4,824 115 136 19,400 19,709 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1512-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.5037.0 5,000 5,020 120 144 22,500 22,771 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1512-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.0037.0 5,410 5,404 129 158 27,050 27,626 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1512-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.5037.0 5,500 5,457 130 161 30,250 29,624 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1512-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37.0 5,800 5,793 138 175 34,800 35,158 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1512-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37.0 4,000 3,967 94 122 26,000 26,005 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1512-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37.0 3,000 4,031 96 118 21,000 20,757 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1512-13 30# Linear Flush 37.0 10,024 10,110 241 2411.00 30.00 1.75 1.75 0.1512-14 Freeze Protect Freeze Protect 10.0 1,470 1,806 43 4312-15 Shut-In Shut-In-Interval 8Moraine@ 15140.23 - 15144.57 ft 139.3 °FInterval 9Moraine@ 14618.15 - 14622.49 ft 139.2 °FInterval 10Moraine@ 14098.94 - 14103.28 ft 139.1 °FInterval 11Moraine@ 13576.44 - 13580.78 ft 139.1 °FInterval 12Moraine@ 13053.84 - 13058.18 ft 139.3 °FConoco Phillips - 3S-602Actual Design6 CUSTOMERConoco Phillips API BFD (lb/gal)8.48LAT 70.39430569LEASE3S-602SALES ORDEBHST (°F)141LONG-150.1949722FORMATIONMoraineDATE 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)50-103-209060910002608Liquid Additives Dry Additives13-1 Shut-In Shut-In-13-2 Freeze Protect Prime Up Pressure Test 5.0 1,000 2,310 55 5513-3 Shut-In Shut-In-13-4 30# Linear Spacer and Ball Drop 15.0 1,260 871 21 211.00 30.00 1.75 1.75 0.1513-5 30# Linear Displace Dart to Seat 15.0 8,010 7,727 184 1841.00 30.00 1.75 1.75 0.1513-6 30# Linear DFIT 10.0 1,680 1,724 41 411.00 30.00 1.75 1.75 0.1513-7 Shut-In Shut-In-13-8 30# Linear Step Rate Test 15.0 1,000 813 19 191.00 30.00 1.75 1.75 0.1513-9 30# Hybor G-i Establish Stable Fluid 15.0 8,400 2,776 66 66 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1513-10 30# Hybor G-i Pad 37.0 9,710 9,460 225 225 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1513-11 30# Hybor G-i Conditioning Pad 100M 0.25 37.0 12,000 11,983 285 289 3,000 3,000 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1513-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37.0 2,000 1,899 45 46 2,000 1,071 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1513-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37.0 2,500 2,468 59 64 5,000 4,573 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1513-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37.0 4,000 4,003 95 108 12,000 12,045 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1513-15 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37.0 4,850 4,846 115 136 19,400 19,815 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1513-16 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37.0 5,000 4,965 118 143 22,500 22,985 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1513-17 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37.0 5,410 5,412 129 158 27,050 27,780 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1513-18 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37.0 5,500 5,493 131 164 30,250 30,903 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1513-19 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37.0 5,800 5,777 138 174 34,800 34,496 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1513-20 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37.0 4,000 4,002 95 123 26,000 26,321 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1513-21 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37.0 3,000 4,028 96 119 21,000 21,442 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1513-22 30# Hybor G-i Spacer and Ball Drop 37.0 2,268 2,220 53 53 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1514-1 30# Hybor G-i Pad 37.0 9,710 9,401 224 224 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1514-2 30# Hybor G-i Conditioning Pad 100M 0.25 37.0 12,000 11,938 284 287 3,000 3,000 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1514-3 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.0037.0 2,000 1,975 47 49 2,000 1,589 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1514-4 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.0037.0 2,500 2,493 59 64 5,000 4,732 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1514-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.0037.0 4,000 3,995 95 108 12,000 12,040 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1514-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.0037.0 4,850 4,835 115 136 19,400 19,766 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1514-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.5037.0 5,000 4,985 119 143 22,500 23,031 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1514-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.0037.0 5,410 5,376 128 157 27,050 27,176 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1514-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.5037.0 5,500 5,513 131 164 30,250 30,642 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1514-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37.0 5,800 5,776 138 174 34,800 34,772 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1514-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37.0 4,000 3,948 94 121 26,000 25,232 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1514-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37.0 3,000 3,998 95 117 21,000 20,882 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1514-13 30# Hybor G-i Spacer and Ball Drop 37.0 2,268 2,200 52 52 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1515-1 30# Hybor G-i Pad 37.0 9,710 9,441 225 225 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1515-2 30# Hybor G-i Conditioning Pad 100M 0.25 37.0 12,000 12,005 286 289 3,000 3,000 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1515-3 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.0037.0 2,000 1,982 47 49 2,000 1,299 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1515-4 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.0037.0 2,500 2,493 59 64 5,000 4,766 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1515-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.0037.0 4,000 4,006 95 109 12,000 12,430 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1515-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.0037.0 4,850 4,826 115 136 19,400 19,815 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1515-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.5037.0 5,000 4,987 119 143 22,500 23,038 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1515-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.0037.0 5,410 5,387 128 153 27,050 22,858 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1515-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.5037.0 5,500 5,487 131 160 30,250 27,239 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1515-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37.0 5,800 5,798 138 176 34,800 35,421 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1515-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37.0 4,000 3,981 95 123 26,000 26,330 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1515-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37.0 3,000 5,071 121 152 21,000 29,121 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1515-13 30# Hybor G-i Spacer and Ball Drop 37.0 2,268 2,155 51 51 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1516-1 30# Hybor G-i Pad 37.0 3,160 3,001 71 71 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1516-2 30# Hybor G-i Conditioning Pad 100M 0.25 37.0 12,000 11,995 286 289 3,000 3,000 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1516-3 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.0037.0 1,400 1,329 32 33 1,4001,106 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1516-4 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.0037.0 1,750 1,738 41 43 3,5001,654 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1516-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.0037.0 2,800 2,879 69 77 8,4007,858 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1516-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.0037.0 3,400 3,356 80 94 13,60012,888 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1516-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.5037.0 3,500 3,453 82 98 15,75014,901 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1516-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.0037.0 3,850 3,800 90 110 19,25018,558 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1516-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.5037.0 3,800 3,807 91 113 20,90020,671 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1516-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37.0 4,050 4,009 95 121 24,300 23,882 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1516-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37.0 2,800 2,749 65 84 18,200 17,810 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1516-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37.0 2,100 3,983 95 118 14,700 21,653 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1516-13 30# Hybor G-i Spacer and Ball Drop 37.0 2,268 2,271 54 54 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1517-1 30# Hybor G-i Pad 37.0 3,160 2,973 71 71 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1517-2 30# Hybor G-i Conditioning Pad 100M 0.25 37.0 12,000 11,941 284 288 3,000 3,000 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1517-3 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.0037.0 1,400 1,354 32 33 1,400 1,188 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1517-4 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.0037.0 1,750 1,692 40 43 3,500 2,921 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1517-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.0037.0 2,800 2,759 66 75 8,400 8,767 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1517-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.0037.0 3,400 3,322 79 95 13,600 14,609 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1517-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.5037.0 3,500 3,400 81 99 15,750 16,562 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1517-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.0037.0 3,850 3,819 91 113 19,250 20,877 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1517-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.5037.0 3,800 3,788 90 115 20,900 23,156 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1517-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37.0 4,050 3,969 95 121 24,300 24,830 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1517-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37.0 2,800 2,394 57 73 18,200 15,418 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1517-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37.0 2,100 2,997 71 86 14,700 13,848 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1517-13 30# Linear Flush 37.0 8,358 8,402 200 2001.00 30.00 1.75 1.75 0.1517-14 Freeze Protect Freeze Protect 10.0 1,470 1,260 30 3017-15 Shut-In Shut-In-Interval 15Moraine@ 11487.28 - 11491.62 ft 139.7 °FInterval 17Moraine@ 10447.39 - 10451.73 ft 140.1 °FInterval 16Moraine@ 10966.12 - 10970.46 ft 139.9 °FInterval 13Moraine@ 12531.21 - 12535.55 ft 139.4 °FInterval 14Moraine@ 12009.52 - 12013.86 ft 139.5 °FConoco Phillips - 3S-602Actual Design7 CUSTOMERConoco Phillips API BFD (lb/gal)8.48LAT 70.39430569LEASE3S-602SALES ORDEBHST (°F)141LONG-150.1949722FORMATIONMoraineDATE 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)50-103-209060910002608Liquid Additives Dry Additives18-1 Shut-In Shut-In-18-2 Freeze Protect Prime Up Pressure Test 5.0 1,764 2,058 49 4918-3 Shut-In Shut-In-18-4 30# Linear Spacer and Ball Drop 15.0 1,260 1,383 33 331.00 30.00 1.75 1.75 0.1518-5 30# Hybor G-i Establish Stable Fluid 15.0 8,400 2,464 59 59 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1518-6 30# Hybor G-i Pad 37.0 3,160 2,830 67 67 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1518-7 30# Hybor G-i Conditioning Pad 100M 0.25 37.0 12,000 11,974 285 288 3,000 3,000 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1518-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.0037.0 1,400 1,370 33 34 1,4001,194 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1518-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.0037.0 1,750 1,512 36 38 3,5002,141 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1518-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37.0 2,800 2,776 66 75 8,400 8,358 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1518-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37.0 3,400 3,396 81 96 13,600 13,959 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1518-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37.0 3,500 3,515 84 101 15,750 16,246 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1518-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37.0 3,850 3,788 90 111 19,250 19,152 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1518-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37.0 3,800 3,778 90 112 20,900 20,918 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1518-15 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37.0 4,050 4,044 96 122 24,300 24,465 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1518-16 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37.0 2,800 2,781 66 86 18,200 18,188 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1518-17 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37.0 2,100 3,255 78 95 14,700 16,368 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1518-18 30# Hybor G-i Spacer and Ball Drop 37.0 2,268 2,215 53 53 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1519-1 30# Hybor G-i Pad 37.0 3,160 3,106 74 74 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1519-2 30# Hybor G-i Conditioning Pad 100M 0.25 37.0 12,000 11,627 277 280 3,000 3,000 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1519-3 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.0037.0 1,400 1,378 33 34 1,400 1,249 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1519-4 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.0037.0 1,750 1,729 41 45 3,5003,701 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1519-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.0037.0 2,800 2,793 67 75 8,400 8,428 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1519-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.0037.0 3,400 3,385 81 95 13,600 13,690 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1519-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.5037.0 3,500 3,511 84 101 15,75016,215 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1519-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.0037.0 3,850 3,806 91 111 19,25019,396 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1519-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.5037.0 3,800 3,791 90 113 20,90021,189 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1519-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37.0 4,050 4,016 96 122 24,300 24,601 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1519-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37.0 2,800 2,517 60 78 18,200 16,856 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1519-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37.0 2,100 3,022 72 86 14,700 13,413 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1519-13 30# Hybor G-i Spacer and Ball Drop 37.0 2,268 2,245 53 53 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1520-1 30# Hybor G-i Pad 37.0 3,160 3,035 72 72 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1520-2 30# Hybor G-i Conditioning Pad 100M 0.25 37.0 12,000 11,796 281 284 3,000 3,000 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1520-3 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.0037.0 1,400 1,350 32 34 1,400 1,315 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1520-4 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.0037.0 1,750 1,758 42 46 3,500 3,636 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1520-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.0037.0 2,800 2,787 66 75 8,400 8,587 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1520-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.0037.0 3,400 3,414 81 96 13,600 14,277 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1520-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.5037.0 3,500 3,426 82 99 15,750 16,120 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1520-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.0037.0 3,850 3,796 90 111 19,250 19,780 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1520-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.5037.0 3,800 3,670 87 109 20,900 20,617 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1520-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37.0 4,050 4,049 96 123 24,300 24,693 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1520-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37.0 2,800 2,346 56 72 18,200 15,357 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1520-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37.0 2,100 3,337 79 96 14,700 15,604 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1520-13 30# Hybor G-i Spacer and Ball Drop 37.0 2,268 2,203 52 52 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1521-1 30# Hybor G-i Pad 37.0 3,160 2,914 69 69 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1521-2 30# Hybor G-i Conditioning Pad 100M 0.25 37.0 12,000 11,947 284 288 3,000 3,000 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1521-3 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.0037.0 1,400 1,352 32 34 1,4001,311 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1521-4 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.0037.0 1,750 1,748 42 45 3,5003,299 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1521-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.0037.0 2,800 2,228 53 60 8,4006,212 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1521-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.0037.0 3,400 3,395 81 95 13,60013,128 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1521-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.5037.0 3,500 3,466 83 98 15,75015,017 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1521-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.0037.0 3,850 3,846 92 111 19,25018,727 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1521-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.5037.0 3,800 3,784 90 112 20,90020,672 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1521-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37.0 4,050 4,067 97 123 24,300 24,224 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1521-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37.0 2,800 2,803 67 86 18,200 18,229 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1521-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37.0 2,100 3,672 87 107 14,700 18,347 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1521-13 30# Hybor G-i Spacer and Ball Drop 37.0 2,268 2,168 52 52 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1522-1 30# Hybor G-i Pad 37.0 3,160 3,018 72 72 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1522-2 30# Hybor G-i Conditioning Pad 100M 0.25 37.0 12,000 12,004 286 289 3,000 3,000 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1522-3 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.0037.0 1,400 1,388 33 35 1,400 1,669 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1522-4 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.0037.0 1,750 1,744 42 45 3,500 3,416 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1522-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.0037.0 2,800 2,800 67 76 8,400 8,434 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1522-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.0037.0 3,400 3,323 79 92 13,600 12,600 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1522-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.5037.0 3,500 3,500 83 100 15,750 15,746 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1522-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.0037.0 3,850 3,848 92 112 19,250 19,233 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1522-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.5037.0 3,800 3,757 89 111 20,900 20,578 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1522-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37.0 4,050 4,074 97 121 24,300 22,983 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1522-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37.0 2,800 2,780 66 85 18,200 17,890 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1522-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37.0 2,100 3,434 82 100 14,700 17,352 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1522-13 30# Hybor G-i Spacer and Ball Drop 37.0 2,268 2,187 52 52 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1523-1 30# Hybor G-i Pad 37.0 3,160 3,272 78 78 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1523-2 30# Hybor G-i Conditioning Pad 100M 0.25 37.0 12,000 11,974 285 288 3,000 3,000 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1523-3 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.0037.0 1,400 1,421 34 35 1,4001,351 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1523-4 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.0037.0 1,750 1,729 41 45 3,5003,557 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1523-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.0037.0 2,800 2,819 67 76 8,4008,420 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1523-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.0037.0 3,400 3,275 78 92 13,60013,154 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1523-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.5037.0 3,500 3,514 84 101 15,75015,937 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1523-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.0037.0 3,850 3,850 92 112 19,25019,252 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1523-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.5037.0 3,800 3,799 90 113 20,90020,817 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1523-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37.0 4,050 4,019 96 122 24,300 24,366 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1523-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37.0 2,800 2,726 65 84 18,200 17,897 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1523-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37.0 2,100 3,384 81 97 14,700 15,327 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1523-13 30# Linear Flush 37.0 6,410 6,414 153 1531.00 30.00 1.75 1.75 0.1523-14 Freeze Protect Freeze Protect 10.0 1,470 1,260 30 3023-15 Shut-In Shut-In-1,641,196 1,623,883 38,664 43,125 4,189,000 4,199,967Interval 18Moraine@ 9925.58 - 9929.92 ft 140.2 °FInterval 19Moraine@ 9402.53 - 9406.87 ft 140.4 °FInterval 20Moraine@ 8879.86 - 8884.2 ft 140.5 °FInterval 21Moraine@ 8358.17 - 8362.51 ft 140.5 °FInterval 22Moraine@ 7878.09 - 7882.43 ft 140.6 °FInterval 23Moraine@ 7399.73 - 7404.07 ft 140 °FConoco Phillips - 3S-602Actual Design8 CUSTOMERConoco Phillips API BFD (lb/gal)8.48LAT 70.39430569LEASE3S-602SALES ORDEBHST (°F)141LONG-150.1949722FORMATIONMoraineDATE 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)50-103-209060910002608Liquid Additives Dry AdditivesDesign 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- - 4,120,000 4,130,967 4,183,700(gal) (gal) (gal) (gal) (lbs) (lbs) (lbs) (lbs)78,346 78,624 69,000 69,000 69,000 Initial Design Material Volume 1,539.6 384.9 1,617.9 921.6 48,538.3 2,831.4 2,831.4 242.7- - - Actual Design Material Volume 1,526.7 381.7 1,605.3 916.0 48,159.6 2,809.3 2,809.3 240.814,852 18,564 -8316 - - - Physical Material Volume Pumped 1,595 375 1670 905 49138 2,900 2,900 2551,539,598 1,526,695 - - - Physical Material Volume Deviance 4% -2% 4% -1% 2% 3% 3% 6%--** IFS numbers for proppant are taken from software calculations based on multiple variablesMicroMotion Volume Pumped 1,556 390 1,634 931 47,940 2,868 2,864 ---** Proppant is billed from Weight Ticket volumesMicroMotion Volume Deviance 2% 2% 2% 2% 0% 2% 2% --Fluid Type-30# LinearSeawaterFreeze Protect30# Hybor G-iProppant TypeWanli 16/20 Ceramic100M----Conoco Phillips - 3S-602Actual Design9 Conoco Phillips Moraine3S-60250-103-20906*Exceeds 80% of burst pressure*Description OD (in) ID (in) Wt (#) GradeFUF (gal/ft)MD Top (ft)MD Btm (ft) Volume (gal)Tubular Burst Pressure (psi)Tubing4.5 3.958 12.6 L-80 0.6392 0 8,148 5,208 8,430Tubing4.5 3.958 12.6 L-80 0.6392 8,148 22,000 8,854 8,430Total22,00014,062ft1.55ft140.6ftft1.55ft140.6ftTop 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)Toe18,671 18,676 5,0841Moraine138.8-------- - ----18,191 18,195 5,0872Moraine138.912:02:29 PM 12:10:49 PM 2,963 3,190 3,22514.83,018 6,276 3,258 4,538 7,498 2,960 13.717,709 17,7145,1343Moraine139.61:20:55 PM 1:29:51 PM 5,718 5,938 5,97116.52,437 5,709 3,272 4,248 7,117 2,869 15.517,230 17,2345,1284Moraine139.51:43:20 PM 1:59:34 PM 21 233 2749.22,412 2,906 494 3,864 4,402 538 15.616,707 16,711 5,1215Moraine139.43:02:01 PM 3:09:52 PM 2,451 2,655 2,69312.32,818 6,064 3,246 4,307 7,411 3,104 14.716,185 16,189 5,1146Moraine139.33:55:22 PM 4:03:25 PM 4,297 4,493 4,53112.32,923 6,255 3,332 4,349 7,483 3,134 14.815,662 15,667 5,1167Moraine139.34:47:29 PM 4:55:19 PM 6,100 6,288 6,32810.42,769 5,782 3,013 4,205 7,093 2,888 14.915,140 15,145 5,1188Moraine139.39:03:23 AM 9:18:24 AM 12 192 23210.82,065 4,734 2,669 3,521 6,128 2,607 14.614,618 14,622 5,1119Moraine139.210:05:55 AM 10:13:13 AM 1,907 2,079 2,1209.52,707 5,991 3,284 4,148 7,101 2,953 14.614,099 14,103 5,10210Moraine139.110:57:55 AM 11:05:02 AM 3,718 3,883 3,9257.62,619 5,965 3,346 4,102 7,170 3,068 14.813,576 13,581 5,10511Moraine139.111:49:37 AM 11:56:41 AM 5,523 5,680 5,7236.62,577 5,796 3,219 4,036 6,994 2,958 14.513,05413,058 5,11412Moraine139.312:48:58 PM 12:48:32 PM 7,343 7,492 7,5329.72,432 5,607 3,175 3,954 7,018 3,064 14.512,531 12,536 5,12113Moraine139.48:46:27 AM 8:58:12 AM 15 156 19312.71,469 3,712 2,243 3,182 5,489 2,307 15.112,010 12,0145,12814Moraine139.510:27:22 AM 10:33:42 AM 2,140 2,273 2,3175.82,609 5,691 3,082 3,974 6,978 3,004 14.311,487 11,492 5,14015Moraine139.711:19:03 AM 11:25:17 AM 3,946 4,071 4,1164.82,527 5,269 2,742 3,901 6,617 2,716 14.510,966 10,970 5,15216Moraine139.912:11:17 PM 12:17:27 PM 5,783 5,900 5,9463.92,429 5,187 2,758 3,832 6,639 2,807 14.910,447 10,452 5,16517Moraine140.112:49:34 PM 12:55:36 PM 7,094 7,203 7,2494.02,405 5,198 2,793 3,843 6,476 2,633 14.69,926 9,930 5,17618Moraine140.28:20:05 AM 8:29:18 AM 21 122 1639.11,554 2,981 1,427 3,010 4,405 1,395 15.39,403 9,407 5,18619Moraine140.49:03:39 AM 9:08:33 AM 1,377 1,470 1,5146.12,275 4,919 2,644 3,684 6,014 2,330 15.18,880 8,884 5,19120Moraine140.59:40:05 AM 9:45:21 AM 2,648 2,733 2,7803.12,269 5,052 2,783 3,649 6,076 2,427 15.28,358 8,363 5,19221Moraine140.510:17:04 AM 10:21:47 AM 3,925 4,002 4,0457.21,999 4,707 2,708 3,512 6,121 2,609 15.27,878 7,882 5,20022Moraine140.610:54:07 AM 10:58:46 AM 5,213 5,283 5,3284.92,069 4,789 2,720 3,500 5,944 2,444 15.1Heel7,400 7,404 5,16423Moraine140.011:31:36 AM 11:35:52 AM 6,510 6,573 6,6184.62,025 4,206 2,181 3,446 5,365 1,919 15.1166.9159.0151.1143.1135.1238.4230.4222.5214.6206.6198.7127.2119.9112.64,7306,6786,3446,0105,6765,3435,0368,3448,0107,6767,3437,01010,0119,6789,3449,0128,67811,320 269.511,01310,67910,345Displacement to Top Sleeve/Perf (gal)(BBLS)11,935 284.211,627 276.8262.2254.3246.32223Interval #1Max Pressure (psi)8,500Isolation TypeSwell PackerTreatment TubularsCustomerFormationLeaseAPIDateTemperature DataTemp. Gradient (°F/100 ft)BHST (°F)Directional Data5,1372,23722,000Directional Data2,2374/13/2025KOPTemperature DataSleeve/Perf DepthSleeves190.7182.8174.878910112345617181920211213141516Temp. Gradient (°F/100 ft)BHST (°F)TVD at Bottom PerfMD at Bottom Perf5,20018,676KOPAvg. TVDTotal MDConoco Phillips - 3S-602 Wellbore Information10 4/13/25 9:29 4/13/25 12:02 153 min -bpm -psi -psi -bbl 36.9 bpm 5,438 psi 6,901 psi 35.6 bpm 4,758 psi 4,510 psi 5,980 psi 4,153 hhp 547 psi 20 psi 768 psi 5.24 ppg 6 6 32 % 32 % 25 cP 95 F 8.9 DFIT 9.067 bpm 1797 psi 3721 psi 9.82 bpm 2101 psi 4021 psi 2797 psi 0.550 psi/ft 2889 psi 2770 psi 2666 psi 199,260 lbs 3,000 lbs 202,260 lbs 202,194 lbs 3,560 gal 85 bbls 2,142 gal 51 bbls 111,549 gal 2,656 bbls Total Proppant Pumped*: Fluid Summary (by fluid description) 30# Hybor G-i Volume: Proppant Summary Minifrac Average Pressure: Minifrac Average DH Pressure: Freeze Protect Volume: Average Visc: Average Temp: Initial Rate (Breakdown): Initial Surface Pressure (Breakdown): Max Rate: Max Surface Pressure: Max BH Pressure: Interval Summary 3S-602 - 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 Average Missile HHP: Initial BH Pressure (Breakdown): Average BH Pressure: Pumps Ending Stage: Max Proppant Concentration: Pump Time: ISDP: Final Fracture Gradient: Final 10 min: Minifrac Max Surface Pressure: 100M Pumped: Final 15 min: Proppant in Formation: 30# Linear Volume: Minifrac Max DH Pressure: Final 5 min: Dart/Ball Early : Average pH: Minifrac Average Rate: Pad Percentage Actual Wanli 16/20 Ceramic Pumped: Diagnostic method Average Missile Pressure: Minifrac Max Rate: Open Well Pressure: Initial OA Pressure: Conoco Phillips - 3S-602 Interval Summary 11 24,251 gal 577 bbls 12,001 gal 286 bbls 69,183 gal 1,647 bbls 2,160 gal 51 bbls 1,359 gal 32 bbls 3,954 gal 94 bbls 2,099 gal 50 bbls 102 gal 2 bbls Completed Comments: Engineer: Treater: Supervisor: Customer Engineer: Customer Rep:Chad Burkett William Martin Fluid Summary (by stage description) 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 Ball Drop Volume: Interval Status: Craig Karpinski Creighton Moore Before pumping the main stage, the arsenal disk was burst and the alpha sleeve was shifted. After shifting the Alpha sleeve, a DFIT was pumped and pressure monitored for closure which was 2,742 psi on the BH Guage and 3067 psi at the sleeve. A step rate was also pumped. Interval 1 was pumped to completion. DFIT Volume: Arsenal Sleeve Shift Volume: Manabu Nozaki Conditioning Pad Volume: Proppant Laden Fluid Volume: Pad Volume: Conoco Phillips - 3S-602 Interval Summary 12 4/13/25 12:02 4/13/25 13:29 87 min 13.7 bpm 6,276 psi 7,498 psi 15 bbl 36.9 bpm 4,879 psi 6,408 psi 34.9 bpm 4,634 psi 4,401 psi 5,925 psi 3,966 hhp 711 psi 730 psi 5.80 ppg 6 4 32 % 32 % 24 cP 102.5 F 8.9 200,348 lbs 3,000 lbs 203,348 lbs 203,254 lbs 106,218 gal 2,529 bbls 23,575 gal 561 bbls 12,004 gal 286 bbls 68,481 gal 1,631 bbls 2,158 gal 51 bbls Completed Comments: Engineer: Treater: Supervisor: Customer Engineer: Customer Rep: Interval Status: Two pumps were lost during this stage, pump 579 had a leak and pump 563 lost a packing. Sand Screws were briefly cut while pump 579 was investigated before continuing with the stage at the same sand set point. Decision was made to drop the ball for interval 3, displace sand and shut down to do maintenance. *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.Chad Burkett William Martin Craig Karpinski Creighton Moore Manabu Nozaki Wanli 16/20 Ceramic Pumped: 100M Pumped: Total Proppant Pumped*: Conditioning Pad Volume: Proppant Laden Fluid Volume: Spacer and Ball Drop Volume: 30# Hybor G-i Volume: Proppant Summary 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: 3S-602 - Moraine - Interval 2 Average BH Pressure: Average Missile HHP: Initial OA Pressure: Max OA Pressure: Max Proppant Concentration: Pumps Starting Stage: Pumps Ending Stage: Average Visc: Average Temp: Average pH: Pad Percentage Design Pad Percentage Actual Proppant in Formation: Fluid Summary (by fluid description) Fluid Summary (by stage description) Pad Volume: Conoco Phillips - 3S-602 Interval Summary 13 4/13/25 15:03 4/13/25 16:25 83 min 15.5 bpm 5,709 psi 7,117 psi 17 bbl 37.7 bpm 5,167 psi 6,574 psi 36.5 bpm 4,422 psi 4,214 psi 5,664 psi 3,956 hhp 1035 psi 677 psi 695 psi 6.25 ppg 6 6 32 % 32 % 26 cP 89.3 F 8.9 3190 psi 0.621 psi/ft 3125 psi 3081 psi 3050 psi 198,575 lbs 3,000 lbs 201,575 lbs 201,556 lbs 24,386 gal 581 bbls 2,100 gal 50 bbls 103,207 gal 2,457 bbls 11,453 gal 273 bbls 22,652 gal 539 bbls 12,069 gal 287 bbls 65,046 gal 1,549 bbls 12,933 gal 308 bbls 2,100 gal 50 bbls 3,440 gal 82 bbls Completed Comments: Engineer: Treater: Supervisor: Customer Engineer: Customer Rep: Establish Stable Fluid Volume: William Martin Craig Karpinski Creighton Moore Interval Status: After seating the ball, crew shut down to perform maintenance outlined in interval 2 summary. The interval was pumped to completion. *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 Proppant Pumped*: Proppant in Formation: Fluid Summary (by fluid description) Proppant Laden Fluid Volume: Flush Volume: Freeze Protect Volume: Manabu Nozaki Chad Burkett 3S-602 - 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): Fluid Summary (by stage description) Conditioning Pad Volume: Initial Surface Pressure (Breakdown): Start Date/Time: Pad Percentage Design Pad Percentage Actual Freeze Protect Volume: Final Fracture Gradient: Average Visc: Initial OA Pressure: ISDP: Average Missile HHP: Average Temp: Average Missile Pressure: Average Surface Pressure: Average BH Pressure: Pumps Starting Stage: Pumps Ending Stage: Average pH: Final 5 min: 30# Linear Volume: 30# Hybor G-i Volume: 100M Pumped: Max OA Pressure: Max Proppant Concentration: Open Well Pressure: Interval Summary Wanli 16/20 Ceramic Pumped: Pad Volume: Proppant Summary Final 10 min: Final 15 min: Displace Ball to Seat Volume: Conoco Phillips - 3S-602 Interval Summary 14 4/14/25 13:41 4/14/25 3:02 min 15.6 bpm 2,906 psi 4,402 psi 9 bbl 37.2 bpm 5,756 psi 7,086 psi 34.4 bpm 4,633 psi 4,414 psi 5,800 psi 3,907 hhp 536 psi 422 psi 658 psi 6.79 ppg 6 5 32 % 32 % 26 cP 81.14 F 9 202,710 lbs 3,000 lbs 205,710 lbs 205,646 lbs 1,366 gal 33 bbls 1,890 gal 45 bbls 91,825 gal 2,186 bbls 17,470 gal 416 bbls 12,006 gal 286 bbls 55,206 gal 1,314 bbls 1,366 gal 33 bbls 2,336 gal 56 bbls 4,807 gal 114 bbls Completed Comments: Engineer: Treater: Supervisor: Customer Engineer: Customer Rep: Manabu Nozaki Chad Burkett William Martin Creighton Moore Rate was dropped midstage due to a pump kicking out due to an engine temp. It was reengaged after getting the fan going. Interval pumped to completion. Creighton Moore Pad Volume: Conditioning Pad Volume: Proppant Laden Fluid Volume: Spacer and Ball Drop Volume: Fluid Summary (by stage description) Establish Stable Fluid Volume: Interval Status: 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: Initial Surface Pressure (Breakdown): End Date/Time: Pump Time: 3S-602 - Moraine - Interval 4 Interval Summary Start Date/Time: Initial BH Pressure (Breakdown): Open Well Pressure: Dart/Ball Early : Max Rate: Average Rate: Average Missile Pressure: Average BH Pressure: Average Missile HHP: Pumps Ending Stage: Pad Percentage Actual 30# Linear 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. Initial Rate (Breakdown): Proppant in Formation: Max Surface Pressure: Freeze Protect Volume: 30# Hybor G-i Volume: Fluid Summary (by fluid description) Spacer and Dart Drop Volume: Conoco Phillips - 3S-602 Interval Summary 15 4/14/25 3:02 4/14/25 15:55 773 min 14.7 bpm 6,064 psi 7,411 psi 12 bbl 37.4 bpm 5,779 psi 7,060 psi 34.5 bpm 4,770 psi 4,524 psi 5,918 psi 4,035 hhp 652 psi 673 psi 7.16 ppg 5 5 30 % 29 % 26.43 cP 84.43 F 9 200,996 lbs 3,000 lbs 203,996 lbs 203,914 lbs 68,030 gal 1,620 bbls 9,551 gal 227 bbls 12,034 gal 287 bbls 44,270 gal 1,054 bbls 2,175 gal 52 bbls Completed Comments: Engineer: Treater: Supervisor: Customer Engineer: Customer Rep: End Date/Time: Max BH Pressure: Average Surface Pressure: Interval Summary Proppant Summary Fluid Summary (by fluid description) Fluid Summary (by stage description) Wanli 16/20 Ceramic Pumped: Conditioning Pad Volume: 100M Pumped: 3S-602 - Moraine - Interval 5 Average BH Pressure: Initial OA Pressure: Max Proppant Concentration: Start Date/Time: Pad Percentage Design Average Rate: Proppant in Formation: Pad Volume: 30# Hybor G-i Volume: William Martin Average Missile HHP: Average Visc: Max Surface Pressure: *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. Average pH: Pad Percentage Actual Manabu Nozaki Chad Burkett Creighton Moore Spacer and Ball Drop Volume: Pump Time: Creighton Moore During the 6.0ppg, sand concentration dropped to about 1ppg during a bin swap. Interval pumped to completion. Pumps Starting Stage: Pumps Ending Stage: Average Missile Pressure: Max OA Pressure: Initial BH Pressure (Breakdown): Dart/Ball Early : Average Temp: Initial Surface Pressure (Breakdown): Max Rate: Total Proppant Pumped*: Initial Rate (Breakdown): Proppant Laden Fluid Volume: Interval Status: Conoco Phillips - 3S-602 Interval Summary 16 4/14/25 15:55 4/14/25 16:47 52 min 14.8 bpm 6,255 psi 7,483 psi 12 bbl 37.3 bpm 6,255 psi 6,982 psi 34.9 bpm 4,827 psi 4,580 psi 5,981 psi 4,129 hhp 644 psi 672 psi 7.26 ppg 5 5 30 % 30 % 25.5 cP 85.5 F 9.02 199,978 lbs 3,000 lbs 202,978 lbs 202,934 lbs 66,408 gal 1,581 bbls 9,479 gal 226 bbls 12,020 gal 286 bbls 42,498 gal 1,012 bbls 2,411 gal 57 bbls Completed Comments: Engineer: Treater: Supervisor: Customer Engineer: Customer Rep: Pump Time: Initial Rate (Breakdown): Average Missile HHP: 3S-602 - Moraine - Interval 6 Interval Summary Average pH: Proppant Summary Fluid Summary (by fluid description) Fluid Summary (by stage description) Pumps Starting Stage: Max Rate: Average Missile Pressure: Average Rate: Proppant in Formation: Average Visc: Average Surface Pressure: Average BH Pressure: 100M Pumped: Pumps Ending Stage: Conditioning Pad Volume: Interval Status: Pad Volume: Wanli 16/20 Ceramic Pumped: Pad Percentage Design Average Temp: Total Proppant Pumped*: Initial Surface Pressure (Breakdown): Initial BH Pressure (Breakdown): Dart/Ball Early : Interval pumped to completion William Martin Creighton Moore Creighton Moore *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. Manabu Nozaki Chad Burkett Proppant Laden Fluid Volume: 30# Hybor G-i Volume: End Date/Time: Max Surface Pressure: Max BH Pressure: Max OA Pressure: Spacer and Ball Drop Volume: Max Proppant Concentration: Pad Percentage Actual Initial OA Pressure: Start Date/Time: Conoco Phillips - 3S-602 Interval Summary 17 4/14/25 16:47 4/14/25 17:45 58 min 14.9 bpm 5,782 psi 7,093 psi 10 bbl 37.7 bpm 5,434 psi 6,855 psi 36.0 bpm 4,848 psi 4,606 psi 6,010 psi 4,278 hhp 647 psi 659 psi 7.21 ppg 5 5 30 % 30 % 27 cP 80 F 9.0 2381 psi 0.465 psi/ft 2400 psi 2419 psi 2443 psi 200,416 lbs 3,000 lbs 203,416 lbs 203,399 lbs 10,966 gal 261 bbls 1,890 gal 45 bbls 64,362 gal 1,532 bbls 9,563 gal 228 bbls 11,986 gal 285 bbls 42,813 gal 1,019 bbls 10,966 gal 261 bbls 1,890 gal 45 bbls Completed Comments: Engineer: Treater: Supervisor: Customer Engineer: Customer Rep: Interval Status: Interval pumped to completion. Fluid Summary (by fluid description) Manabu Nozaki Chad Burkett Freeze Protect Volume: Freeze Protect Volume: William Martin Creighton Moore Fluid Summary (by stage description) Creighton Moore 30# Linear Volume: Interval Summary Final Fracture Gradient: Pump Time: Max Rate: Initial BH Pressure (Breakdown): Start Date/Time: Pumps Ending Stage: Flush Volume: Pad Volume: 30# Hybor G-i Volume: 100M Pumped: ISDP: Average pH: Max Proppant Concentration: Final 10 min: Final 15 min: Dart/Ball Early : Pad Percentage Actual Initial OA Pressure: Pad Percentage Design Pumps Starting Stage: Final 5 min: Proppant Summary Proppant in Formation: Proppant Laden Fluid Volume: Average Visc: Max Surface Pressure: Max BH Pressure: Average Rate: Average Missile Pressure: Initial Rate (Breakdown): Initial Surface Pressure (Breakdown): Max OA Pressure: Total Proppant Pumped*: *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. Average BH Pressure: Average Surface Pressure: Wanli 16/20 Ceramic Pumped: Average Temp: Average Missile HHP: 3S-602 - Moraine - Interval 7 End Date/Time: Conditioning Pad Volume: Conoco Phillips - 3S-602 Interval Summary 18 4/15/25 9:01 4/15/25 10:05 65 min 14.6 bpm 4,734 psi 6,128 psi 11 bbl 36.8 bpm 4,621 psi 6,015 psi 34.8 bpm 3,957 psi 3,702 psi 5,175 psi 3,370 hhp 413 psi 141 psi 653 psi 7.23 ppg 6 6 30 % 30 % 25 cP 91 F 8.81 200,943 lbs 3,000 lbs 203,943 lbs 203,874 lbs 902 gal 21 bbls 1,848 gal 44 bbls 69,874 gal 1,664 bbls 9,814 gal 234 bbls 11,924 gal 284 bbls 42,746 gal 1,018 bbls 3,098 gal 74 bbls 3,194 gal 76 bbls Completed Comments: Engineer: Treater: Supervisor: Customer Engineer: Customer Rep: William Martin Chad Burkett Creighton Moore Creighton Moore Manabu Nozaki Spacer and Ball Drop Volume: Interval Status: Interval pumped to completion. Proppant Laden Fluid Volume: Wanli 16/20 Ceramic Pumped: 100M Pumped: Proppant Summary Freeze Protect Volume: 30# Hybor G-i Volume: Interval Summary 3S-602 - Moraine - Interval 8 Fluid Summary (by fluid description) Pad Volume: Average Visc: Total Proppant Pumped*: 30# Linear Volume: Conditioning Pad Volume: Average Missile HHP: Fluid Summary (by stage description) Pad Percentage Actual Pad Percentage Design Initial Surface Pressure (Breakdown): Start Date/Time: Initial BH Pressure (Breakdown): Average pH: Average Surface Pressure: Max Rate: Pumps Starting Stage: *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 in Formation: Average Temp: Average Missile Pressure: Initial Rate (Breakdown): Max Surface Pressure: Establish Stable Fluid Volume: Pumps Ending Stage: Average Rate: Max Proppant Concentration: Average BH Pressure: Max OA Pressure: Open Well Pressure: Initial OA Pressure: Max BH Pressure: Dart/Ball Early : End Date/Time: Pump Time: Conoco Phillips - 3S-602 Interval Summary 19 4/15/25 10:05 4/15/25 10:57 52 min 14.6 bpm 5,991 psi 7,101 psi 9 bbl 37.2 bpm 4,410 psi 5,858 psi 35.1 bpm 4,145 psi 3,879 psi 5,391 psi 3,570 hhp 652 psi 685 psi 6.98 ppg 6 6 30 % 30 % 25 cP 94 F 8.78 199,221 lbs 3,000 lbs 202,221 lbs 202,174 lbs 66,724 gal 1,589 bbls 9,560 gal 228 bbls 12,000 gal 286 bbls 42,883 gal 1,021 bbls 2,281 gal 54 bbls Completed Comments: Engineer: Treater: Supervisor: Customer Engineer: Customer Rep: Start Date/Time: End Date/Time: Pump Time: *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. William Martin Creighton Moore Average Temp: Max Proppant Concentration: Pumps Starting Stage: Average Surface Pressure: Manabu Nozaki Chad Burkett Spacer and Ball Drop Volume: 3S-602 - Moraine - Interval 9 Conditioning Pad Volume: Proppant Laden Fluid Volume: Initial BH Pressure (Breakdown): Fluid Summary (by stage description) Average pH: Fluid Summary (by fluid description) 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: Interval Summary Dart/Ball Early : Average Visc: Pad Percentage Design Max OA Pressure: Proppant in Formation: 30# Hybor G-i Volume: Initial OA Pressure: Average Rate: 100M Pumped: Pad Percentage Actual Interval Status: Pad Volume: Average Missile HHP: Creighton Moore Average BH Pressure: Interval pumped to completion. Conoco Phillips - 3S-602 Interval Summary 20 4/15/25 10:57 4/15/25 11:49 52 min 14.8 bpm 5,965 psi 7,170 psi 8 bbl 37.2 bpm 4,410 psi 5,858 psi 35.1 bpm 4,145 psi 3,879 psi 5,391 psi 3,570 hhp 677 psi 691 psi 6.98 ppg 6 6 30 % 30 % 25 cP 89 F 8.91 200,211 lbs 3,000 lbs 203,211 lbs 203,153 lbs 66,315 gal 1,579 bbls 9,510 gal 226 bbls 12,008 gal 286 bbls 42,621 gal 1,015 bbls 2,176 gal 52 bbls Completed Comments: Engineer: Treater: Supervisor: Customer Engineer: Customer Rep: Creighton Moore Creighton Moore *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. Manabu Nozaki Chad Burkett 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: Interval Summary Pump Time: Start Date/Time: 3S-602 - Moraine - Interval 10 End Date/Time: Interval pumped to completion. Average Missile HHP: Wanli 16/20 Ceramic Pumped: Initial OA Pressure: Max Proppant Concentration: Proppant Laden Fluid Volume: 100M Pumped: Pad Volume: Conditioning Pad Volume: Average Temp: Initial Surface Pressure (Breakdown): Proppant Summary Average Missile Pressure: Average Rate: Total Proppant Pumped*: Proppant in Formation: Fluid Summary (by fluid description) Max Surface Pressure: Max BH Pressure: Pumps Ending Stage: Max Rate: Initial Rate (Breakdown): Interval Status: Spacer and Ball Drop Volume: Fluid Summary (by stage description) William Martin 30# Hybor G-i Volume: Conoco Phillips - 3S-602 Interval Summary 21 4/15/25 11:49 4/15/25 12:48 59 min 14.5 bpm 5,796 psi 6,994 psi 7 bbl 37.3 bpm 4,265 psi 5,665 psi 35.4 bpm 3,668 psi 3,391 psi 4,888 psi 3,180 hhp 652 psi 685 psi 7.22 ppg 6 6 30 % 29 % 25 cP 90 F 8.87 202,002 lbs 3,000 lbs 205,002 lbs 204,926 lbs 66,893 gal 1,593 bbls 9,644 gal 230 bbls 12,001 gal 286 bbls 43,047 gal 1,025 bbls 2,201 gal 52 bbls Completed Comments: Engineer: Treater: Supervisor: Customer Engineer: Customer Rep: Fluid Summary (by stage description) Pad Volume: Interval pumped to completion. Manabu Nozaki Chad Burkett Creighton Moore Creighton Moore *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 Percentage Design Average Surface Pressure: Max OA Pressure: Max BH Pressure: Average Rate: Average BH Pressure: Interval Summary Proppant Summary Fluid Summary (by fluid description) Total Proppant Pumped*: Proppant in Formation: Pumps Ending Stage: Pump Time: Initial BH Pressure (Breakdown): Dart/Ball Early : 3S-602 - 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: William Martin Pumps Starting Stage: 100M Pumped: Conditioning Pad Volume: 30# Hybor G-i Volume: Proppant Laden Fluid Volume: Start Date/Time: Interval Status: Average Missile HHP: Initial Rate (Breakdown): Average Missile Pressure: Initial Surface Pressure (Breakdown): Max Surface Pressure: Spacer and Ball Drop Volume: Conoco Phillips - 3S-602 Interval Summary 22 4/15/25 12:48 4/15/25 13:39 50 min 14.5 bpm 5,607 psi 7,018 psi 10 bbl 37.3 bpm 4,120 psi 5,614 psi 36.3 bpm 3,949 psi 3,664 psi 5,152 psi 3,510 hhp 659 psi 672 psi 7.07 ppg 6 6 30 % 30 % 25 cP 84.3 F 8.88 3225 psi 0.631 psi/ft 3166 psi 3136 psi 3114 psi 200,682 lbs 3,000 lbs 203,682 lbs 203,665 lbs 10,110 gal 241 bbls 1,806 gal 43 bbls 64,508 gal 1,536 bbls 9,576 gal 228 bbls 12,005 gal 286 bbls 42,927 gal 1,022 bbls 10,110 gal 241 bbls 1,806 gal 43 bbls Completed Comments: Engineer: Treater: Supervisor: Customer Engineer: Customer Rep: Pumps Starting Stage: Max Proppant Concentration: Pump Time: 3S-602 - Moraine - Interval 12 Interval Summary Initial BH Pressure (Breakdown): Average Missile HHP: Initial Surface Pressure (Breakdown): Max OA Pressure: Average pH: Max Rate: Initial OA Pressure: End Date/Time: Dart/Ball Early : Max BH Pressure: Average Visc: Creighton Moore Chad Burkett Average Surface Pressure: Freeze Protect Volume: Start Date/Time: Average Rate: Average Missile Pressure: Final Fracture Gradient: Pad Percentage Actual Initial Rate (Breakdown): Average BH Pressure: Interval pumped to completion. William Martin Proppant Summary Fluid Summary (by fluid description) Fluid Summary (by stage description) 100M Pumped: 30# Linear Volume: Freeze Protect Volume: 30# Hybor G-i Volume: Max Surface Pressure: ISDP: Interval Status: Pad Volume: Flush Volume: Conditioning Pad Volume: Creighton Moore *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. Manabu Nozaki Final 15 min: Final 5 min: Total Proppant Pumped*: Final 10 min: Wanli 16/20 Ceramic Pumped: Pumps Ending Stage: Pad Percentage Design Proppant in Formation: Proppant Laden Fluid Volume: Average Temp: Conoco Phillips - 3S-602 Interval Summary 23 4/20/25 8:44 4/20/25 10:27 103 min 15.1 bpm 3,712 psi 5,489 psi 13 bbl 37.6 bpm 3,916 psi 5,251 psi 34.1 bpm 3,359 psi 3,167 psi 4,579 psi 2,808 hhp 380 psi 0 psi 468 psi 7.33 ppg 6 6 30 % 29 % 25 cP 93 F 8.88 DFIT 10.140 bpm 1563 psi 3352 psi 10.8 bpm 1655 psi 3456 psi 3026 psi 0.591 psi/ft 2699 psi 2300 psi 2178 psi 201,431 lbs 3,000 lbs 204,431 lbs 204,379 lbs Minifrac Average Pressure: Minifrac Average DH Pressure: Final 15 min: Interval Summary End Date/Time: Average Missile HHP: 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: Total Proppant Pumped*: Average Visc: Initial OA Pressure: Average Surface Pressure: Initial BH Pressure (Breakdown): Average Missile Pressure: Minifrac Max DH Pressure: Pump Time: 3S-602 - Moraine - Interval 13 Minifrac Max Rate: Max BH Pressure: Minifrac Max Surface Pressure: Pumps Ending Stage: Open Well Pressure: Diagnostic method Pumps Starting Stage: Average Rate: Proppant Summary Dart/Ball Early : Max OA Pressure: Average pH: Minifrac Average Rate: Average Temp: Start Date/Time: Max Rate: Wanli 16/20 Ceramic Pumped: Average BH Pressure: 100M Pumped: Proppant in Formation: Conoco Phillips - 3S-602 Interval Summary 24 11,135 gal 265 bbls 2,310 gal 55 bbls 69,332 gal 1,651 bbls 7,727 gal 184 bbls 9,460 gal 225 bbls 11,983 gal 285 bbls 42,893 gal 1,021 bbls 3,091 gal 74 bbls 813 gal 19 bbls 2,776 gal 66 bbls 1,724 gal 41 bbls Completed Comments: Engineer: Treater: Supervisor: Customer Engineer: Customer Rep: Proppant Laden Fluid Volume: Fluid Summary (by stage description) DFIT Volume: A DFIT was pumped before this stage and pressure decline monitored for 23 minutes. Closure was found to be 2491 psi at the BH Gauge. A step rate test was pumped after resuming pumping after the DFIT. Interval pumped to completion. William Martin Creighton Moore Creighton Moore Fluid Summary (by fluid description) 30# Linear Volume: Manabu Nozaki Daniel Faur *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. Conditioning Pad Volume: Spacer and Ball Drop Volume: Displace Dart to Seat Volume: 30# Hybor G-i Volume: Freeze Protect Volume: Pad Volume: Step Rate Test Volume: Establish Stable Fluid Volume: Interval Status: Conoco Phillips - 3S-602 Interval Summary 25 4/20/25 10:27 4/20/25 11:19 52 min 14.3 bpm 5,691 psi 6,978 psi 6 bbl 37.2 bpm 3,675 psi 5,055 psi 35.2 bpm 3,345 psi 3,134 psi 4,535 psi 2,888 hhp 456 psi 478 psi 7.12 ppg 5 5 30 % 29 % 25 cP 86 F 8.93 199,862 lbs 3,000 lbs 202,862 lbs 202,823 lbs 66,433 gal 1,582 bbls 9,401 gal 224 bbls 11,938 gal 284 bbls 42,894 gal 1,021 bbls 2,200 gal 52 bbls Completed Comments: Engineer: Treater: Supervisor: Customer Engineer: Customer Rep: Conditioning Pad Volume: Interval pumped to completion. Fluid Summary (by stage description) Creighton Moore Creighton Moore *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. Initial Surface Pressure (Breakdown): Total Proppant Pumped*: 30# Hybor G-i Volume: Proppant Laden Fluid Volume: Pad Volume: Proppant in Formation: Fluid Summary (by fluid description) Spacer and Ball Drop Volume: Interval Summary Start Date/Time: 3S-602 - Moraine - Interval 14 William Martin Manabu Nozaki Daniel Faur Max Rate: Max BH Pressure: Wanli 16/20 Ceramic Pumped: Pump Time: Average pH: End Date/Time: Average Temp: Dart/Ball Early : Max Surface Pressure: Average Missile HHP: Pumps Starting Stage: Average BH Pressure: 100M Pumped: Max OA Pressure: Max Proppant Concentration: Initial Rate (Breakdown): Average Visc: Initial OA Pressure: Proppant Summary Pad Percentage Actual Interval Status: Initial BH Pressure (Breakdown): Average Surface Pressure: Pad Percentage Design Average Rate: Average Missile Pressure: Pumps Ending Stage: Conoco Phillips - 3S-602 Interval Summary 26 4/20/25 11:19 4/20/25 12:11 52 min 14.5 bpm 5,269 psi 6,617 psi 5 bbl 37.6 bpm 3,963 psi 5,022 psi 36.5 bpm 3,139 psi 2,932 psi 4,393 psi 2,810 hhp 450 psi 492 psi 7.26 ppg 5 5 30 % 29 % 24 cP 96 F 8.88 202,317 lbs 3,000 lbs 205,317 lbs 205,247 lbs 67,619 gal 1,610 bbls 9,441 gal 225 bbls 12,005 gal 286 bbls 44,018 gal 1,048 bbls 2,155 gal 51 bbls Completed Comments: Engineer: Treater: Supervisor: Customer Engineer: Customer Rep: During 5.0 ppg, sand concentration dropped due to debris in the hopper and a bin swap on the Sahara system. 30# Hybor G-i Volume: Dart/Ball Early : 3S-602 - 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): Average Missile HHP: Initial BH Pressure (Breakdown): Average BH Pressure: Pump Time: Fluid Summary (by fluid description) Interval Status: Creighton Moore Creighton Moore Pad Volume: Conditioning Pad Volume: Max Surface Pressure: Fluid Summary (by stage description) William Martin Spacer and Ball Drop Volume: Average Surface Pressure: Average Visc: Average pH: Wanli 16/20 Ceramic Pumped: Proppant Summary Total Proppant Pumped*: Proppant in Formation: Average Temp: Initial OA Pressure: Max OA Pressure: Max Proppant Concentration: 100M Pumped: Proppant Laden Fluid Volume: Pumps Starting Stage: *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. Manabu Nozaki Daniel Faur Start Date/Time: Average Rate: Conoco Phillips - 3S-602 Interval Summary 27 4/20/25 12:11 4/20/25 12:49 38 min 14.9 bpm 5,187 psi 6,639 psi 4 bbl 37.4 bpm 3,512 psi 4,886 psi 34.5 bpm 3,286 psi 3,078 psi 4,584 psi 2,776 hhp 472 psi 482 psi 7.14 ppg 5 5 30 % 29 % 23 cP 94 F 8.86 140,981 lbs 3,000 lbs 143,981 lbs 143,948 lbs 48,370 gal 1,152 bbls 3,001 gal 71 bbls 11,995 gal 286 bbls 31,103 gal 741 bbls 2,271 gal 54 bbls Completed Comments: Engineer: Treater: Supervisor: Customer Engineer: Customer Rep: William Martin Creighton Moore Creighton Moore l.Manabu Nozaki Daniel Faur Max Proppant Concentration: Pad Percentage Design Average Visc: Pump Time: Average Surface 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: Fluid Summary (by fluid description) Interval Summary Pad Percentage Actual Initial OA Pressure: Initial BH Pressure (Breakdown): Dart/Ball Early : Average Missile HHP: Max OA Pressure: Conditioning Pad Volume: Proppant Laden Fluid Volume: Pumps Ending Stage: Max Surface Pressure: Pad Volume: Wanli 16/20 Ceramic Pumped: Initial Rate (Breakdown): Initial Surface Pressure (Breakdown): 100M Pumped: Average Missile Pressure: Proppant Summary Max Rate: 3S-602 - Moraine - Interval 16 Interval Status: Interval pumped to completion. Spacer and Ball Drop Volume: 30# Hybor G-i Volume: Fluid Summary (by stage description) Total Proppant Pumped*: Conoco Phillips - 3S-602 Interval Summary 28 4/20/25 12:49 4/20/25 13:30 41 min 14.6 bpm 5,198 psi 6,476 psi 4 bbl 37.6 bpm 3,690 psi 4,861 psi 36.5 bpm 3,502 psi 3,247 psi 4,625 psi 3,129 hhp 475 psi 482 psi 7.10 ppg 5 5 30 % 30 % 25 cP 97 F 8.85 3289 psi 0.637 psi/ft 3225 psi 3153 psi 3132 psi 142,176 lbs 3,000 lbs 145,176 lbs 145,156 lbs 8,402 gal 200 bbls 1,260 gal 30 bbls 44,408 gal 1,057 bbls 2,973 gal 71 bbls 11,941 gal 284 bbls 29,494 gal 702 bbls 8,402 gal 200 bbls 1,260 gal 30 bbls Completed Comments: Engineer: Treater: Supervisor: Customer Engineer: Customer Rep: 3S-602 - Moraine - Interval 17 Interval Summary Average pH: ISDP: Final Fracture Gradient: Proppant Summary Average Rate: Pad Volume: Freeze Protect Volume: Final 5 min: Proppant in Formation: Average Missile Pressure: Initial Rate (Breakdown): Dart/Ball Early : 30# Hybor G-i Volume: Wanli 16/20 Ceramic Pumped: Final 10 min: *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. Freeze Protect Volume: 30# Linear Volume: Manabu Nozaki Daniel Faur 100M Pumped: Flush Volume: Total Proppant Pumped*: Conditioning Pad Volume: Proppant Laden Fluid Volume: Fluid Summary (by fluid description) Fluid Summary (by stage description) Interval pumped to completion. William Martin Creighton Moore Creighton Moore End Date/Time: Max Proppant Concentration: Average BH Pressure: Start Date/Time: Pumps Ending Stage: Pad Percentage Design Pad Percentage Actual Final 15 min: Max Surface Pressure: Initial BH Pressure (Breakdown): Interval Status: 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: Conoco Phillips - 3S-602 Interval Summary 29 4/21/25 8:17 4/21/25 9:03 46 min 15.3 bpm 2,981 psi 4,405 psi 9 bbl 37.4 bpm 3,494 psi 4,712 psi 34.8 bpm 3,081 psi 2,879 psi 4,194 psi 2,626 hhp 340 psi 0 psi 378 psi 7.04 ppg 6 6 30 % 29 % 26 cP 82.5 F 8.9 140,989 lbs 3,000 lbs 143,989 lbs 143,947 lbs 1,383 gal 33 bbls 2,058 gal 49 bbls 49,698 gal 1,183 bbls 2,830 gal 67 bbls 11,974 gal 285 bbls 30,215 gal 719 bbls 3,598 gal 86 bbls 2,464 gal 59 bbls Completed Comments: Engineer: Treater: Supervisor: Customer Engineer: Customer Rep: William Martin Proppant Summary Freeze Protect Volume: 30# Hybor G-i Volume: 100M Pumped: Creighton Moore Interval pumped to completion. Creighton Moore Daniel Faur Interval Summary Average Temp: Average pH: Average BH Pressure: Pumps Starting Stage: Pumps Ending Stage: 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: Max Rate: Average Missile HHP: Open Well Pressure: Max BH Pressure: Initial Surface Pressure (Breakdown): 3S-602 - Moraine - Interval 18 Pump Time: Interval Status: Initial Rate (Breakdown): Average Rate: Conditioning Pad Volume: Spacer and Ball Drop Volume: End Date/Time: *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: Manabu Nozaki Initial OA Pressure: Max OA Pressure: Max Surface Pressure: Wanli 16/20 Ceramic Pumped: Establish Stable Fluid Volume: Proppant Laden Fluid Volume: Total Proppant Pumped*: Proppant in Formation: Average Visc: Fluid Summary (by stage description) 30# Linear Volume: Fluid Summary (by fluid description) Conoco Phillips - 3S-602 Interval Summary 30 4/21/25 9:03 4/21/25 9:40 36 min 15.1 bpm 4,919 psi 6,014 psi 6 bbl 37.5 bpm 3,123 psi 3,288 psi 34.6 bpm 2,936 psi 2,720 psi 4,052 psi 2,491 hhp 378 psi 437 psi 7.31 ppg 6 6 30 % 29 % 24 cP 78.4 F 8.9 138,738 lbs 3,000 lbs 141,738 lbs 141,668 lbs 46,926 gal 1,117 bbls 3,106 gal 74 bbls 11,627 gal 277 bbls 29,948 gal 713 bbls Completed Comments: Engineer: Treater: Supervisor: Customer Engineer: Customer Rep: Interval Status: *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. Manabu Nozaki Daniel Faur Average Temp: Average Missile Pressure: Average pH: Average BH Pressure: Total Proppant Pumped*: Proppant Laden Fluid Volume: Fluid Summary (by stage description) Creighton Moore 30# Hybor G-i Volume: Fluid Summary (by fluid description) Pad Volume: Wanli 16/20 Ceramic Pumped: 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: Proppant in Formation: 100M Pumped: Conditioning Pad Volume: Average Missile HHP: Max Proppant Concentration: Pumps Ending Stage: 3S-602 - Moraine - Interval 19 Initial Surface Pressure (Breakdown): Average Surface Pressure: Pad Percentage Design Proppant Summary Interval pumped to completion. William Martin Creighton Moore Conoco Phillips - 3S-602 Interval Summary 31 4/21/25 9:40 4/21/25 10:17 37 min 15.2 bpm 5,052 psi 6,076 psi 3 bbl 37.8 bpm 2,981 psi 4,243 psi 35.1 bpm 4,014 psi 2,662 psi 4,014 psi 3,455 hhp 418 psi 440 psi 7.17 ppg 6 6 30 % 29 % 25 cP 86.4 F 8.9 139,986 lbs 3,000 lbs 142,986 lbs 142,923 lbs 46,967 gal 1,118 bbls 3,035 gal 72 bbls 11,796 gal 281 bbls 29,933 gal 713 bbls 2,203 gal 52 bbls Completed Comments: Engineer: Treater: Supervisor: Customer Engineer: Customer Rep: Total Proppant Pumped*: Proppant in Formation: Conditioning Pad Volume: Interval Summary Start Date/Time: End Date/Time: Pad Volume: 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: Proppant Summary Wanli 16/20 Ceramic Pumped: 100M Pumped: Pumps Ending Stage: Average BH Pressure: Pump Time: Pad Percentage Design Average Temp: Fluid Summary (by fluid description) Fluid Summary (by stage description) Max OA Pressure: Pad Percentage Actual 30# Hybor G-i Volume: Average Missile HHP: Initial OA Pressure: 3S-602 - Moraine - Interval 20 Creighton Moore *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. Manabu Nozaki Daniel Faur Max Surface Pressure: Proppant Laden Fluid Volume: Spacer and Ball Drop Volume: Max Proppant Concentration: Average Visc: Interval Status: William Martin Creighton Moore Initial Rate (Breakdown): Pumps Starting Stage: Interval pumped to completion. Conoco Phillips - 3S-602 Interval Summary 32 4/21/25 10:17 4/21/25 10:54 37 min 15.2 bpm 4,707 psi 6,121 psi 7 bbl 37.5 bpm 2,840 psi 4,059 psi 35.0 bpm 2,671 psi 2,444 psi 3,761 psi 2,288 hhp 434 psi 434 psi 7.01 ppg 6 6 30 % 29 % 24 cP 86 F 8.9 139,166 lbs 3,000 lbs 142,166 lbs 142,132 lbs 47,390 gal 1,128 bbls 2,914 gal 69 bbls 11,947 gal 284 bbls 30,361 gal 723 bbls 2,168 gal 52 bbls Completed Comments: Engineer: Treater: Supervisor: Customer Engineer: Customer Rep: Interval Summary Proppant Summary Wanli 16/20 Ceramic Pumped: Fluid Summary (by fluid description) Fluid Summary (by stage description) Conditioning Pad Volume: Proppant Laden Fluid Volume: Spacer and Ball Drop Volume: Start Date/Time: End Date/Time: 30# Hybor G-i Volume: Pump Time: Initial Rate (Breakdown): Initial Surface Pressure (Breakdown): Initial BH Pressure (Breakdown): Dart/Ball Early : Max Rate: *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. Initial OA Pressure: Max OA Pressure: Proppant in Formation: Pad Volume: 100M Pumped: Average Missile HHP: Pumps Ending Stage: Average Visc: Max BH Pressure: Pad Percentage Design Average pH: Average BH Pressure: Pumps Starting Stage: William Martin Average Temp: Average Missile Pressure: Average Surface Pressure: Pad Percentage Actual Average Rate: Max Proppant Concentration: 3S-602 - Moraine - Interval 21 Creighton Moore Creighton Moore Manabu Nozaki Daniel Faur Interval Status: Max Surface Pressure: Total Proppant Pumped*: Interval pumped to completion. Conoco Phillips - 3S-602 Interval Summary 33 4/21/25 10:54 4/21/25 11:31 37 min 15.1 bpm 4,789 psi 5,944 psi 5 bbl 37.4 bpm 2,634 psi 3,845 psi 35.0 bpm 2,517 psi 2,287 psi 3,631 psi 2,161 hhp 432 psi 448 psi 7.41 ppg 6 6 30 % 29 % 26 cP 92.5 F 8.9 139,901 lbs 3,000 lbs 142,901 lbs 142,870 lbs 47,857 gal 1,139 bbls 3,018 gal 72 bbls 12,004 gal 286 bbls 30,648 gal 730 bbls 2,187 gal 52 bbls Completed Comments: Engineer: Treater: Supervisor: Customer Engineer: Customer Rep: Proppant in Formation: Proppant Laden Fluid Volume: 30# Hybor G-i Volume: Total Proppant Pumped*: *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) Fluid Summary (by stage description) Pad Volume: Spacer and Ball Drop Volume: Sand concentration briefly dropped due to a bin swap on the Sahara sand system. Interval pumped to completion. William Martin Creighton Moore Creighton Moore Manabu Nozaki Interval Summary Dart/Ball Early : Average Missile Pressure: Initial OA Pressure: Average Surface Pressure: Max OA Pressure: Max Surface Pressure: Average Missile HHP: Average BH Pressure: Max BH Pressure: Max Rate: Start Date/Time: End Date/Time: Pump Time: Average Rate: Pad Percentage Actual Pumps Starting Stage: Pumps Ending Stage: Pad Percentage Design Average Visc: Average Temp: Initial BH Pressure (Breakdown): Average pH: Conditioning Pad Volume: Proppant Summary Daniel Faur Wanli 16/20 Ceramic Pumped: Max Proppant Concentration: Initial Surface Pressure (Breakdown): 3S-602 - Moraine - Interval 22 Interval Status: 100M Pumped: Initial Rate (Breakdown): Conoco Phillips - 3S-602 Interval Summary 34 4/21/25 11:31 4/21/25 12:11 40 min 15.1 bpm 4,206 psi 5,365 psi 5 bbl 37.3 bpm 2,636 psi 3,709 psi 36.7 bpm 2,455 psi 2,214 psi 3,540 psi 2,208 hhp 440 psi 456 psi 7.08 ppg 6 6 30 % 29 % 25 cP 91.3 F 8.8 3188 psi 0.617 psi/ft 3148 psi 3122 psi 3103 psi 140,078 lbs 3,000 lbs 143,078 lbs 143,058 lbs 6,414 gal 153 bbls 1,260 gal 30 bbls 45,782 gal 1,090 bbls 3,272 gal 78 bbls 11,974 gal 285 bbls 30,536 gal 727 bbls 6,414 gal 153 bbls 1,260 gal 30 bbls Completed Comments: Engineer: Treater: Supervisor: Customer Engineer: Customer Rep: Manabu Nozaki Daniel Faur Interval Status: Creighton Moore William Martin Creighton Moore Dart/Ball Early : Proppant Summary Fluid Summary (by fluid description) Fluid Summary (by stage description) Final 10 min: Final 5 min: 100M Pumped: Average Missile Pressure: Average Missile HHP: Max Proppant Concentration: Interval Summary Pad Percentage Actual Initial Surface Pressure (Breakdown): Max Rate: Pumps Ending Stage: Max OA Pressure: ISDP: Pad Percentage Design Average BH Pressure: Pump Time: End Date/Time: 30# Linear Volume: Average Visc: Average Temp: Final 15 min: Final Fracture Gradient: Total Proppant Pumped*: *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. Max BH Pressure: Average Rate: Max Surface Pressure: Initial OA Pressure: Pumps Starting Stage: Initial BH Pressure (Breakdown): 3S-602 - Moraine - Interval 23 Initial Rate (Breakdown): Start Date/Time: Average pH: Average Surface Pressure: Wanli 16/20 Ceramic Pumped: Freeze Protect Volume: Proppant in Formation: 30# Hybor G-i Volume: Interval pumped to completion. Flush Volume: Conditioning Pad Volume: Proppant Laden Fluid Volume: Pad Volume: Freeze Protect Volume: Conoco Phillips - 3S-602 Interval Summary 35 CustomerFormationLeaseAPIDateWell SummaryWanli 16/20 Ceramic 100M Total ProppantBH Pressure Rate Visc Temp pH BH Pressure Rate gal bbl gal bbl gal bbl gal bbl lbs lbs lbs15980 35.6 25 95 8.9 6901 36.9 3,560 85 2,142 51 117,251 2,792 199,260 3,000 202,260 25925 34.9 24 103 8.9 6408 36.9106,218 2,529 200,348 3,000 203,348 35664 36.5 26 89 8.9 6574 37.7 24,386 581 2,100 50 129,693 3,088 198,575 3,000 201,575 45800 34.4 26 81 9.0 7086 37.2 1,366 33 1,890 45 95,081 2,264 202,710 3,000 205,710 55918 34.5 26 84 9.0 7060 37.468,030 1,620 200,996 3,000 203,996 65981 34.9 26 86 9.0 6982 37.366,408 1,581 199,978 3,000 202,978 76010 36.0 27 80 9.0 6855 37.7 10,966 261 1,890 45 77,218 1,839 200,416 3,000 203,416 85175 34.8 25 91 8.8 6015 36.8 902 21 1,848 44 72,624 1,729 200,943 3,000 203,943 95391 35.1 25 94 8.8 5858 37.266,724 1,589 199,221 3,000 202,221 105391 35.1 25 89 8.9 5858 37.266,315 1,579 200,211 3,000 203,211 114888 35.4 25 90 8.9 5665 37.366,893 1,593 202,002 3,000 205,002 125152 36.3 25 84 8.9 5614 37.3 10,110 241 1,806 43 76,424 1,820 200,682 3,000 203,682 134579 34.1 25 93 8.9 5251 37.6 11,135 265 2,310 55 82,777 1,971 201,431 3,000 204,431 144535 35.2 25 86 8.9 5055 37.266,433 1,582 199,862 3,000 202,862 154393 36.5 24 96 8.9 5022 37.667,619 1,610 202,317 3,000 205,317 164584 34.5 23 94 8.9 4886 37.448,370 1,152 140,981 3,000 143,981 174625 36.5 25 97 8.9 4861 37.6 8,402 200 1,260 30 54,070 1,287 142,176 3,000 145,176 184194 34.8 26 83 8.9 4712 37.4 1,383 33 2,058 49 53,139 1,265 140,989 3,000 143,989 194052 34.6 24 78 8.9 3288 37.546,926 1,117 138,738 3,000 141,738 204014 35.1 25 86 8.9 4243 37.846,967 1,118 139,986 3,000 142,986 213761 35.0 24 86 8.9 4059 37.547,390 1,128 139,166 3,000 142,166 223631 35.0 26 93 8.9 3845 37.447,857 1,139 139,901 3,000 142,901 233540 36.7 25 91 8.8 3709 37.3 6,414 153 1,260 30 53,456 1,273 140,078 3,000 143,078 Minimum902 21 1260 30 46926 1117 138738 3000 141738 Average7862 187 1856 44 70604 1681 179607 3000 182607 Maximum24386 581 2310 55 129693 3088 202710 3000 205710 Wanli 16/20 Ceramic 100M Total ProppantPressure Rate Visc Temp pH Pressure Rate gal bbl gal bbl gal bbl gal bbl lbs lbs TotalPlanned78,346 1,865 0 0 14,852 354 1,641,196 39,076 4,120,000 69,000 4,189,000Recorded5606 35.3 25 89 8.91 7086 37.8 78,624 1,872 0 0 18,564 442 1,623,883 38,664 4,130,967 69,000 4,199,967Weight Tickets4,183,700 69,000 4,252,700** Proppant is billed from Weight Ticket volumes** IFS numbers for proppant are taken from software calculations based on Total FluidFluids ProppantsFluids ProppantsTotal FluidFreeze ProtectFreeze ProtectAverage MaxSeawater30# Linear30# LinearIntervalAverage MaxSeawaterApril 13, 202550-103-209063S-602MoraineConoco Phillips Conoco Phillips - 3S-602 Fluid System-Proppant Summary36 <-Paste Interval 1 Plots HereePRV Test - 4.13.254/13/202508:2808:2908:3008:3108:3208:3308:344/13/202508:35Time010002000300040005000600070008000900010000Treating 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 IA08:28:24 08:29:3608:32:19 08:33:58TP TP858.5 946.91007 1008TPP TPP266.1 302.3663.8 245.4IGKP IGKP900.0 900.01100 1100Conoco Phillips - 3S-602 Interval 1 Plots37 <-Paste Interval 1 Plots HerePressure Test - 4.13.254/13/202508:4408:4608:4808:5008:524/13/202508:54Time010002000300040005000600070008000900010000Treating Pressure (psi)Treating Pressure @Pump (psi)I1 Global Kickout Pressure (psi)P2 Kickout Pressure (psi)Pop-off (psi)111098Global Event Log891011Intersection IntersectionPressure Test - Locals Pressure Test - GlobalPressure Test - Max Pressure Test - Pass08:43:31 08:43:3708:47:36 08:52:15TP TP230.2 256.19517 9330TPP TPP274.2 308.69566 9381IGKP IGKP25.00 95009500 9500PKP PKP500.4 232.99500 9500Customer: CONOCOPHILLIPS - NORTH SLOPE-EBUSJob Date: 13-Apr-2025Sales Order #: 0910002608Well Description: 3S-602 3S-602UWI: 50-103-20906Conoco Phillips - 3S-602 Interval 1 Plots38 <-Paste Interval 1 Plots HereBlender Chemical Plot - Bucket Test 4.13.254/13/202508:1608:1808:2008:2208:2408:264/13/202508:28Time0.00.51.01.52.02.53.0A012345BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-III Conc (lb/Mgal)Optiflo-II Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)MO-67 Conc (gal/Mgal)AABBAAConoco Phillips - 3S-602 Interval 1 Plots39 <-Paste Interval 1 Plots HereADP Chemical Plots - Bucket Test 4.13.254/13/202507:37:0007:37:3007:38:0007:38:3007:39:0007:39:3007:40:0007:40:304/13/202507:41:00Time010203040A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)ABConoco Phillips - 3S-602 Interval 1 Plots40 Treatment Plot - Arsenal Burst Disk4/13/202509:3009:354/13/202509:40Time010002000300040005000600070008000900010000A0102030405060708090100B012345678910C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD41312Global Event Log1213Intersection IntersectionOpen Well Arsenal Burst Disk09:29:42 09:42:32TP TP547.0 6957SR SR0.000 0.000Conoco Phillips - 3S-602 Interval 1 Plots41 Treatment Plot - Alpha Sleeve Shift4/13/202509:45:0009:45:3009:46:0009:46:3009:47:004/13/202509:47:30Time010002000300040005000600070008000900010000A0102030405060708090100B012345678910C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD14Global Event Log14IntersectionAlpha Sleeve Shift 09:46:52TP5749SR0.073Conoco Phillips - 3S-602 Interval 1 Plots42 Treatment Plot - Interval 01 DFIT4/13/202509:5009:5510:0010:054/13/202510:10Time010002000300040005000A0102030405060708090100B012345678910C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD6515Global Event Log15IntersectionISIP 09:54:03TP622.8SR0.000GBP2797Conoco Phillips - 3S-602 Interval 1 Plots43 Treatment Plot - Interval 01 Step Rate Test4/13/202510:2810:3010:3210:3410:3610:384/13/202510:40Time010002000300040005000A0102030405060708090100B012345678910C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD87212019181716Global Event Log161718192021Intersection Intersection IntersectionOpen Well Step 1 Step 2Step 3 Step 4 Step 510:29:43 10:32:06 10:34:4010:35:52 10:36:57 10:37:51TP TP TP321.5 1035 11371294 1343 1412SR SR SR0.000 1.455 2.5954.188 5.276 6.378Conoco Phillips - 3S-602 Interval 1 Plots44 Treatment Plot - Interval 014/13/202510:4011:0011:2011:404/13/202512:00Time010002000300040005000600070008000A0102030405060708090100B012345678910C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD117161514131211109872Conoco Phillips - 3S-602 Interval 1 Plots45 Blender Chemical Plot - Interval 014/13/202510:4011:0011:2011:404/13/202512:00Time0.00.51.01.52.02.53.0A012345BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-III Conc (lb/Mgal)Optiflo-II Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)MO-67 Conc (gal/Mgal)AABBAA117161514131211109872Conoco Phillips - 3S-602 Interval 1 Plots46 ADP Chemical Plots - Interval 014/13/202510:4011:0011:2011:404/13/202512:00Time010203040A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)AB117161514131211109872Conoco Phillips - 3S-602 Interval 1 Plots47 Net Pressure Plot - Interval 017892345678910100Time (min)23456789100010000A-5-4-3-2-1012345CNet Gauge BH Pres (psi)A Closure Pressure = 2742 psi 0 Time = 04/13/25 10:29:00 1Time-219.27NetPr0.000Slope0.000Customer: CONOCOPHILLIPS - NORTH SLOPE-EBUSJob Date: 13-Apr-2025Sales Order #: 0910002608Well Description: 3S-602 3S-602UWI: 50-103-20906Conoco Phillips - 3S-602 Interval 1 Plots48 <-Paste Interval 2 Plots HereTreatment Plot - Interval 024/13/202512:0012:2012:4013:004/13/202513:20Time01000200030004000500060007000A0102030405060708090100B012345678910C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD21109876543211732Conoco Phillips - 3S-602 Interval 2 Plots49 <-Paste Interval 2 Plots HereBlender Chemical Plot - Interval 024/13/202512:0012:2012:4013:004/13/202513:20Time0.00.51.01.52.02.53.0A012345BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-III Conc (lb/Mgal)Optiflo-II Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)MO-67 Conc (gal/Mgal)AABBAA21109876543211732Conoco Phillips - 3S-602 Interval 2 Plots50 <-Paste Interval 2 Plots HereADP Chemical Plots - Interval 024/13/202512:0012:2012:4013:004/13/202513:20Time010203040A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)AB21109876543211732Conoco Phillips - 3S-602 Interval 2 Plots51 <-Paste Interval 2 Plots HereNet Pressure Plot - Interval 022345678910Time (min)23456789100010000A-5-4-3-2-1012345CNet Gauge BH Pres (psi)A Closure Pressure = 2742 psi 0 Time = 04/13/25 12:00:00 1Time-310.27NetPr0.000Slope0.000Customer: CONOCOPHILLIPS - NORTH SLOPE-EBUSJob Date: 13-Apr-2025Sales Order #: 0910002608Well Description: 3S-602 3S-602UWI: 50-103-20906Conoco Phillips - 3S-602 Interval 2 Plots52 <-Paste Interval 3 Plots HereTreatment Plot - Interval 034/13/202515:0015:2015:4016:004/13/202516:20Time01000200030004000500060007000A0102030405060708090100B012345678910C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD1211109876543Conoco Phillips - 3S-602 Interval 3 Plots53 <-Paste Interval 3 Plots HereBlender Chemical Plot - Interval 034/13/202515:0015:1015:2015:3015:4015:5016:0016:104/13/202516:20Time0.00.51.01.52.02.53.0A012345BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-III Conc (lb/Mgal)Optiflo-II Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)MO-67 Conc (gal/Mgal)AABBAA1211109876543Conoco Phillips - 3S-602 Interval 3 Plots54 <-Paste Interval 3 Plots HereADP Chemical Plots - Interval 034/13/202515:0015:1015:2015:3015:4015:5016:0016:104/13/202516:20Time010203040A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)AB1211109876543Conoco Phillips - 3S-602 Interval 3 Plots55 <-Paste Interval 3 Plots HereNet Pressure Plot - Interval 0323456789Time (min)23456789100010000A-5-4-3-2-1012345CNet Gauge BH Pres (psi)A Closure Pressure = 2742 psi 0 Time = 04/13/25 14:55:00 1Time-485.27NetPr0.000Slope0.000Customer: CONOCOPHILLIPS - NORTH SLOPE-EBUSJob Date: 13-Apr-2025Sales Order #: 0910002608Well Description: 3S-602 3S-602UWI: 50-103-20906Conoco Phillips - 3S-602 Interval 3 Plots56 <-Paste Interval 4 Plots HereePRV Test - 4.14.254/14/202513:0713:0813:0913:1013:114/14/202513:12Time010002000300040005000600070008000900010000Treating 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 IA13:07:37 13:09:2613:10:58 13:12:00TP TP794.7 871.8815.2 844.4TPP TPP840.9 840.3863.8 897.2IGKP IGKP900.0 900.0900.0 900.0Conoco Phillips - 3S-602 Interval 4 Plots57 <-Paste Interval 4 Plots HerePressure Test - 4.14.254/14/202513:1413:1613:1813:204/14/202513:22Time010002000300040005000600070008000900010000Treating Pressure (psi)Treating Pressure @Pump (psi)I1 Global Kickout Pressure (psi)P2 Kickout Pressure (psi)Pop-off (psi)10987Global Event Log78910Intersection IntersectionPressure Test - Global Pressure Test - LocalPressure Test - Max Pressure Test - Pass13:13:26 13:13:3013:15:38 13:20:38TP TP174.3 188.79522 9335TPP TPP192.9 212.99575 9370IGKP IGKP25.00 95009500 9500PKP PKP500.4 50.679500 9500Customer: CONOCOPHILLIPS - NORTH SLOPE-EBUSJob Date: 14-Apr-2025Sales Order #: 0910002608Well Description: 3S-602 3S-602UWI: 50-103-20906Conoco Phillips - 3S-602 Interval 4 Plots58 <-Paste Interval 4 Plots HereBlender Chemical Plot - Bucket Test 4.14.254/14/202513:0013:0513:104/14/202513:15Time0.00.51.01.52.02.53.0A012345BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-III Conc (lb/Mgal)Optiflo-II Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)MO-67 Conc (gal/Mgal)AABBAA2Conoco Phillips - 3S-602 Interval 4 Plots59 <-Paste Interval 4 Plots HereADP Chemical Plots - Bucket Test 4.14.254/14/202512:36:0012:36:3012:37:0012:37:3012:38:0012:38:3012:39:004/14/202512:39:30Time010203040A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)AB1Conoco Phillips - 3S-602 Interval 4 Plots60 Treatment Plot - Interval 044/14/202513:4014:0014:2014:404/14/202515:00Time01000200030004000500060007000A0102030405060708090100B012345678910C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD211514131211109876545Conoco Phillips - 3S-602 Interval 4 Plots61 Blender Chemical Plot - Interval 044/14/202513:4013:5014:0014:1014:2014:3014:4014:5015:004/14/202515:10Time0.00.51.01.52.02.53.0A012345BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-III Conc (lb/Mgal)Optiflo-II Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)MO-67 Conc (gal/Mgal)AABBAA211514131211109876545Conoco Phillips - 3S-602 Interval 4 Plots62 ADP Chemical Plots - Interval 044/14/202513:4014:0014:2014:404/14/202515:00Time010203040A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)AB211514131211109876545Conoco Phillips - 3S-602 Interval 4 Plots63 Net Pressure Plot - Interval 042345678923456710Time (min)23456789100010000A-5-4-3-2-1012345CNet Gauge BH Pres (psi)A Closure Pressure = 2742 psi 0 Time = 04/14/25 13:58:00 1Time-348.03NetPr0.000Slope0.000Customer: CONOCOPHILLIPS - NORTH SLOPE-EBUSJob Date: 14-Apr-2025Sales Order #: 0910002608Well Description: 3S-602 3S-602UWI: 50-103-20906Conoco Phillips - 3S-602 Interval 4 Plots64 <-Paste Interval 5 Plots HereTreatment Plot - Interval 054/14/202515:1015:2015:3015:4015:504/14/202516:00Time01000200030004000500060007000A0102030405060708090100B012345678910C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD211312111098765432165Conoco Phillips - 3S-602 Interval 5 Plots65 <-Paste Interval 5 Plots HereBlender Chemical Plot - Interval 054/14/202515:1015:2015:3015:4015:504/14/202516:00Time0.00.51.01.52.02.53.0A012345BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-III Conc (lb/Mgal)Optiflo-II Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)MO-67 Conc (gal/Mgal)AABBAA11312111098765432165Conoco Phillips - 3S-602 Interval 5 Plots66 <-Paste Interval 5 Plots HereADP Chemical Plots - Interval 054/14/202515:1015:2015:3015:4015:504/14/202516:00Time010203040A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)AB21131211109876543211565Conoco Phillips - 3S-602 Interval 5 Plots67 <-Paste Interval 5 Plots HereNet Pressure Plot - Interval 05567892345610Time (min)23456789100010000A-5-4-3-2-1012345CNet Gauge BH Pres (psi)A Closure Pressure = 2742 psi 0 Time = 04/14/25 15:05:00 1Time-415.03NetPr0.000Slope0.000Customer: CONOCOPHILLIPS - NORTH SLOPE-EBUSJob Date: 14-Apr-2025Sales Order #: 0910002608Well Description: 3S-602 3S-602UWI: 50-103-20906Conoco Phillips - 3S-602 Interval 5 Plots68 <-Paste Interval 6 Plots HereTreatment Plot - Interval 064/14/202516:0016:1016:2016:3016:404/14/202516:50Time01000200030004000500060007000A0102030405060708090100B012345678910C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD211312111098765432176Conoco Phillips - 3S-602 Interval 6 Plots69 <-Paste Interval 6 Plots HereBlender Chemical Plot - Interval 064/14/202516:0016:1016:2016:3016:404/14/202516:50Time0.00.51.01.52.02.53.0A012345BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-III Conc (lb/Mgal)Optiflo-II Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)MO-67 Conc (gal/Mgal)AABBAA211312111098765432176Conoco Phillips - 3S-602 Interval 6 Plots70 <-Paste Interval 6 Plots HereADP Chemical Plots - Interval 064/14/202516:0016:1016:2016:3016:404/14/202516:50Time010203040A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)AB11312111098765432176Conoco Phillips - 3S-602 Interval 6 Plots71 <-Paste Interval 6 Plots HereNet Pressure Plot - Interval 066789100Time (min)23456789100010000A-5-4-3-2-1012345CNet Gauge BH Pres (psi)A Closure Pressure = 2742 psi 0 Time = 04/14/25 15:05:00 1Time-415.03NetPr0.000Slope0.000Customer: CONOCOPHILLIPS - NORTH SLOPE-EBUSJob Date: 14-Apr-2025Sales Order #: 0910002608Well Description: 3S-602 3S-602UWI: 50-103-20906Conoco Phillips - 3S-602 Interval 6 Plots72 <-Paste Interval 7 Plots HereePRV Test - 4.15.254/15/202507:3407:3607:3807:404/15/202507:42Time010002000300040005000600070008000900010000Treating 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 IA07:33:39 07:37:2307:39:42 07:41:22TP TP784.1 700.2652.9 712.0TPP TPP808.0 733.7697.2 754.7IGKP IGKP900.0 900.0900.0 900.0Conoco Phillips - 3S-602 Interval 7 Plots73 <-Paste Interval 7 Plots HerePressure Test - 4.15.254/15/202508:2408:2608:2808:3008:3208:344/15/202508:36Time010002000300040005000600070008000900010000Treating Pressure (psi)Treating Pressure @Pump (psi)I1 Global Kickout Pressure (psi)P2 Kickout Pressure (psi)Pop-off (psi)1211Global Event Log1112Intersection IntersectionPressure Test - Max Pressure Test - Pass08:28:43 08:33:45TP TP9427 9333TPP TPP9498 9379IGKP IGKP9475 9475PKP PKP9400 9400Customer: CONOCOPHILLIPS - NORTH SLOPE-EBUSJob Date: 15-Apr-2025Sales Order #: 0910002608Well Description: 3S-602 3S-602UWI: 50-103-20906Conoco Phillips - 3S-602 Interval 7 Plots74 <-Paste Interval 7 Plots HereBlender Chemical Plot - Bucket Test 4.15.254/15/202507:0507:1007:154/15/202507:20Time0.00.51.01.52.02.53.0A012345BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-III Conc (lb/Mgal)Optiflo-II Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)MO-67 Conc (gal/Mgal)AABBAA2Conoco Phillips - 3S-602 Interval 7 Plots75 <-Paste Interval 7 Plots HereADP Chemical Plots - Bucket Test 4.15.254/15/202506:5006:5106:5206:5306:5406:554/15/202506:56Time010203040A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)ABConoco Phillips - 3S-602 Interval 7 Plots76 Treatment Plot - Interval 074/14/202516:5017:0017:1017:2017:304/14/202517:40Time01000200030004000500060007000A0102030405060708090100B012345678910C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD14131211109876543217Conoco Phillips - 3S-602 Interval 7 Plots77 Blender Chemical Plot - Interval 074/14/202516:5017:0017:1017:2017:304/14/202517:40Time0.00.51.01.52.02.53.0A012345BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-III Conc (lb/Mgal)Optiflo-II Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)MO-67 Conc (gal/Mgal)AABBAA14131211109876543217Conoco Phillips - 3S-602 Interval 7 Plots78 ADP Chemical Plots - Interval 074/14/202516:5017:0017:1017:2017:304/14/202517:40Time010203040A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)AB14131211109876543217Conoco Phillips - 3S-602 Interval 7 Plots79 Net Pressure Plot - Interval 07Time (min)23456789100010000A-5-4-3-2-1012345CNet Gauge BH Pres (psi)A Closure Pressure = 2742 psi 0 Time = 04/14/25 15:05:00 1Time-415.03NetPr0.000Slope0.000Customer: CONOCOPHILLIPS - NORTH SLOPE-EBUSJob Date: 14-Apr-2025Sales Order #: 0910002608Well Description: 3S-602 3S-602UWI: 50-103-20906Conoco Phillips - 3S-602 Interval 7 Plots80 <-Paste Interval 8 Plots HereTreatment Plot - Interval 084/15/202509:0009:2009:404/15/202510:00Time01000200030004000500060007000A0102030405060708090100B012345678910C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD211817161514131211109876549Conoco Phillips - 3S-602 Interval 8 Plots81 <-Paste Interval 8 Plots HereBlender Chemical Plot - Interval 084/15/202509:0009:1009:2009:3009:4009:5010:004/15/202510:10Time0.00.51.01.52.02.53.0A012345BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-III Conc (lb/Mgal)Optiflo-II Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)MO-67 Conc (gal/Mgal)AABBAA1181716151413121110987659Conoco Phillips - 3S-602 Interval 8 Plots82 <-Paste Interval 8 Plots HereADP Chemical Plots - Interval 084/15/202509:0009:1009:2009:3009:4009:5010:004/15/202510:10Time010203040A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)AB11817161514131211109876549Conoco Phillips - 3S-602 Interval 8 Plots83 <-Paste Interval 8 Plots HereNet Pressure Plot - Interval 08345678Time (min)23456789100010000A-5-4-3-2-1012345CNet Gauge BH Pres (psi)A Closure Pressure = 2742 psi 0 Time = 04/15/25 08:55:35 1Time-111.04NetPr0.000Slope0.000Customer: CONOCOPHILLIPS - NORTH SLOPE-EBUSJob Date: 15-Apr-2025Sales Order #: 0910002608Well Description: 3S-602 3S-602UWI: 50-103-20906Conoco Phillips - 3S-602 Interval 8 Plots84 <-Paste Interval 9 Plots HereTreatment Plot - Interval 094/15/202510:1010:2010:3010:4010:504/15/202511:00Time01000200030004000500060007000A0102030405060708090100B012345678910C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD113121110987654321109Conoco Phillips - 3S-602 Interval 9 Plots85 <-Paste Interval 9 Plots HereBlender Chemical Plot - Interval 094/15/202510:1010:2010:3010:4010:504/15/202511:00Time0.00.51.01.52.02.53.0A012345BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-III Conc (lb/Mgal)Optiflo-II Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)MO-67 Conc (gal/Mgal)AABBAA113121110987654321109Conoco Phillips - 3S-602 Interval 9 Plots86 <-Paste Interval 9 Plots HereADP Chemical Plots - Interval 094/15/202510:1010:2010:3010:4010:504/15/202511:00Time010203040A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)AB113121110987654321109Conoco Phillips - 3S-602 Interval 9 Plots87 <-Paste Interval 9 Plots HereNet Pressure Plot - Interval 0989100Time (min)23456789100010000A-5-4-3-2-1012345CNet Gauge BH Pres (psi)A Closure Pressure = 2742 psi 0 Time = 04/15/25 08:55:35 1Time-111.04NetPr0.000Slope0.000Customer: CONOCOPHILLIPS - NORTH SLOPE-EBUSJob Date: 15-Apr-2025Sales Order #: 0910002608Well Description: 3S-602 3S-602UWI: 50-103-20906Conoco Phillips - 3S-602 Interval 9 Plots88 <-Paste Interval 10 Plots HereTreatment Plot - Interval 104/15/202511:0011:1011:2011:3011:404/15/202511:50Time01000200030004000500060007000A0102030405060708090100B012345678910C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD21131211109876543211110Conoco Phillips - 3S-602 Interval 10 Plots89 <-Paste Interval 10 Plots HereBlender Chemical Plot - Interval 104/15/202511:0011:1011:2011:3011:404/15/202511:50Time0.00.51.01.52.02.53.0A012345BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-III Conc (lb/Mgal)Optiflo-II Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)MO-67 Conc (gal/Mgal)AABBAA1131211109876543211110Conoco Phillips - 3S-602 Interval 10 Plots90 <-Paste Interval 10 Plots HereADP Chemical Plots - Interval 104/15/202511:0011:1011:2011:3011:404/15/202511:50Time010203040A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)AB1131211109876543211110Conoco Phillips - 3S-602 Interval 10 Plots91 <-Paste Interval 10 Plots HereNet Pressure Plot - Interval 1056789234510Time (min)23456789100010000A-5-4-3-2-1012345CNet Gauge BH Pres (psi)A Closure Pressure = 2742 psi 0 Time = 04/15/25 11:00:35 1Time-236.04NetPr0.000Slope0.000Customer: CONOCOPHILLIPS - NORTH SLOPE-EBUSJob Date: 15-Apr-2025Sales Order #: 0910002608Well Description: 3S-602 3S-602UWI: 50-103-20906Conoco Phillips - 3S-602 Interval 10 Plots92 <-Paste Interval 11 Plots HereTreatment Plot - Interval 114/15/202511:5012:0012:1012:2012:3012:404/15/202512:50Time01000200030004000500060007000A0102030405060708090100B012345678910C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD21131211109876543211211Conoco Phillips - 3S-602 Interval 11 Plots93 <-Paste Interval 11 Plots HereBlender Chemical Plot - Interval 114/15/202511:5012:0012:1012:2012:304/15/202512:40Time0.00.51.01.52.02.53.0A012345BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-III Conc (lb/Mgal)Optiflo-II Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)MO-67 Conc (gal/Mgal)AABBAA113121110987654321131211Conoco Phillips - 3S-602 Interval 11 Plots94 <-Paste Interval 11 Plots HereADP Chemical Plots - Interval 114/15/202511:5012:0012:1012:2012:304/15/202512:40Time010203040A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)AB113121110987654321131211Conoco Phillips - 3S-602 Interval 11 Plots95 <-Paste Interval 11 Plots HereNet Pressure Plot - Interval 1167892345610Time (min)23456789100010000A-5-4-3-2-1012345CNet Gauge BH Pres (psi)A Closure Pressure = 2742 psi 0 Time = 04/15/25 11:50:35 1Time-286.04NetPr0.000Slope0.000Customer: CONOCOPHILLIPS - NORTH SLOPE-EBUSJob Date: 15-Apr-2025Sales Order #: 0910002608Well Description: 3S-602 3S-602UWI: 50-103-20906Conoco Phillips - 3S-602 Interval 11 Plots96 <-Paste Interval 12 Plots HereTreatment Plot - Interval 124/15/202512:5013:0013:1013:2013:304/15/202513:40Time01000200030004000500060007000A0102030405060708090100B012345678910C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD1312111098765432112Conoco Phillips - 3S-602 Interval 12 Plots97 <-Paste Interval 12 Plots HereBlender Chemical Plot - Interval 124/15/202512:5013:0013:1013:2013:304/15/202513:40Time0.00.51.01.52.02.53.0A012345BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-III Conc (lb/Mgal)Optiflo-II Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)MO-67 Conc (gal/Mgal)AABBAA1312111098765432112Conoco Phillips - 3S-602 Interval 12 Plots98 <-Paste Interval 12 Plots HereADP Chemical Plots - Interval 124/15/202512:5013:0013:1013:2013:304/15/202513:40Time010203040A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)AB131211109876543211312Conoco Phillips - 3S-602 Interval 12 Plots99 <-Paste Interval 12 Plots HereNet Pressure Plot - Interval 127892345610Time (min)23456789100010000A-5-4-3-2-1012345CNet Gauge BH Pres (psi)A Closure Pressure = 2742 psi 0 Time = 04/15/25 12:40:35 1Time-336.04NetPr0.000Slope0.000Customer: CONOCOPHILLIPS - NORTH SLOPE-EBUSJob Date: 15-Apr-2025Sales Order #: 0910002608Well Description: 3S-602 3S-602UWI: 50-103-20906Conoco Phillips - 3S-602 Interval 12 Plots100 <-Paste Interval 13 Plots HereePRV Test - 4.20.254/20/202507:3507:3607:3707:3807:3907:4007:4107:424/20/202507:43Time010002000300040005000600070008000900010000Treating Pressure (psi)Treating Pressure @Pump (psi)I1 Global Kickout Pressure (psi)P2 Kickout Pressure (psi)Pop-off (psi)9876Global Event Log6789Intersection IntersectionePRV - Primary Tubing ePRV - Primary IAePRV - Secondary Tubing ePRV - Secondary IA07:35:59 07:38:4307:41:35 07:42:53TP TP934.7 970.0976.4 994.7TPP TPP987.2 663.7946.3 973.5IGKP IGKP900.0 14001400 1400Conoco Phillips - 3S-602 Interval 13 Plots101 <-Paste Interval 13 Plots HerePressure Test - 4.20.254/20/202508:0408:0608:0808:1008:1208:1408:1608:184/20/202508:20Time010002000300040005000600070008000900010000Treating Pressure (psi)Treating Pressure @Pump (psi)I1 Global Kickout Pressure (psi)P2 Kickout Pressure (psi)Pop-off (psi)181716151413Global Event Log131415161718Intersection IntersectionPressure Test - Global Pressure Test - LocalsPressure Test - Pass Pressure Test - FailPressure Test - Start Pressure Test - Pass08:05:23 08:05:3108:07:13 08:11:1408:14:43 08:20:20TP TP239.6 271.09537 94339531 8927TPP TPP248.6 288.89516 89219452 8862IGKP IGKP25.00 95009500 95009500 9500PKP PKP500.4 75.569500 95009500 9500Customer: CONOCOPHILLIPS - NORTH SLOPE-EBUSJob Date: 20-Apr-2025Sales Order #: 0910002608Well Description: 3S-602 3S-602UWI: 50-103-20906Conoco Phillips - 3S-602 Interval 13 Plots102 <-Paste Interval 13 Plots HereBlender Chemical Plot - Bucket Test 4.20.254/20/202507:1507:2007:2507:3007:354/20/202507:40Time0.00.51.01.52.02.53.0A012345BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-III Conc (lb/Mgal)Optiflo-II Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)MO-67 Conc (gal/Mgal)AABBAA2Conoco Phillips - 3S-602 Interval 13 Plots103 <-Paste Interval 13 Plots HereADP Chemical Plots - Bucket Test 4.20.254/20/202506:1106:1206:1306:1406:154/20/202506:16Time010203040A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)AB1113Conoco Phillips - 3S-602 Interval 13 Plots104 Treatment Plot - Interval 13 DFIT4/20/202508:5009:0009:104/20/202509:20Time01000200030004000500060007000A0102030405060708090100B012345678910C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD7654Conoco Phillips - 3S-602 Interval 13 Plots105 Blender Chemical Plot - Interval 13 DFIT4/20/202508:4508:5008:554/20/202509:00Time0.00.51.01.52.02.53.0A012345BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-III Conc (lb/Mgal)Optiflo-II Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)MO-67 Conc (gal/Mgal)AABBAA654Conoco Phillips - 3S-602 Interval 13 Plots106 ADP Chemical Plots - Interval 13 DFIT4/20/202508:4008:4508:5008:5509:004/20/202509:05Time010203040A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)AB7654Conoco Phillips - 3S-602 Interval 13 Plots107 Treatment Plot - Interval 13 Step Rate Test4/20/202509:2609:2809:304/20/202509:32Time01000200030004000500060007000A0102030405060708090100B012345678910C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD93332313029Global Event Log2930313233Intersection IntersectionStep 1 Step 2 Stage At Top Perf = 5 Step 3Step 409:28:08 09:30:3309:31:41 09:32:4409:33:18TP TP1004 10561118 11541188SR SR1.090 1.9432.935 3.9334.873GBP GBP2982 29963053 30753117Conoco Phillips - 3S-602 Interval 13 Plots108 Treatment Plot - Interval 134/20/202509:3009:4009:5010:0010:1010:204/20/202510:30Time01000200030004000500060007000A0102030405060708090100B012345678910C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD122212019181716151413121110914Conoco Phillips - 3S-602 Interval 13 Plots109 Blender Chemical Plot - Interval 134/20/202509:3009:4009:5010:0010:1010:204/20/202510:30Time0.00.51.01.52.02.53.0A012345BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-III Conc (lb/Mgal)Optiflo-II Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)MO-67 Conc (gal/Mgal)AABBAA21222120191817161514131211109814Conoco Phillips - 3S-602 Interval 13 Plots110 ADP Chemical Plots - Interval 134/20/202509:3009:4009:5010:0010:1010:204/20/202510:30Time010203040A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)AB1222120191817161514131211109814Conoco Phillips - 3S-602 Interval 13 Plots111 Net Pressure Plot - Interval 1378923456710Time (min)345678923456789100010000A-5-4-3-2-1012345CNet Gauge BH Pres (psi)A Closure Pressure = 2816 psi 0 Time = 04/20/25 09:25:07 1Time-149.03NetPr0.000Slope0.000Customer: CONOCOPHILLIPS - NORTH SLOPE-EBUSJob Date: 20-Apr-2025Sales Order #: 0910002608Well Description: 3S-602 3S-602UWI: 50-103-20906Conoco Phillips - 3S-602 Interval 13 Plots112 <-Paste Interval 14 Plots HereTreatment Plot - Interval 144/20/202510:3010:4010:5011:0011:104/20/202511:20Time0100020003000400050006000A0102030405060708090100B024681012C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD1131211109876543211514Conoco Phillips - 3S-602 Interval 14 Plots113 <-Paste Interval 14 Plots HereBlender Chemical Plot - Interval 144/20/202510:3010:4010:5011:0011:104/20/202511:20Time0.00.51.01.52.02.53.0A012345BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-III Conc (lb/Mgal)Optiflo-II Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)MO-67 Conc (gal/Mgal)AABBAA1131211109876543211514Conoco Phillips - 3S-602 Interval 14 Plots114 <-Paste Interval 14 Plots HereADP Chemical Plots - Interval 144/20/202510:3010:4010:5011:0011:104/20/202511:20Time010203040A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)AB1131211109876543211514Conoco Phillips - 3S-602 Interval 14 Plots115 <-Paste Interval 14 Plots HereNet Pressure Plot - Interval 1492345610Time (min)345678923456789100010000A-5-4-3-2-1012345CNet Gauge BH Pres (psi)A Closure Pressure = 2816 psi 0 Time = 04/20/25 10:25:07 1Time-209.03NetPr0.000Slope0.000Customer: CONOCOPHILLIPS - NORTH SLOPE-EBUSJob Date: 20-Apr-2025Sales Order #: 0910002608Well Description: 3S-602 3S-602UWI: 50-103-20906Conoco Phillips - 3S-602 Interval 14 Plots116 <-Paste Interval 15 Plots HereTreatment Plot - Interval 154/20/202511:2011:3011:4011:5012:0012:104/20/202512:20Time0100020003000400050006000A0102030405060708090100B024681012C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD21131211109876543211615Conoco Phillips - 3S-602 Interval 15 Plots117 <-Paste Interval 15 Plots HereBlender Chemical Plot - Interval 154/20/202511:2011:3011:4011:5012:004/20/202512:10Time0.00.51.01.52.02.53.0A012345BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-III Conc (lb/Mgal)Optiflo-II Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)MO-67 Conc (gal/Mgal)AABBAA21131211109876543211615Conoco Phillips - 3S-602 Interval 15 Plots118 <-Paste Interval 15 Plots HereADP Chemical Plots - Interval 154/20/202511:2011:3011:4011:5012:004/20/202512:10Time010203040A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)AB2113121110987654321131615Conoco Phillips - 3S-602 Interval 15 Plots119 <-Paste Interval 15 Plots HereNet Pressure Plot - Interval 15567892345610Time (min)345678923456789100010000A-5-4-3-2-1012345CNet Gauge BH Pres (psi)A Closure Pressure = 2816 psi 0 Time = 04/20/25 11:20:07 1Time-264.03NetPr0.000Slope0.000Customer: CONOCOPHILLIPS - NORTH SLOPE-EBUSJob Date: 20-Apr-2025Sales Order #: 0910002608Well Description: 3S-602 3S-602UWI: 50-103-20906Conoco Phillips - 3S-602 Interval 15 Plots120 <-Paste Interval 16 Plots HereTreatment Plot - Interval 164/20/202512:1512:2012:2512:3012:3512:4012:4512:504/20/202512:55Time0100020003000400050006000A0102030405060708090100B024681012C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD21131211109876543211716Conoco Phillips - 3S-602 Interval 16 Plots121 <-Paste Interval 16 Plots HereBlender Chemical Plot - Interval 164/20/202512:1512:2012:2512:3012:3512:4012:454/20/202512:50Time0.00.51.01.52.02.53.0A012345BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-III Conc (lb/Mgal)Optiflo-II Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)MO-67 Conc (gal/Mgal)AABBAA21131211109876543211716Conoco Phillips - 3S-602 Interval 16 Plots122 <-Paste Interval 16 Plots HereADP Chemical Plots - Interval 164/20/202512:1512:2012:2512:3012:3512:4012:454/20/202512:50Time010203040A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)AB21131211109876543211716Conoco Phillips - 3S-602 Interval 16 Plots123 <-Paste Interval 16 Plots HereNet Pressure Plot - Interval 1678923410Time (min)345678923456789100010000A-5-4-3-2-1012345CNet Gauge BH Pres (psi)A Closure Pressure = 2816 psi 0 Time = 04/20/25 12:10:07 1Time-314.03NetPr0.000Slope0.000Customer: CONOCOPHILLIPS - NORTH SLOPE-EBUSJob Date: 20-Apr-2025Sales Order #: 0910002608Well Description: 3S-602 3S-602UWI: 50-103-20906Conoco Phillips - 3S-602 Interval 16 Plots124 <-Paste Interval 17 Plots HereTreatment Plot - Interval 174/20/202512:5013:0013:1013:204/20/202513:30Time0100020003000400050006000A0102030405060708090100B024681012C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD141312111098765432117Conoco Phillips - 3S-602 Interval 17 Plots125 <-Paste Interval 17 Plots HereBlender Chemical Plot - Interval 174/20/202512:5012:5513:0013:0513:1013:1513:2013:254/20/202513:30Time0.00.51.01.52.02.53.0A012345BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-III Conc (lb/Mgal)Optiflo-II Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)MO-67 Conc (gal/Mgal)AABBAA141312111098765432117Conoco Phillips - 3S-602 Interval 17 Plots126 <-Paste Interval 17 Plots HereADP Chemical Plots - Interval 174/20/202512:5012:5513:0013:0513:1013:1513:2013:254/20/202513:30Time010203040A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)AB141312111098765432117Conoco Phillips - 3S-602 Interval 17 Plots127 <-Paste Interval 17 Plots HereNet Pressure Plot - Interval 172345678923410Time (min)345678923456789100010000A-5-4-3-2-1012345CNet Gauge BH Pres (psi)A Closure Pressure = 2816 psi 0 Time = 04/20/25 12:53:07 1Time-357.03NetPr0.000Slope0.000Customer: CONOCOPHILLIPS - NORTH SLOPE-EBUSJob Date: 20-Apr-2025Sales Order #: 0910002608Well Description: 3S-602 3S-602UWI: 50-103-20906Conoco Phillips - 3S-602 Interval 17 Plots128 <-Paste Interval 18 Plots HereePRV Test - 4.21.254/21/202507:2907:3007:3107:3207:3307:3407:354/21/202507:36Time010002000300040005000600070008000900010000Treating 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 IA07:29:17 07:30:5107:33:27 07:35:39TP TP698.1 689.7732.1 757.7TPP TPP715.3 711.2747.0 723.3IGKP IGKP900.0 900.0900.0 900.0Conoco Phillips - 3S-602 Interval 18 Plots129 <-Paste Interval 18 Plots HerePressure Test - 4.21.254/21/202507:3807:4007:4207:4407:4607:4807:504/21/202507:52Time010002000300040005000600070008000900010000Treating Pressure (psi)Treating Pressure @Pump (psi)I1 Global Kickout Pressure (psi)P2 Kickout Pressure (psi)Pop-off (psi)21211109Global Event Log9101112Intersection IntersectionPressure Test - Global Pressure Test - LocalsPressure Test - Max Pressure Test - Pass07:37:34 07:37:4107:44:45 07:49:48TP TP759.6 759.79415 9396TPP TPP188.1 222.09438 9131IGKP IGKP25.00 95009500 9500PKP PKP500.4 155.69500 9500Customer: CONOCOPHILLIPS - NORTH SLOPE-EBUSJob Date: 21-Apr-2025Sales Order #: 0910002608Well Description: 3S-602 3S-602UWI: 50-103-20906Conoco Phillips - 3S-602 Interval 18 Plots130 <-Paste Interval 18 Plots HereBlender Chemical Plot - Bucket Test 4.21.254/21/202507:2007:2507:3007:3507:404/21/202507:45Time0.00.51.01.52.02.53.0A012345BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-III Conc (lb/Mgal)Optiflo-II Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)MO-67 Conc (gal/Mgal)AABBAAConoco Phillips - 3S-602 Interval 18 Plots131 <-Paste Interval 18 Plots HereADP Chemical Plots - Bucket Test 4.21.254/21/202506:52:4006:53:0006:53:2006:53:4006:54:0006:54:2006:54:404/21/202506:55:00Time010203040A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)ABConoco Phillips - 3S-602 Interval 18 Plots132 Treatment Plot - Interval 184/21/202508:2008:3008:4008:5009:004/21/202509:10Time0100020003000400050006000A0102030405060708090100B012345678910C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD2118171615141312111098765419Conoco Phillips - 3S-602 Interval 18 Plots133 Blender Chemical Plot - Interval 184/21/202508:2008:3008:4008:504/21/202509:00Time0.00.51.01.52.02.53.0A012345BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-III Conc (lb/Mgal)Optiflo-II Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)MO-67 Conc (gal/Mgal)AABBAA2118171615141312111098765419Conoco Phillips - 3S-602 Interval 18 Plots134 ADP Chemical Plots - Interval 184/21/202508:2008:3008:4008:504/21/202509:00Time010203040A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)AB2118171615141312111098765419Conoco Phillips - 3S-602 Interval 18 Plots135 Net Pressure Plot - Interval 1823456Time (min)2345678923456789100100010000A-5-4-3-2-1012345CNet Gauge BH Pres (psi)A Closure Pressure = 2742 psi 0 Time = 04/21/25 08:10:29 1Time-69.04NetPr0.000Slope0.000Customer: CONOCOPHILLIPS - NORTH SLOPE-EBUSJob Date: 21-Apr-2025Sales Order #: 0910002608Well Description: 3S-602 3S-602UWI: 50-103-20906Conoco Phillips - 3S-602 Interval 18 Plots136 <-Paste Interval 19 Plots HereTreatment Plot - Interval 194/21/202509:1009:2009:304/21/202509:40Time0100020003000400050006000A0102030405060708090100B012345678910C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD2113121110987654321182019Conoco Phillips - 3S-602 Interval 19 Plots137 <-Paste Interval 19 Plots HereBlender Chemical Plot - Interval 194/21/202509:0509:1009:1509:2009:2509:3009:354/21/202509:40Time0.00.51.01.52.02.53.0A012345BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-III Conc (lb/Mgal)Optiflo-II Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)MO-67 Conc (gal/Mgal)AABBAA21131211109876543212019Conoco Phillips - 3S-602 Interval 19 Plots138 <-Paste Interval 19 Plots HereADP Chemical Plots - Interval 194/21/202509:0509:1009:1509:2009:2509:3009:354/21/202509:40Time010203040A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)AB21131211109876543212019Conoco Phillips - 3S-602 Interval 19 Plots139 <-Paste Interval 19 Plots HereNet Pressure Plot - Interval 192345Time (min)2345678923456789100100010000A-5-4-3-2-1012345CNet Gauge BH Pres (psi)A Closure Pressure = 2742 psi 0 Time = 04/21/25 08:50:29 1Time-109.04NetPr0.000Slope0.000Customer: CONOCOPHILLIPS - NORTH SLOPE-EBUSJob Date: 21-Apr-2025Sales Order #: 0910002608Well Description: 3S-602 3S-602UWI: 50-103-20906Conoco Phillips - 3S-602 Interval 19 Plots140 <-Paste Interval 20 Plots HereTreatment Plot - Interval 204/21/202509:4009:5010:0010:104/21/202510:20Time0100020003000400050006000A0102030405060708090100B012345678910C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD21131211109876543212120Conoco Phillips - 3S-602 Interval 20 Plots141 <-Paste Interval 20 Plots HereBlender Chemical Plot - Interval 204/21/202509:4009:4509:5009:5510:0010:0510:1010:154/21/202510:20Time0.00.51.01.52.02.53.0A012345BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-III Conc (lb/Mgal)Optiflo-II Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)MO-67 Conc (gal/Mgal)AABBAA21131211109876543212120Conoco Phillips - 3S-602 Interval 20 Plots142 <-Paste Interval 20 Plots HereADP Chemical Plots - Interval 204/21/202509:4009:4509:5009:5510:0010:0510:1010:154/21/202510:20Time010203040A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)AB2113121110987654321132120Conoco Phillips - 3S-602 Interval 20 Plots143 <-Paste Interval 20 Plots HereNet Pressure Plot - Interval 20234Time (min)2345678923456789100100010000A-5-4-3-2-1012345CNet Gauge BH Pres (psi)A Closure Pressure = 2742 psi 0 Time = 04/21/25 09:34:29 1Time-153.04NetPr0.000Slope0.000Customer: CONOCOPHILLIPS - NORTH SLOPE-EBUSJob Date: 21-Apr-2025Sales Order #: 0910002608Well Description: 3S-602 3S-602UWI: 50-103-20906Conoco Phillips - 3S-602 Interval 20 Plots144 <-Paste Interval 21 Plots HereTreatment Plot - Interval 214/21/202510:2010:3010:4010:504/21/202511:00Time0100020003000400050006000A0102030405060708090100B012345678910C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD21131211109876543212221Conoco Phillips - 3S-602 Interval 21 Plots145 <-Paste Interval 21 Plots HereBlender Chemical Plot - Interval 214/21/202510:2010:2510:3010:3510:4010:4510:504/21/202510:55Time0.00.51.01.52.02.53.0A012345BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-III Conc (lb/Mgal)Optiflo-II Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)MO-67 Conc (gal/Mgal)AABBAA21131211109876543212221Conoco Phillips - 3S-602 Interval 21 Plots146 <-Paste Interval 21 Plots HereADP Chemical Plots - Interval 214/21/202510:2010:2510:3010:3510:4010:4510:504/21/202510:55Time010203040A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)AB2113121110987654321132221Conoco Phillips - 3S-602 Interval 21 Plots147 <-Paste Interval 21 Plots HereNet Pressure Plot - Interval 212345Time (min)2345678923456789100100010000A-5-4-3-2-1012345CNet Gauge BH Pres (psi)A Closure Pressure = 2742 psi 0 Time = 04/21/25 10:05:29 1Time-184.04NetPr0.000Slope0.000Customer: CONOCOPHILLIPS - NORTH SLOPE-EBUSJob Date: 21-Apr-2025Sales Order #: 0910002608Well Description: 3S-602 3S-602UWI: 50-103-20906Conoco Phillips - 3S-602 Interval 21 Plots148 <-Paste Interval 22 Plots HereTreatment Plot - Interval 224/21/202511:0011:1011:204/21/202511:30Time0100020003000400050006000A0102030405060708090100B012345678910C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD21131211109876543212322Conoco Phillips - 3S-602 Interval 22 Plots149 <-Paste Interval 22 Plots HereBlender Chemical Plot - Interval 224/21/202510:5511:0011:0511:1011:1511:2011:2511:304/21/202511:35Time0.00.51.01.52.02.53.0A012345BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-III Conc (lb/Mgal)Optiflo-II Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)MO-67 Conc (gal/Mgal)AABBAA21131211109876543212322Conoco Phillips - 3S-602 Interval 22 Plots150 <-Paste Interval 22 Plots HereADP Chemical Plots - Interval 224/21/202510:5511:0011:0511:1011:1511:2011:2511:304/21/202511:35Time010203040A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)AB21131211109876543212322Conoco Phillips - 3S-602 Interval 22 Plots151 <-Paste Interval 22 Plots HereNet Pressure Plot - Interval 226789Time (min)2345678923456789100100010000A-5-4-3-2-1012345CNet Gauge BH Pres (psi)A Closure Pressure = 2742 psi 0 Time = 04/21/25 10:05:29 1Time-184.04NetPr0.000Slope0.000Customer: CONOCOPHILLIPS - NORTH SLOPE-EBUSJob Date: 21-Apr-2025Sales Order #: 0910002608Well Description: 3S-602 3S-602UWI: 50-103-20906Conoco Phillips - 3S-602 Interval 22 Plots152 <-Paste Interval 23 Plots HereTreatment Plot - Interval 234/21/202511:4011:5012:004/21/202512:10Time0100020003000400050006000A0102030405060708090100B012345678910C0255075100125150DTreating Pressure (psi)Slurry Rate (bpm)Slurry Proppant Conc (lb/gal)BH Proppant Conc (lb/gal)Gauge BH Pres (psi)Actual BH Temp (°F)ABCCAD141312111098765432123Conoco Phillips - 3S-602 Interval 23 Plots153 <-Paste Interval 23 Plots HereBlender Chemical Plot - Interval 234/21/202511:3511:4011:4511:5011:5512:0012:054/21/202512:10Time0.00.51.01.52.02.53.0A012345BBC-140 X2 Conc (gal/Mgal)CL-28M Conc (gal/Mgal)Optiflo-III Conc (lb/Mgal)Optiflo-II Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)MO-67 Conc (gal/Mgal)AABBAA141312111098765432123Conoco Phillips - 3S-602 Interval 23 Plots154 <-Paste Interval 23 Plots HereADP Chemical Plots - Interval 234/21/202511:3511:4011:4511:5011:5512:0012:054/21/202512:10Time010203040A0.00.20.40.60.81.01.21.41.61.82.0BWG-36 Conc (lb/Mgal)Losurf-300D Conc (gal/Mgal)AB141312111098765432123Conoco Phillips - 3S-602 Interval 23 Plots155 <-Paste Interval 23 Plots HereNet Pressure Plot - Interval 2378923410Time (min)2345678923456789100100010000A-5-4-3-2-1012345CNet Gauge BH Pres (psi)A Closure Pressure = 2742 psi 0 Time = 04/21/25 11:28:29 1Time-267.04NetPr0.000Slope0.000Customer: CONOCOPHILLIPS - NORTH SLOPE-EBUSJob Date: 21-Apr-2025Sales Order #: 0910002608Well Description: 3S-602 3S-602UWI: 50-103-20906Conoco Phillips - 3S-602 Interval 23 Plots156 Sales Order# - - - - - - - - - - Event Log Sieve Analysis Fann 15 Minute Field Break Test Real-Time QC Well Summary Stimulation Treatment Appendix Chemical Summary Planned Design Water Straps Water Analysis Prepared for: Manabu Nozaki April 22, 2025 Harrison Bay County, AK 0910002608 Conoco Phillips 3S-602 Intervals 1-23 Moraine Moraine Formation API: 50-103-20906 Conoco Phillips - 3S-602 Appendix 157 Interval DateDesigned Proppant (lbs)Proppant in Formation (lbs)Designed Fluid (bbl)Vol Clean (bbl)Vol Slurry (bbl)Pad Percentage Design Pad Percentage Actual Proppant Aggressiveness (lb/bbl Clean)Notes1 4/13/2025 203,000 202,194 3,047 2792 3,007 32.0 31.8 1212 4/13/2025 203,000 203,254 2,491 2529 2,745 32.0 31.6 1233 4/13/2025 203,000 201,556 3,150 3088 3,302 32.0 32.1 1284 4/14/2025 203,000 205,646 2,314 2264 2,482 32.0 31.6 1545 4/14/2025 203,000 203,914 1,572 1620 1,836 30.0 29.0 1916 4/14/2025 203,000 202,934 1,572 1581 1,797 30.0 29.6 1987 4/14/2025 203,000 203,399 1,837 1839 2,055 30.0 29.5 1978 4/15/2025 203,000 203,874 1,844 1729 1,946 30.0 29.7 1979 4/15/2025 203,000 202,174 1,572 1589 1,803 30.0 29.5 19510 4/15/2025 203,000 203,153 1,572 1579 1,795 30.0 29.6 19711 4/15/2025 203,000 204,926 1,572 1593 1,810 30.0 29.5 19712 4/15/2025 203,000 203,665 1,792 1820 2,036 30.0 29.5 19613 4/20/2025 203,000 204,379 2,081 1971 2,188 30.0 29.4 19714 4/20/2025 203,000 202,823 1,572 1582 1,797 30.0 29.3 19615 4/20/2025 203,000 205,247 1,572 1610 1,828 30.0 28.9 19316 4/20/2025 143,000 143,948 1,116 1152 1,305 30.0 28.8 19017 4/20/2025 143,000 145,156 1,296 1287 1,442 30.0 29.6 20218 4/21/2025 143,000 143,947 1,388 1265 1,418 30.0 29.0 19619 4/21/2025 143,000 141,668 1,116 1117 1,268 30.0 29.2 19520 4/21/2025 143,000 142,923 1,116 1118 1,270 30.0 29.3 19621 4/21/2025 143,000 142,132 1,116 1128 1,279 30.0 29.1 19322 4/21/2025 143,000 142,870 1,116 1139 1,291 30.0 29.1 19223 4/21/2025 143,000 143,058 1,250 1273 1,425 30.0 29.5 193 3S-602 Interval HighlightsConoco Phillips - 3S-602Well Summary158 CustomerConoco Phillips FormationMoraineLease3S-602API50-103-20906DateInterval 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)Prime Up000000001109 30 122 74 3584 206 207 722122 28 106 69 3163 190 188 03119 22 137 57 3945 204 205 04105 22 102 59 2858 166 166 0564 16 67 50 2076 121 121 0668 15 68 40 2030 118 118 0773 14 78 36 2168 145 145 0871 18 72 43 2210 126 126 60968 17 68 40 2132 119 118 01067 17 67 41 2027 119 119 01168 17 69 41 2004 119 119 01276 14 84 35 2360 117 118 01375 17 83 40 2560 145 145 631467 17 67 37 2020 119 118 01569 17 70 38 2093 121 121 01649 12 48 26 1420 85 86 01750 12 67 24 1460 100 100 01851 12 52 28 1672 101 101 601944 11 47 27 1385 94 93 02045 11 48 26 1391 94 95 02145 11 48 27 1476 94 94 02246 11 49 27 1435 95 94 02344 14 51 20 1669 102 103 0Total 1595 375 1670 905 49138 2900 2900 255w/o Prime Up1595 375 1670 905 49138 2900 2900 255Interval4/13/2025Dry AdditivesLiquid AdditivesConoco Phillips - 3S-602 Chemical Summary159 CUSTOMERConoco Phillips FALSEAPI BFD (lb/gal)8.48LAT 70.39430569LEASE3S-602SALES ORDERBHST (°F)141LONG-150.1949722FORMATIONMoraineDATE 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-In1:57:07 1-2 Freeze Protect Prime Up Pressure Test 5 1,000 24 24 0:04:46 1:57:07 1-3 Shut-In Shut-In1:52:21 1-4 30# Linear Arsenal Sleeve Shift 5 1,260 30 30 0:06:00 1:52:21 1.00 30.00 1.75 1.75 0.151-5 30# Linear DFIT 10 2,100 50 50 0:05:00 1:46:21 1.00 30.00 1.75 1.75 0.151-6 Shut-In Shut-In1:41:21 1-7 Shut-In Step Rate Test 15 8,400 200 200 0:13:20 1:41:21 1-8 30# Hybor G-i Establish Stable Fluid 15 8,400 200 200 0:13:20 1:28:01 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.151-9 30# Hybor G-i Pad 37 24,250 577 577 0:15:36 1:14:41 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.151-10 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:59:05 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.151-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 12,000 286 298 12,000 0:08:04 0:51:16 1.00 0.25 1.00 0.60 30.00 1.75 1.750.151-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 16,000 381 415 32,000 0:11:14 0:43:12 1.00 0.25 1.00 0.60 30.00 1.75 1.750.151-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 16,000 381 432 48,000 0:11:42 0:31:58 1.00 0.25 1.00 0.60 30.00 1.75 1.750.151-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 10,000 238 281 40,000 0:07:37 0:20:15 1.00 0.25 1.00 0.60 30.00 1.75 1.750.151-15 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 8,000 190 229 36,000 0:06:12 0:12:39 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.151-16 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 6,400 152 186 32,000 0:05:03 0:06:27 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.151-17 30# Hybor G-i Spacer and Ball Drop 37 2,155 51 51 0:01:23 0:01:23 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.152-1 30# Hybor G-i Pad 37 23,550 561 561 0:15:09 1:13:17 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.152-2 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:58:08 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.152-3 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 12,000 286 298 12,000 0:08:04 0:50:19 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.152-4 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 15,000 357 389 30,000 0:10:32 0:42:15 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.152-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 16,600 395 448 49,800 0:12:09 0:31:43 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.152-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 7,500 179 210 30,000 0:05:42 0:19:34 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.152-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 6,200 148 177 27,900 0:04:49 0:13:52 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.152-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 5,220 124 152 26,100 0:04:07 0:09:03 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.152-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 4,400 105 130 24,200 0:03:32 0:04:56 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.152-10 30# Hybor G-i Spacer and Ball Drop 37 2,155 51 51 0:01:23 0:01:23 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.153-1 30# Linear Displace Ball to Seat 37 11,453 273 273 0:07:22 1:41:34 1.00 30.00 1.75 1.75 0.153-2 30# Hybor G-i Establish Stable Fluid 15 8,400 200 200 0:13:20 1:34:12 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.153-3 30# Hybor G-i Pad 37 22,650 539 539 0:14:35 1:20:52 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.153-4 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 1:06:17 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.153-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 12,000 286 298 12,000 0:08:04 0:58:29 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.153-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 15,000 357 389 30,000 0:10:32 0:50:24 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.153-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 14,000 333 378 42,000 0:10:14 0:39:52 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.153-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 10,000 238 281 40,000 0:07:37 0:29:38 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.153-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 8,000 190 233 40,000 0:06:19 0:22:01 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.153-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 6,000 143 181 36,000 0:04:55 0:15:42 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.153-11 30# Linear Flush 37 11,320 270 270 0:07:17 0:10:47 1.00 30.00 1.75 1.75 0.153-12 Freeze Protect Freeze Protect 10 1,470 35 35 0:03:30 0:03:30 3-13 Shut-In Shut-In4/13/25Liquid Additives Dry Additives50-103-209060910002608Interval 1Moraine@ 18671.17 - 18675.51 ft 138.8 °F"Alpha SleeveInterval 2Moraine@ 18190.6 - 18194.94 ft 138.9 °F"Frac Sleeve 1Interval 3Moraine@ 17709.27 - 17713.61 ft 139.6 °F"Frac Sleeve 2Conoco Phillips - 3S-602Planned Design160 CUSTOMERConoco Phillips FALSEAPI BFD (lb/gal)8.48LAT 70.39430569LEASE3S-602SALES ORDERBHST (°F)141LONG-150.1949722FORMATIONMoraineDATE 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)4/13/25Liquid Additives Dry Additives50-103-2090609100026084-1 Shut-In Shut-In1:24:52 4-2 Freeze Protect Prime Up Pressure Test 5 1,764 42 42 0:08:24 1:24:52 4-3 Shut-In Shut-In1:16:28 4-4 30# Linear Spacer and Dart Drop 15 1,260 30 30 0:02:00 1:16:28 1.00 30.00 1.75 1.75 0.154-5 30# Hybor G-i Establish Stable Fluid 15 8,400 200 200 0:13:20 1:14:28 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.154-6 30# Hybor G-i Pad 37 17,480 416 416 0:11:15 1:01:08 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.154-7 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:49:53 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.154-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 8,500 202 211 8,500 0:05:43 0:42:05 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.154-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 8,500 202 220 17,000 0:05:58 0:36:21 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.154-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 8,000 190 216 24,000 0:05:51 0:30:23 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.154-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 9,000 214 253 36,000 0:06:51 0:24:32 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.154-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 8,000 190 233 40,000 0:06:19 0:17:41 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.154-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 7,000 167 211 42,000 0:05:44 0:11:22 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.154-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37 5,000 119 154 32,500 0:04:10 0:05:38 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.154-15 30# Hybor G-i Spacer and Ball Drop 37 2,268 54 54 0:01:28 0:01:28 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.155-1 30# Hybor G-i Pad 37 9,710 231 231 0:06:15 0:48:27 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.155-2 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:42:12 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.155-3 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 2,000 48 50 2,000 0:01:21 0:34:24 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.155-4 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 2,500 60 65 5,000 0:01:45 0:33:03 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.155-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.000 37 4,000 95 108 12,000 0:02:56 0:31:18 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.155-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 4,850 115 136 19,400 0:03:41 0:28:22 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.155-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 5,000 119 143 22,500 0:03:53 0:24:41 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.155-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 5,410 129 158 27,050 0:04:17 0:20:48 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.155-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 5,500 131 163 30,250 0:04:26 0:16:31 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.155-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 5,800 138 175 34,800 0:04:45 0:12:06 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.155-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37 4,000 95 123 26,000 0:03:20 0:07:21 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.155-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37 3,000 71 94 21,000 0:02:33 0:04:00 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.155-13 30# Hybor G-i Spacer and Ball Drop 37 2,268 54 54 0:01:28 0:01:28 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.156-1 30# Hybor G-i Pad 37 9,710 231 231 0:06:15 0:48:27 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.156-2 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:42:12 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.156-3 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 2,000 48 50 2,000 0:01:21 0:34:24 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.156-4 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 2,500 60 65 5,000 0:01:45 0:33:03 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.156-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 4,000 95 108 12,000 0:02:56 0:31:18 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.156-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 4,850 115 136 19,400 0:03:41 0:28:22 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.156-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 5,000 119 143 22,500 0:03:53 0:24:41 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.156-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 5,410 129 158 27,050 0:04:17 0:20:48 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.156-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 5,500 131 163 30,250 0:04:26 0:16:31 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.156-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 5,800 138 175 34,800 0:04:45 0:12:06 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.156-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37 4,000 95 123 26,000 0:03:20 0:07:21 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.156-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37 3,000 71 94 21,000 0:02:33 0:04:00 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.156-13 30# Hybor G-i Spacer and Ball Drop 37 2,268 54 54 0:01:28 0:01:28 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.157-1 30# Hybor G-i Pad 37 9,710 231 231 0:06:15 1:02:31 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.157-2 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:56:16 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.157-3 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.0000 37 2,000 48 50 2,000 0:01:21 0:48:27 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.157-4 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 2,500 60 65 5,000 0:01:45 0:47:07 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.157-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 4,000 95 108 12,000 0:02:56 0:45:21 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.157-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 4,850 115 136 19,400 0:03:41 0:42:26 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.157-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 5,000 119 143 22,500 0:03:53 0:38:44 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.157-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 5,410 129 158 27,050 0:04:17 0:34:52 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.157-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 5,500 131 163 30,250 0:04:26 0:30:35 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.157-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 5,800 138 175 34,800 0:04:45 0:26:10 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.157-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37 4,000 95 123 26,000 0:03:20 0:21:24 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.157-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37 3,000 71 94 21,000 0:02:33 0:18:04 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.157-13 30# Linear Flush 37 11,691 278 278 0:07:31 0:15:31 1.00 30.00 1.75 1.75 0.157-14 Freeze Protect Freeze Protect 5 1,680 40 40 0:08:00 0:08:00 7-15 Shut-In Shut-InInterval 4Moraine@ 17229.72 - 17234.06 ft 139.5 °F"Frac Sleeve 3Interval 5Moraine@ 16707.05 - 16711.39 ft 139.4 °F"Frac Sleeve 4Interval 6Moraine@ 16184.78 - 16189.12 ft 139.3 °F"Frac Sleeve 5Interval 7Moraine@ 15662.36 - 15666.7 ft 139.3 °F"Frac Sleeve 6Conoco Phillips - 3S-602Planned Design161 CUSTOMERConoco Phillips FALSEAPI BFD (lb/gal)8.48LAT 70.39430569LEASE3S-602SALES ORDERBHST (°F)141LONG-150.1949722FORMATIONMoraineDATE 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)4/13/25Liquid Additives Dry Additives50-103-2090609100026088-1 Shut-In Shut-In1:08:51 8-2 Freeze Protect Prime Up Pressure Test 5 1,764 42 42 0:08:24 1:08:51 8-3 Shut-In Shut-In1:00:27 8-4 30# Linear Spacer and Ball Drop 15 1,260 30 30 0:02:00 1:00:27 1.00 30.00 1.75 1.75 0.158-5 30# Hybor G-i Establish Stable Fluid 20 8,400 200 200 0:10:00 0:58:27 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.158-6 30# Hybor G-i Pad 37 9,710 231 231 0:06:15 0:48:27 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.158-7 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:42:12 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.158-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 2,000 48 50 2,000 0:01:21 0:34:24 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.158-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 2,500 60 65 5,000 0:01:45 0:33:03 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.158-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 4,000 95 108 12,000 0:02:56 0:31:18 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.158-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 4,850 115 136 19,400 0:03:41 0:28:22 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.158-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 5,000 119 143 22,500 0:03:53 0:24:41 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.158-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 5,410 129 158 27,050 0:04:17 0:20:48 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.158-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 5,500 131 163 30,250 0:04:26 0:16:31 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.158-15 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 5,800 138 175 34,800 0:04:45 0:12:06 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.158-16 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37 4,000 95 123 26,000 0:03:20 0:07:21 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.158-17 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37 3,000 71 94 21,000 0:02:33 0:04:00 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.158-18 30# Hybor G-i Spacer and Ball Drop 37 2,268 54 54 0:01:28 0:01:28 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.159-1 30# Hybor G-i Pad 37 9,710 231 231 0:06:15 0:48:27 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.159-2 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:42:12 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.159-3 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 2,000 48 50 2,000 0:01:21 0:34:24 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.159-4 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 2,500 60 65 5,000 0:01:45 0:33:03 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.159-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 4,000 95 108 12,000 0:02:56 0:31:18 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.159-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 4,850 115 136 19,400 0:03:41 0:28:22 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.159-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.5000 37 5,000 119 143 22,500 0:03:53 0:24:41 1.00 0.25 1.00 0.60 30.00 1.75 1.750.159-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 5,410 129 158 27,050 0:04:17 0:20:48 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.159-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 5,500 131 163 30,250 0:04:26 0:16:31 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.159-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 5,800 138 175 34,800 0:04:45 0:12:06 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.159-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37 4,000 95 123 26,000 0:03:20 0:07:21 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.159-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37 3,000 71 94 21,000 0:02:33 0:04:00 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.159-13 30# Hybor G-i Spacer and Ball Drop 37 2,268 54 54 0:01:28 0:01:28 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1510-1 30# Hybor G-i Pad 37 9,710 231 231 0:06:15 0:48:27 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1510-2 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:42:12 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1510-3 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 2,000 48 50 2,000 0:01:21 0:34:24 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1510-4 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 2,500 60 65 5,000 0:01:45 0:33:03 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1510-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 4,000 95 108 12,000 0:02:56 0:31:18 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1510-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 4,850 115 136 19,400 0:03:41 0:28:22 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1510-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 5,000 119 143 22,500 0:03:53 0:24:41 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1510-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 5,410 129 158 27,050 0:04:17 0:20:48 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1510-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 5,500 131 163 30,250 0:04:26 0:16:31 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1510-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 5,800 138 175 34,800 0:04:45 0:12:06 1.00 0.25 1.00 0.60 30.00 1.75 1.750.1510-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37 4,000 95 123 26,000 0:03:20 0:07:21 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1510-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37 3,000 71 94 21,000 0:02:33 0:04:00 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1510-13 30# Hybor G-i Spacer and Ball Drop 37 2,268 54 54 0:01:28 0:01:28 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1511-1 30# Hybor G-i Pad 37 9,710 231 231 0:06:15 0:48:27 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1511-2 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:42:12 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1511-3 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 2,000 48 50 2,000 0:01:21 0:34:24 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1511-4 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 2,500 60 65 5,000 0:01:45 0:33:03 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1511-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 4,000 95 108 12,000 0:02:56 0:31:18 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1511-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 4,850 115 136 19,400 0:03:41 0:28:22 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1511-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 5,000 119 143 22,500 0:03:53 0:24:41 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1511-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 5,410 129 158 27,050 0:04:17 0:20:48 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1511-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 5,500 131 163 30,250 0:04:26 0:16:31 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1511-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 5,800 138 175 34,800 0:04:45 0:12:06 1.00 0.25 1.00 0.60 30.00 1.75 1.750.1511-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37 4,000 95 123 26,000 0:03:20 0:07:21 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1511-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37 3,000 71 94 21,000 0:02:33 0:04:00 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1511-13 30# Hybor G-i Spacer and Ball Drop 37 2,268 54 54 0:01:28 0:01:28 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1512-1 30# Hybor G-i Pad 37 9,710 231 231 0:06:15 0:56:57 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1512-2 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:50:42 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1512-3 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 2,000 48 50 2,000 0:01:21 0:42:53 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1512-4 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 2,500 60 65 5,000 0:01:45 0:41:32 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1512-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 4,000 95 108 12,000 0:02:56 0:39:47 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1512-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 4,850 115 136 19,400 0:03:41 0:36:51 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1512-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 5,000 119 143 22,500 0:03:53 0:33:10 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1512-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 5,410 129 158 27,050 0:04:17 0:29:17 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1512-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 5,500 131 163 30,250 0:04:26 0:25:01 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1512-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 5,800 138 175 34,800 0:04:45 0:20:35 1.00 0.25 1.00 0.60 30.00 1.75 1.750.1512-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37 4,000 95 123 26,000 0:03:20 0:15:50 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1512-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37 3,000 71 94 21,000 0:02:33 0:12:30 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1512-13 30# Linear Flush 37 10,024 239 239 0:06:27 0:09:57 1.00 30.00 1.75 1.75 0.1512-14 Freeze Protect Freeze Protect 10 1,470 35 35 0:03:30 0:03:30 12-15 Shut-In Shut-InInterval 12Moraine@ 13053.84 - 13058.18 ft 139.3 °F"Frac Sleeve 11Interval 9Moraine@ 14618.15 - 14622.49 ft 139.2 °F"Frac Sleeve 8Interval 10Moraine@ 14098.94 - 14103.28 ft 139.1 °F"Frac Sleeve 9Interval 11Moraine@ 13576.44 - 13580.78 ft 139.1 °F"Frac Sleeve 10Interval 8Moraine@ 15140.23 - 15144.57 ft 139.3 °F"Frac Sleeve 7Conoco Phillips - 3S-602Planned Design162 CUSTOMERConoco Phillips FALSEAPI BFD (lb/gal)8.48LAT 70.39430569LEASE3S-602SALES ORDERBHST (°F)141LONG-150.1949722FORMATIONMoraineDATE 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)4/13/25Liquid Additives Dry Additives50-103-20906091000260813-1 Shut-In Shut-In1:26:51 13-2 Freeze Protect Prime Up Pressure Test 5 1,000 24 24 0:04:46 1:26:51 13-3 Shut-In Shut-In1:22:05 13-4 30# Linear Spacer and Ball Drop 15 1,260 30 30 0:02:00 1:22:05 1.00 30.00 1.75 1.75 0.1513-5 30# Linear Displace Dart to Seat 15 8,010 191 191 0:12:43 1:20:05 1.00 30.00 1.75 1.75 0.1513-6 30# Linear DFIT 10 1,680 40 40 0:04:00 1:07:22 1.00 30.00 1.75 1.75 0.1513-7 Shut-In Shut-In1:03:22 13-8 30# Linear Step Rate Test 15 1,000 24 24 0:01:35 1:03:22 1.00 30.00 1.75 1.75 0.1513-9 30# Hybor G-i Establish Stable Fluid 15 8,400 200 200 0:13:20 1:01:47 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1513-10 30# Hybor G-i Pad 37 9,710 231 231 0:06:15 0:48:27 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1513-11 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:42:12 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1513-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 2,000 48 50 2,000 0:01:21 0:34:24 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1513-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 2,500 60 65 5,000 0:01:45 0:33:03 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1513-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 4,000 95 108 12,000 0:02:56 0:31:18 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1513-15 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 4,850 115 136 19,400 0:03:41 0:28:22 1.00 0.25 1.00 0.60 30.00 1.75 1.750.1513-16 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 5,000 119 143 22,500 0:03:53 0:24:41 1.00 0.25 1.00 0.60 30.00 1.75 1.750.1513-17 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 5,410 129 158 27,050 0:04:17 0:20:48 1.00 0.25 1.00 0.60 30.00 1.75 1.750.1513-18 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 5,500 131 163 30,250 0:04:26 0:16:31 1.00 0.25 1.00 0.60 30.00 1.75 1.750.1513-19 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 5,800 138 175 34,800 0:04:45 0:12:06 1.00 0.25 1.00 0.60 30.00 1.75 1.750.1513-20 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37 4,000 95 123 26,000 0:03:20 0:07:21 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1513-21 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37 3,000 71 94 21,000 0:02:33 0:04:00 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1513-22 30# Hybor G-i Spacer and Ball Drop 37 2,268 54 54 0:01:28 0:01:28 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1514-1 30# Hybor G-i Pad 37 9,710 231 231 0:06:15 0:48:27 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1514-2 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:42:12 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1514-3 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 2,000 48 50 2,000 0:01:21 0:34:24 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1514-4 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 2,500 60 65 5,000 0:01:45 0:33:03 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1514-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 4,000 95 108 12,000 0:02:56 0:31:18 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1514-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 4,850 115 136 19,400 0:03:41 0:28:22 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1514-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 5,000 119 143 22,500 0:03:53 0:24:41 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1514-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 5,410 129 158 27,050 0:04:17 0:20:48 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1514-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 5,500 131 163 30,250 0:04:26 0:16:31 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1514-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 5,800 138 175 34,800 0:04:45 0:12:06 1.00 0.25 1.00 0.60 30.00 1.75 1.750.1514-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37 4,000 95 123 26,000 0:03:20 0:07:21 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1514-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37 3,000 71 94 21,000 0:02:33 0:04:00 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1514-13 30# Hybor G-i Spacer and Ball Drop 37 2,268 54 54 0:01:28 0:01:28 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1515-1 30# Hybor G-i Pad 37 9,710 231 231 0:06:15 0:48:27 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1515-2 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:42:12 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1515-3 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 2,000 48 50 2,000 0:01:21 0:34:24 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1515-4 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 2,500 60 65 5,000 0:01:45 0:33:03 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1515-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 4,000 95 108 12,000 0:02:56 0:31:18 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1515-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 4,850 115 136 19,400 0:03:41 0:28:22 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1515-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 5,000 119 143 22,500 0:03:53 0:24:41 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1515-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 5,410 129 158 27,050 0:04:17 0:20:48 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1515-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 5,500 131 163 30,250 0:04:26 0:16:31 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1515-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 5,800 138 175 34,800 0:04:45 0:12:06 1.00 0.25 1.00 0.60 30.00 1.75 1.750.1515-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37 4,000 95 123 26,000 0:03:20 0:07:21 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1515-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37 3,000 71 94 21,000 0:02:33 0:04:00 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1515-13 30# Hybor G-i Spacer and Ball Drop 37 2,268 54 54 0:01:28 0:01:28 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1516-1 30# Hybor G-i Pad 37 3,160 75 75 0:02:02 0:34:22 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1516-2 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:32:20 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1516-3 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 1,400 33 35 1,400 0:00:57 0:24:31 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1516-4 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 1,750 42 45 3,500 0:01:14 0:23:35 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1516-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 2,800 67 76 8,400 0:02:03 0:22:21 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1516-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 3,400 81 95 13,600 0:02:35 0:20:18 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1516-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 3,500 83 100 15,750 0:02:43 0:17:43 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1516-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 3,850 92 112 19,250 0:03:03 0:15:00 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1516-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 3,800 90 113 20,900 0:03:04 0:11:57 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1516-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 4,050 96 122 24,300 0:03:19 0:08:54 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1516-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37 2,800 67 86 18,200 0:02:20 0:05:35 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1516-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37 2,100 50 66 14,700 0:01:47 0:03:15 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1516-13 30# Hybor G-i Spacer and Ball Drop 37 2,268 54 54 0:01:28 0:01:28 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1517-1 30# Hybor G-i Pad 37 3,160 75 75 0:02:02 0:41:47 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1517-2 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:39:45 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1517-3 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 1,400 33 35 1,400 0:00:57 0:31:56 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1517-4 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 1,750 42 45 3,500 0:01:14 0:31:00 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1517-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 2,800 67 76 8,400 0:02:03 0:29:46 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1517-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 3,400 81 95 13,600 0:02:35 0:27:43 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1517-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 3,500 83 100 15,750 0:02:43 0:25:08 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1517-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 3,850 92 112 19,250 0:03:03 0:22:25 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1517-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 3,800 90 113 20,900 0:03:04 0:19:22 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1517-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 4,050 96 122 24,300 0:03:19 0:16:19 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1517-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37 2,800 67 86 18,200 0:02:20 0:13:00 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1517-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37 2,100 50 66 14,700 0:01:47 0:10:40 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1517-13 30# Linear Flush 37 8,358 199 199 0:05:23 0:08:53 1.00 30.00 1.75 1.75 0.1517-14 Freeze Protect Freeze Protect 10 1,470 35 35 0:03:30 0:03:30 17-15 Shut-In Shut-InInterval 13Moraine@ 12531.21 - 12535.55 ft 139.4 °F"Frac Sleeve 12Interval 14Moraine@ 12009.52 - 12013.86 ft 139.5 °F"Frac Sleeve 13Interval 15Moraine@ 11487.28 - 11491.62 ft 139.7 °F"Frac Sleeve 14Interval 16Moraine@ 10966.12 - 10970.46 ft 139.9 °F"Frac Sleeve 15Interval 17Moraine@ 10447.39 - 10451.73 ft 140.1 °F"Frac Sleeve 16Conoco Phillips - 3S-602Planned Design163 CUSTOMERConoco Phillips FALSEAPI BFD (lb/gal)8.48LAT 70.39430569LEASE3S-602SALES ORDERBHST (°F)141LONG-150.1949722FORMATIONMoraineDATE 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)4/13/25Liquid Additives Dry Additives50-103-20906091000260818-1 Shut-In Shut-In0:58:06 18-2 Freeze Protect Prime Up Pressure Test 5 1,764 42 42 0:08:24 0:58:06 18-3 Shut-In Shut-In0:49:42 18-4 30# Linear Spacer and Ball Drop 15 1,260 30 30 0:02:00 0:49:42 1.00 30.00 1.75 1.75 0.1518-5 30# Hybor G-i Establish Stable Fluid 15 8,400 200 200 0:13:20 0:47:42 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1518-6 30# Hybor G-i Pad 37 3,160 75 75 0:02:02 0:34:22 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1518-7 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:32:20 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1518-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 1,400 33 35 1,400 0:00:57 0:24:31 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1518-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 1,750 42 45 3,500 0:01:14 0:23:35 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1518-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 2,800 67 76 8,400 0:02:03 0:22:21 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1518-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 3,400 81 95 13,600 0:02:35 0:20:18 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1518-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 3,500 83 100 15,750 0:02:43 0:17:43 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1518-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 3,850 92 112 19,250 0:03:03 0:15:00 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1518-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 3,800 90 113 20,900 0:03:04 0:11:57 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1518-15 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 4,050 96 122 24,300 0:03:19 0:08:54 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1518-16 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37 2,800 67 86 18,200 0:02:20 0:05:35 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1518-17 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37 2,100 50 66 14,700 0:01:47 0:03:15 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1518-18 30# Hybor G-i Spacer and Ball Drop 37 2,268 54 54 0:01:28 0:01:28 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1519-1 30# Hybor G-i Pad 37 3,160 75 75 0:02:02 0:34:22 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1519-2 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:32:20 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1519-3 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 1,400 33 35 1,400 0:00:57 0:24:31 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1519-4 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 1,750 42 45 3,500 0:01:14 0:23:35 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1519-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 2,800 67 76 8,400 0:02:03 0:22:21 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1519-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 3,400 81 95 13,600 0:02:35 0:20:18 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1519-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 3,500 83 100 15,750 0:02:43 0:17:43 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1519-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 3,850 92 112 19,250 0:03:03 0:15:00 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1519-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 3,800 90 113 20,900 0:03:04 0:11:57 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1519-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 4,050 96 122 24,300 0:03:19 0:08:54 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1519-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37 2,800 67 86 18,200 0:02:20 0:05:35 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1519-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37 2,100 50 66 14,700 0:01:47 0:03:15 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1519-13 30# Hybor G-i Spacer and Ball Drop 37 2,268 54 54 0:01:28 0:01:28 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1520-1 30# Hybor G-i Pad 37 3,160 75 75 0:02:02 0:34:22 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1520-2 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:32:20 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1520-3 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 1,400 33 35 1,400 0:00:57 0:24:31 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1520-4 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 1,750 42 45 3,500 0:01:14 0:23:35 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1520-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 2,800 67 76 8,400 0:02:03 0:22:21 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1520-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 3,400 81 95 13,600 0:02:35 0:20:18 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1520-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 3,500 83 100 15,750 0:02:43 0:17:43 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1520-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 3,850 92 112 19,250 0:03:03 0:15:00 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1520-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 3,800 90 113 20,900 0:03:04 0:11:57 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1520-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 4,050 96 122 24,300 0:03:19 0:08:54 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1520-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37 2,800 67 86 18,200 0:02:20 0:05:35 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1520-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37 2,100 50 66 14,700 0:01:47 0:03:15 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1520-13 30# Hybor G-i Spacer and Ball Drop 37 2,268 54 54 0:01:28 0:01:28 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1521-1 30# Hybor G-i Pad 37 3,160 75 75 0:02:02 0:34:22 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1521-2 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:32:20 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1521-3 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 1,400 33 35 1,400 0:00:57 0:24:31 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1521-4 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 1,750 42 45 3,500 0:01:14 0:23:35 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1521-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 2,800 67 76 8,400 0:02:03 0:22:21 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1521-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 3,400 81 95 13,600 0:02:35 0:20:18 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1521-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 3,500 83 100 15,750 0:02:43 0:17:43 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1521-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 3,850 92 112 19,250 0:03:03 0:15:00 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1521-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 3,800 90 113 20,900 0:03:04 0:11:57 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1521-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 4,050 96 122 24,300 0:03:19 0:08:54 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1521-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37 2,800 67 86 18,200 0:02:20 0:05:35 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1521-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37 2,100 50 66 14,700 0:01:47 0:03:15 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1521-13 30# Hybor G-i Spacer and Ball Drop 37 2,268 54 54 0:01:28 0:01:28 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1522-1 30# Hybor G-i Pad 37 3,160 75 75 0:02:02 0:34:22 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1522-2 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:32:20 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1522-3 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 1,400 33 35 1,400 0:00:57 0:24:31 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1522-4 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 1,750 42 45 3,500 0:01:14 0:23:35 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1522-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 2,800 67 76 8,400 0:02:03 0:22:21 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1522-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 3,400 81 95 13,600 0:02:35 0:20:18 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1522-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 3,500 83 100 15,750 0:02:43 0:17:43 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1522-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 3,850 92 112 19,250 0:03:03 0:15:00 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1522-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 3,800 90 113 20,900 0:03:04 0:11:57 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1522-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 4,050 96 122 24,300 0:03:19 0:08:54 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1522-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37 2,800 67 86 18,200 0:02:20 0:05:35 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1522-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37 2,100 50 66 14,700 0:01:47 0:03:15 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1522-13 30# Hybor G-i Spacer and Ball Drop 37 2,268 54 54 0:01:28 0:01:28 1.00 0.25 1.00 0.50 30.00 1.75 1.75 0.1523-1 30# Hybor G-i Pad 37 3,160 75 75 0:02:02 0:40:32 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1523-2 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:38:30 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1523-3 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 1,400 33 35 1,400 0:00:57 0:30:41 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1523-4 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 1,750 42 45 3,500 0:01:14 0:29:45 1.00 0.25 1.00 0.50 30.00 1.75 1.75 0.1523-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 2,800 67 76 8,400 0:02:03 0:28:31 1.00 0.25 1.00 0.50 30.00 1.75 1.75 0.1523-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 3,400 81 95 13,600 0:02:35 0:26:28 1.00 0.25 1.00 0.50 30.00 1.75 1.75 0.1523-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 3,500 83 100 15,750 0:02:43 0:23:53 1.00 0.25 1.00 0.50 30.00 1.75 1.75 0.1523-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 3,850 92 112 19,250 0:03:03 0:21:10 1.00 0.25 1.00 0.50 30.00 1.75 1.75 0.1523-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 3,800 90 113 20,900 0:03:04 0:18:07 1.00 0.25 1.00 0.50 30.00 1.75 1.75 0.1523-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 4,050 96 122 24,300 0:03:19 0:15:04 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1523-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37 2,800 67 86 18,200 0:02:20 0:11:45 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1523-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37 2,100 50 66 14,700 0:01:47 0:09:24 1.00 0.25 1.00 0.60 30.00 1.75 1.75 0.1523-13 30# Linear Flush 37 6,410 153 153 0:04:07 0:07:37 1.00 30.00 1.75 1.75 0.1523-14 Freeze Protect Freeze Protect 10 1,470 35 35 0:03:30 0:03:30 23-15 Shut-In Shut-In1,641,196 39,076 43,526 4,189,000Design Total (gal)Design Total (lbs)CL-28M BC-140X2 Losurf-300D MO-67 WG-36 OPTIFLO-III OPTIFLO-II BE-6-4,120,000(gal) (gal) (gal) (gal) (lbs) (lbs) (lbs) (lbs)78,34669,000Initial Design Material Volume 1,539.6384.9 1,617.9 921.6 48,538.3 2,831.4 2,831.4 242.7-14,852-1,539,598-CL-28M BC-140X2 Losurf-300D MO-67 WG-36 OPTIFLO-III OPTIFLO-II BE-6Fluid Type-30# LinearSeawaterFreeze Protect30# Hybor G-i-Proppant TypeWanli 16/20 Ceramic100M--Interval 21Moraine@ 8358.17 - 8362.51 ft 140.5 °F"Frac Sleeve 20Interval 22Moraine@ 7878.09 - 7882.43 ft 140.6 °F"Frac Sleeve 21Interval 23Moraine@ 7399.73 - 7404.07 ft 140 °FInterval 18Moraine@ 9925.58 - 9929.92 ft 140.2 °F"Frac Sleeve 17Interval 19Moraine@ 9402.53 - 9406.87 ft 140.4 °F"Frac Sleeve 18Interval 20Moraine@ 8879.86 - 8884.2 ft 140.5 °F"Frac Sleeve 1821:43:23 Conoco Phillips - 3S-602Planned Design164 Customer:Well:Date:Formation:SO#:Tank Type Water Source Inches Gallons Barrels Temperature (°F) Inches Gallons Barrels1 Atigan CPF3 103 19,368 461 100 11 1,627 392 Atigan CPF3 103 19,368 461 120 11 1,627 393 Atigan CPF3 101 18,981 452 105 11 1,627 394 Atigan CPF3 102 19,175 457 114 11 1,627 395 Atigan CPF3 104 19,562 466 107 11 1,627 396 Atigan CPF3 102 19,175 457 115 11 1,627 397 Wichita CPF3 102 20,580 490 103 11 2,100 508 Wichita CPF3 104 21,000 500 105 11 2,100 509 Atigan CPF3 103 19,368 461 108 11 1,627 3910 Wichita CPF3 101 20,370 485 103 101 20,370 48511 Atigan CPF3 101 18,981 452 105 11 1,627 3912 Atigan CPF3 103 19,368 461 110 12 1,809 4313 Wichita CPF3 105 21,000 500 113 12 2,268 5414 Wichita CPF3 102 20,580 490 111 12 2,268 5415 Wichita CPF3 100 20,160 480 108 11 2,100 5016 Atigan CPF3 104 19,562 466 115 40 6,920 16517 Atigan CPF3 101 18,981 452 107 101 18,981 45218 Wichita CPF3 103 20,790 495 112 103 20,790 49519 Atigan CPF3 101 18,981 452 116 101 18,981 45220 Atigan CPF3 103 19,368 461 44 7,673 18321 Atigan CPF3 103 19,368 461 11 1,627 3922 Tiger CPF3 101 16,561 394 11 1,390 3323 Tiger CPF3 101 16,561 394 11 1,390 3324 Tiger CPF3 101 16,561 394 11 1,390 33Flow Rate Stop FlowingGallons Barrels Gallons Barrels Gallons Barrels Gallons Barrels463,770 11,042 125,176 2,980 0 0 338,594 8,062Location SummaryStarting Volume Ending Volume On the Fly FlowingTotal UsedGeneral Beginning Strap Ending StrapOn the Fly Load SummaryDateStart flowing Flowing TempConoco Phillips 3S-6024/3/2025MoraineConoco Phillips - 3S-602Water Straps 4.13165 Customer:Well:Date:Formation:SO#:Tank Type Water Source Inches Gallons Barrels Temperature (°F) Inches Gallons Barrels1 Atigan CPF3 102 19,175 457 103 11 1,627 392 Atigan CPF3 102 19,175 457 110 11 1,627 393 Atigan CPF3 102 19,175 457 101 11 1,627 394 Atigan CPF3 102 19,175 457 105 11 1,627 395 Atigan CPF3 102 19,175 457 108 11 1,627 396 Atigan CPF3 108 20,336 484 104 11 1,627 397 Wichita CPF3 104 21,000 500 108 11 2,100 508 Wichita CPF3 104 21,000 500 102 11 2,100 509 Atigan CPF3 106 19,949 475 110 11 1,627 3910 Wichita CPF3 104 21,000 500 115 104 21,000 50011 Atigan CPF3 110 20,722 493 112 11 1,627 3912 Atigan CPF3 110 20,722 493 114 11 1,627 3913 Wichita CPF3 104 21,000 500 108 11 2,100 5014 Wichita CPF3 104 21,000 500 105 20 3,780 9015 Wichita CPF3 104 21,000 500 107 35 6,636 15816 Atigan CPF3 108 20,336 484 111 108 20,336 48417 Atigan CPF3 110 20,722 493 115 110 20,722 49318 Wichita CPF3 104 21,000 500 109 104 21,000 50019 Atigan CPF3 111 20,914 498 113 111 20,914 49820 Atigan CPF3 110 20,722 493 117 25 4,182 10021 Atigan CPF3 110 20,722 493 115 25 4,182 10022 Tiger CPF3 105 17,262 411 113 11 1,390 3323 Tiger CPF3 101 16,561 394 110 11 1,390 3324 Tiger CPF3 101 16,561 394 113 11 1,390 33Flow Rate Stop FlowingGallons Barrels Gallons Barrels Gallons Barrels Gallons Barrels478,402 11,391 147,866 3,521 0 0 330,536 7,870Location SummaryStarting Volume Ending Volume On the Fly FlowingTotal UsedGeneral Beginning Strap Ending StrapOn the Fly Load SummaryDateStart flowing Flowing TempConoco Phillips 3S-6024/14/2025MoraineConoco Phillips - 3S-602Water Straps 4.14166 Customer:Well:Date:Formation:SO#:Tank Type Water Source Inches Gallons Barrels Temperature (°F) Inches Gallons Barrels1 Atigan CPF3 102 19,175 457 103 9 1,262 302 Atigan CPF3 103 19,368 461 101 12 1,809 433 Atigan CPF3 102 19,175 457 101 9 1,262 304 Atigan CPF3 100 18,788 447 105 10 1,444 345 Atigan CPF3 103 19,368 461 108 10 1,444 346 Atigan CPF3 100 18,788 447 104 10 1,444 347 Wichita CPF3 100 20,160 480 108 10 1,890 458 Wichita CPF3 100 20,160 480 102 10 1,890 459 Atigan CPF3 103 19,368 461 102 10 1,444 3410 Wichita CPF3 100 20,160 480 105 100 20,160 48011 Atigan CPF3 101 18,981 452 100 10 1,444 3412 Atigan CPF3 101 18,981 452 104 10 1,444 3413 Wichita CPF3 101 20,370 485 108 9 1,722 4114 Wichita CPF3 101 20,370 485 105 10 1,890 4515 Wichita CPF3 102 20,580 490 107 20 3,780 9016 Atigan CPF3 108 20,336 484 104 45 7,873 18717 Atigan CPF3 110 20,722 493 105 110 20,722 49318 Wichita CPF3 104 21,000 500 109 30 5,670 13519 Atigan CPF3 111 20,914 498 102 30 5,095 12120 Atigan CPF3 104 19,562 466 100 30 5,095 12121 Atigan CPF3 104 19,562 466 103 10 1,444 3422 Tiger CPF3 101 16,561 394 101 10 1,235 2923 Tiger CPF3 100 16,388 390 100 10 1,235 2924 Tiger CPF3 105 17,262 411 105 10 1,235 29Flow Rate Stop FlowingGallons Barrels Gallons Barrels Gallons Barrels Gallons Barrels466,099 11,098 93,936 2,237 0 0 372,163 8,861Location SummaryStarting Volume Ending Volume On the Fly FlowingTotal UsedGeneral Beginning Strap Ending StrapOn the Fly Load SummaryDateStart flowing Flowing TempConoco Phillips 3S-6024/14/2025MoraineConoco Phillips - 3S-602Water Straps 4.15167 Customer:Well:Date:Formation:SO#:Tank Type Water Source Inches Gallons Barrels Temperature (°F) Inches Gallons Barrels1 Atigan CPF3 97 18,208 434 105 15 2,357 562 Atigan CPF3 95 17,821 424 105 15 2,357 563 Atigan CPF3 95 17,821 424 106 10 1,444 344 Atigan CPF3 95 17,821 424 105 10 1,444 345 Atigan CPF3 95 17,821 424 108 10 1,444 346 Atigan CPF3 95 17,821 424 106 10 1,444 347 Wichita CPF3 95 19,110 455 108 10 1,890 458 Wichita CPF3 95 19,110 455 105 10 1,890 459 Atigan CPF3 100 18,788 447 110 10 1,444 3410 Wichita CPF3 97 19,530 465 107 97 19,530 46511 Atigan CPF3 98 18,401 438 106 10 1,444 3412 Atigan CPF3 100 18,788 447 107 10 1,444 3413 Wichita CPF3 102 20,580 490 108 10 1,890 4514 Wichita CPF3 101 20,370 485 105 50 9,660 23015 Wichita CPF3 100 20,160 480 107 74 14,700 35016 Atigan CPF3 100 18,788 447 108 100 18,788 44717 Atigan CPF3 101 18,981 452 105 101 18,981 45218 Wichita CPF3 105 21,000 500 109 101 20,370 48519 Atigan CPF3 101 18,981 452 107 55 9,951 23720 Atigan CPF3 102 19,175 457 105 55 9,951 23721 Atigan CPF3 105 19,755 470 106 10 1,444 3422 Tiger CPF3 101 16,561 394 109 10 1,235 2923 Tiger CPF3 101 16,561 394 105 10 1,235 2924 Tiger CPF3 101 16,561 394 108 10 1,235 29Flow Rate Stop FlowingGallons Barrels Gallons Barrels Gallons Barrels Gallons Barrels448,510 10,679 147,575 3,514 0 0 300,935 7,165Location SummaryStarting Volume Ending Volume On the Fly FlowingTotal UsedGeneral Beginning Strap Ending StrapOn the Fly Load SummaryDateStart flowing Flowing TempConoco Phillips 3S-6024/14/2025MoraineConoco Phillips - 3S-602Water Straps 4.20168 Customer:Well:Date:Formation:SO#:Tank Type Water Source Inches Gallons Barrels Temperature (°F) Inches Gallons Barrels1 Atigan CPF3 104 19,562 466 98 10 1,444 342 Atigan CPF3 104 19,562 466 100 10 1,444 343 Atigan CPF3 104 19,562 466 101 10 1,444 344 Atigan CPF3 104 19,562 466 101 10 1,444 345 Atigan CPF3 104 19,562 466 100 10 1,444 346 Atigan CPF3 104 19,562 466 103 10 1,444 347 Wichita CPF3 102 20,580 490 101 10 1,890 458 Wichita CPF3 102 20,580 490 103 10 1,890 459 Atigan CPF3 104 19,562 466 100 10 1,444 3410 Wichita CPF3 102 20,580 490 104 100 20,160 48011 Atigan CPF3 104 19,562 466 100 10 1,444 3412 Atigan CPF3 104 19,562 466 101 10 1,444 3413 Wichita CPF3 102 20,580 490 103 10 1,890 4514 Wichita CPF3 102 20,580 490 101 45 8,610 20515 Wichita CPF3 102 20,580 490 104 104 21,000 50016 Atigan CPF3 104 19,562 466 101 104 19,562 46617 Atigan CPF3 110 20,722 493 102 110 20,722 49318 Wichita CPF3 100 20,160 480 100 100 20,160 48019 Atigan CPF3 104 19,562 466 101 104 19,562 46620 Atigan CPF3 104 19,562 466 103 55 9,951 23721 Atigan CPF3 104 19,562 466 100 55 9,951 23722 Tiger CPF3 105 17,262 411 101 10 1,235 2923 Tiger CPF3 105 17,262 411 100 10 1,235 2924 Tiger CPF3 105 17,262 411 103 10 1,235 29Flow Rate Stop FlowingGallons Barrels Gallons Barrels Gallons Barrels Gallons Barrels470,448 11,201 172,051 4,096 0 0 298,397 7,105Location SummaryStarting Volume Ending Volume On the Fly FlowingTotal UsedGeneral Beginning Strap Ending StrapOn the Fly Load SummaryDateStart flowing Flowing TempConoco Phillips 3S-6024/14/2025MoraineConoco Phillips - 3S-602Water Straps 4.21169 SpecificGravityTestingTemperatureDissolved Iron(Fe2+)Chloride(Cl-)Sulfate(SO42-)Calcium(Ca2+)Magnesium(Mg2+)TotalHardnessLinearViscosityWaterpHGelpHPost-CrosslinkpHCrosslink Bacteria- °F mg/L mg/L mg/L mg/L mg/L mg/L cP - - - (Y/N) BQ ValueTank #H2S present? Y/NHydrometer Digital Thermometer Strip Strip Strip TitrationTotal Hardness Minus CalciumTitration FANN-35 Probe Probe Probe - Mycometer1 N 1.026 112.6 0 26,840 1,600 2,920 1,080 4,000 27.0 6.90 7.47 8.94 Y 3,3202 N 1.025 108.6 0 21,060 1,600 2,600 1,640 4,240 26.0 6.91 7.23 8.76 Y 2,5463 N 1.025 109.6 0 19,470 1,600 2,160 2,480 4,640 26.0 7.12 7.42 8.71 Y 2,1874 N 1.025 102.0 0 21,120 1,600 1,720 520 2,240 27.0 6.87 7.21 8.78 Y 2,7205 N 1.025 112.6 0 21,120 1,600 2,240 400 2,640 27.0 7.10 7.35 8.81 Y 1,8786 N 1.025 97.3 0 19,410 1,600 1,720 520 2,240 27.0 6.93 7.45 8.54 Y 5,7857 N 1.026 108.1 0 23,030 1,600 2,080 960 3,040 27.0 6.88 7.08 8.64 Y 3,6128 N 1.025 96.2 0 27,570 1,600 1,640 1,000 2,640 26.0 6.92 7.12 8.74 Y 2,5059 N 1.025 104.5 0 23,030 1,600 1,840 1,200 3,040 24.0 7.05 7.27 8.75 Y 6,25910 N 1.024 98.4 0 19,410 1,600 1,640 1,000 2,640 25.0 6.94 7.46 8.98 Y 38,86811 N 1.025 88.6 0 19,410 1,600 1,680 2,320 4,000 25.0 7.20 7.35 8.81 Y 7,69812 N 1.025 91.7 0 27,570 1,600 1,920 320 2,240 28.0 7.18 7.25 8.65 Y 6,39113 N 1.024 98.7 0 25,170 1,600 1,920 720 2,640 26.0 6.98 7.21 8.57 Y 8,61214 N 1.030 106.7 0 20,830 1,200 2,560 1,240 3,800 27.0 6.91 7.31 8.65 Y 6,78515 N 1.029 112.2 0 24,710 1,200 2,480 1,520 4,000 25.0 7.22 7.27 8.68 Y 8,98616 N 1.030 1114.0 0 21,060 1,200 2,600 1,400 4,000 25.0 7.00 7.19 8.76 Y 9,80717 N 1.028 117.1 0 19,470 1,200 2,520 1,480 4,000 25.0 7.21 7.35 8.70 Y 7,23318 N 1.029 112.0 0 18,010 1,200 2,000 2,000 4,000 26.0 7.12 7.32 8.78 Y 6,68219 N 1.028 122.0 0 22,800 1,200 2,240 1,760 4,000 26.0 7.15 7.48 8.65 Y 1,19420 N 1.028 123.0 0 18,030 1,200 1,840 1,880 3,720 25.0 7.00 7.12 8.69 Y 4,16321 N 1.030 86.1 0 21,060 1,200 2,520 920 3,440 28.0 7.12 7.23 8.76 Y 4,53222 N 1.028 88.8 0 21,060 1,200 2,120 1,880 4,000 27.0 6.87 7.17 8.75 Y 4,68923 N 1.028 99.2 0 24,710 1,200 1,840 1,960 3,800 26.0 6.98 7.15 8.74 Y 7,25324 N 1.028 102.3 0 22,800 1,200 2,000 1,920 3,920 26.0 7.08 7.20 8.90 Y 8,230Average 1.027 0 22,031 1417 2,117 1338 3,455 26.1 7.03 7.28 8.74 - 6,747Maximum 1.030 0 27,570 1,600 2,920 2,480 4,640 28.0 7.22 7.48 8.98 - 38,868Minimum 1.024 0 18,010 1,200 1,840 920 3,440 25.00 6.87 7.12 8.65 - 1,194Range 0.006 0 9,560 400 1,080 1,560 1,200 3.0 0.35 0.36 0.33 - 37,673Well Name:3S-602Water Source:CPF3Alaska District Field QCPrejob Water Analysis on LocationCompany:Conoco Phillips Conoco Phillips - 3S-602Water Analysis 4.12170 SpecificGravityTestingTemperatureDissolved Iron(Fe2+)Chloride(Cl-)Sulfate(SO42-)Calcium(Ca2+)Magnesium(Mg2+)TotalHardnessLinearViscosityWaterpHGelpHPost-CrosslinkpHCrosslink Bacteria- °F mg/L mg/L mg/L mg/L mg/L mg/L cP - - - (Y/N) BQ ValueTank #H2S present? Y/NHydrometer Digital Thermometer Strip Strip Strip TitrationTotal Hardness Minus CalciumTitration FANN-35 Probe Probe Probe - Mycometer1 N 1.026 104.0 0 21,120 1,600 3,120 880 4,0002 N 1.026 104.0 0 23,030 1,600 2,160 2,680 4,8403 N 1.026 104.0 0 23,030 1,600 2,160 1,560 3,7204 N 1.025 104.0 0 23,030 1,600 2,400 2,160 4,5605 N 1.025 104.0 0 25,170 1,600 2,360 1,880 4,2406 N 1.025 103.0 0 15,160 1,600 2,320 1,680 4,0007 N 1.025 103.0 0 21,120 1,600 2,560 1,920 4,4808 N 1.025 103.0 0 19,410 1,600 2,800 1,200 4,0009 N 1.025 103.0 0 21,120 1,600 2,120 1,280 3,40011 N 1.025 103.0 0 23,030 1,600 3,600 400 4,00012 N 1.024 105.0 0 25,170 1,600 2,880 480 3,36013 N 1.024 105.0 0 41,100 1,600 3,280 80 3,36014 N 1.024 105.0 0 25,170 1,600 3,320 400 3,72015 N 1.024 105.0 0 20,830 1,600 3,600 0 3,60016 N 1.025 105.0 0 24,710 1,600 3,200 320 3,52017 N 1.024 102.0 0 21,060 1,600 3,200 320 3,52018 N 1.025 102.0 0 19,470 1,600 3,200 160 3,36019 N 1.025 102.0 0 21,060 1,600 3,440 200 3,64020 N 1.025 102.0 0 19,470 1,600 3,280 80 3,360Average 1.025 0 22,803 1600 2,895 931 3,825 26.0 7.09 7.53 9.06 - 20,848Maximum 1.026 0 41,100 1,600 3,600 2,680 4,840 27.0 7.13 7.61 9.09 - 34,335Minimum 1.024 0 15,160 1,600 2,120 0 3,360 25.00 7.06 7.42 9.02 - 9,728Range 0.002 0 25,940 0 1,480 2,680 1,480 2.0 0.07 0.19 0.07 - 24,60797281764030003133783433520002Y26.0 7.13 7.57 9.02 Y26.0 7.11 7.61 9.05Y25.0 7.06 7.42 9.08 Y27.0 7.04 7.53 9.09Well Name:3S-602Water Source:CPF3Alaska District Field QCPrejob Water Analysis on LocationCompany:Conoco Phillips Conoco Phillips - 3S-602Water Analysis 4.14171 SpecificGravityTestingTemperatureDissolved Iron(Fe2+)Chloride(Cl-)Sulfate(SO42-)Calcium(Ca2+)Magnesium(Mg2+)TotalHardnessLinearViscosityWaterpHGelpHPost-CrosslinkpHCrosslink Bacteria- °F mg/L mg/L mg/L mg/L mg/L mg/L cP - - - (Y/N) BQ ValueTank #H2S present? Y/NHydrometer Digital Thermometer Strip Strip Strip TitrationTotal Hardness Minus CalciumTitration FANN-35 Probe Probe Probe - Mycometer1 N 1.025 111.0 0 19,410 1,600 1,120 1,880 3,0002 N 1.025 111.0 0 23,030 1,600 1,440 2,200 3,6403 N 1.026 111.0 0 21,120 1,600 1,480 1,840 3,3204 N 1.024 111.0 0 23,030 1,600 1,400 1,480 2,8805 N 1.030 111.0 0 19,410 1,600 1,040 2,000 3,0406 N 1.029 103.0 0 21,120 1,600 1,320 2,080 3,4007 N 1.030 103.0 0 21,120 1,600 560 2,600 3,1608 N 1.028 103.0 0 23,030 1,600 1,040 1,880 2,9209 N 1.029 103.0 0 19,410 1,600 1,360 1,800 3,16011 N 1.028 103.0 0 16,440 1,600 1,160 1,960 3,12012 N 1.028 85.0 0 22,500 1,600 1,280 1,840 3,12013 N 1.030 85.0 0 29,080 1,600 1,200 1,800 3,00014 N 1.028 85.0 0 24,460 1,600 1,200 1,720 2,92015 N 1.029 85.0 0 22,500 1,600 1,120 1,240 2,36020 N 1.028 85.0 0 22,500 1,600 1,240 1,800 3,04021 N 1.028 84.0 0 26,640 1,600 1,080 1,160 2,24022 N 1.030 84.0 0 13,940 1,600 1,120 2,240 3,36023 N 1.030 84.0 0 24,460 1,600 1,120 1,800 2,92024 N 1.030 84.0 0 22,500 1,600 1,080 2,360 3,440Average 1.028 0 21,879 1600 1,177 1878 3,055 25.5 7.06 7.28 8.94 - 11,334Maximum 1.030 0 29,080 1,600 1,480 2,600 3,640 27.0 7.10 7.33 8.97 - 24,812Minimum 1.024 0 13,940 1,600 560 1,160 2,240 25.00 7.00 7.25 8.90 - 2,801Range 0.006 0 15,140 0 920 1,440 1,400 2.0 0.10 0.08 0.07 - 22,01124,81225.0 7.00 7.25 8.94 Y 8,75727.0 7.09 7.32 8.90 Y2,80125.0 7.10 7.23 8.96 Y 8,96425.0 7.05 7.33 8.97 YWell Name:3S-602Water Source:CPF3Alaska District Field QCPrejob Water Analysis on LocationCompany:Conoco Phillips Conoco Phillips - 3S-602Water Analysis 4.15172 SpecificGravityTestingTemperatureDissolved Iron(Fe2+)Chloride(Cl-)Sulfate(SO42-)Calcium(Ca2+)Magnesium(Mg2+)TotalHardnessLinearViscosityWaterpHGelpHPost-CrosslinkpHCrosslink Bacteria- °F mg/L mg/L mg/L mg/L mg/L mg/L cP - - - (Y/N) BQ ValueTank #H2S present? Y/NHydrometer Digital Thermometer Strip Strip Strip TitrationTotal Hardness Minus CalciumTitration FANN-35 Probe Probe Probe - Mycometer1 N 1.025 110.0 0 19,410 1,600 1,040 1,880 2,9202 N 1.025 110.0 0 16,440 1,600 1,400 960 2,3603 N 1.025 110.0 0 22,500 1,200 1,040 2,000 3,0404 N 1.025 110.0 0 29,080 1,200 1,320 920 2,2405 N 1.025 110.0 0 24,460 1,200 1,040 2,000 3,0406 N 1.025 115.0 0 22,500 1,200 1,040 1,600 2,6407 N 1.024 115.0 0 19,410 1,600 1,360 1,680 3,0408 N 1.024 115.0 0 16,440 1,600 1,360 1,280 2,6409 N 1.025 115.0 0 22,500 1,200 1,600 1,400 3,00011 N 1.025 115.0 0 29,080 1,200 1,560 680 2,24012 N 1.025 125.0 0 19,410 1,200 1,560 1,080 2,64013 N 1.025 125.0 0 16,440 1,200 1,400 1,520 2,92014 N 1.025 125.0 0 22,500 1,200 1,960 1,640 3,60015 N 1.025 125.0 0 29,080 1,200 1,320 920 2,24020 N 1.024 125.0 0 24,460 1,200 1,960 680 2,64021 N 1.024 85.0 0 22,500 1,200 1,480 1,880 3,36022 N 1.024 85.0 0 22,500 1,200 1,360 1,560 2,92023 N 1.024 85.0 0 26,640 1,200 1,480 1,440 2,92024 N 1.025 85.0 0 26,640 1,200 1,960 280 2,240Average 1.025 0 22,736 1284 1,434 1337 2,771 26.3 7.12 7.22 8.81 - 4,012Maximum 1.025 0 29,080 1,600 1,960 2,000 3,600 27.0 7.15 7.24 8.88 - 5,094Minimum 1.024 0 16,440 1,200 1,040 280 2,240 25.00 7.09 7.19 8.69 - 3,155Range 0.001 0 12,640 400 920 1,720 1,360 2.0 0.06 0.05 0.19 - 1,9395,09426.0 7.12 7.23 8.78 Y 3,47427.0 7.09 7.19 8.69 Y3,15527.0 7.10 7.24 8.88 Y 4,32525.0 7.15 7.20 8.88 YWell Name:3S-602Water Source:CPF3Alaska District Field QCPrejob Water Analysis on LocationCompany:Conoco Phillips Conoco Phillips - 3S-602Water Analysis 4.20173 SpecificGravityTestingTemperatureDissolved Iron(Fe2+)Chloride(Cl-)Sulfate(SO42-)Calcium(Ca2+)Magnesium(Mg2+)TotalHardnessLinearViscosityWaterpHGelpHPost-CrosslinkpHCrosslink Bacteria- °F mg/L mg/L mg/L mg/L mg/L mg/L cP - - - (Y/N) BQ ValueTank #H2S present? Y/NHydrometer Digital Thermometer Strip Strip Strip TitrationTotal Hardness Minus CalciumTitration FANN-35 Probe Probe Probe - Mycometer1 N 1.025 110.0 0 21,120 1,400 1,240 2,640 63,4822 N 1.025 110.0 0 21,120 1,400 1,400 2,800 73,8023 N 1.025 110.0 0 21,120 1,600 1,040 2,640 53,4814 N 1.025 110.0 0 16,440 1,800 840 2,640 72,8275 N 1.025 110.0 0 16,440 1,400 1,640 3,040 70,8736 N 1.026 108.0 0 21,120 1,600 1,040 2,640 42,7527 N 1.025 108.0 0 21,120 1,840 1,360 3,200 65,0878 N 1.025 108.0 0 21,120 1,400 840 2,240 74,7199 N 1.026 108.0 0 16,440 1,400 1,240 2,640 75,91612 N 1.026 108.0 0 16,440 1,560 1,480 3,040 79,09113 N 1.026 109.0 0 21,120 1,400 1,240 2,640 72,75820 N 1.024 109.0 0 21,120 1,560 1,640 3,200 73,23721 N 1.024 109.0 0 21,120 1,560 1,040 2,600 76,89222 N 1.024 109.0 0 21,120 1,400 1,240 2,640 96,32423 N 1.024 109.0 0 16,440 1,960 960 2,920 73,06624 N 1.026 109.0 0 21,120 1,400 1,520 2,920 52,392Average 1.025 0 19,658 - 1,543 1235 2,778 26.3 7.07 7.25 9.05 - 69,794Maximum 1.026 0 21,120 0 1,960 1,640 3,200 27.0 7.16 7.29 9.10 - 96,324Minimum 1.024 0 16,440 0 1,400 840 2,240 26.00 7.08 7.23 9.08 - 42,752Range 0.002 0 4,680 0 560 800 960 1.0 0.08 0.06 0.02 - 53,57226.0 7.08 7.23 9.08 Y27.0 6.96 7.23 8.96 Y26.0 7.16 7.29 9.10 YWell Name:3S-602Water Source:CPF3Alaska District Field QCPrejob Water Analysis on LocationCompany:Conoco Phillips Conoco Phillips - 3S-602Water Analysis 4.21174 Linear Linear XL XL XL Lip time Linear Linear XL XL XL Lip time 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 95 9.02 0 11 Pad 21 Pad247.11 82 8.8 0 .25# 25 6.95 95 8.82 0 25 Avg Linear Visc .25# 25 7.02 97 8.76 0 25 Avg Linear Visc .25# 24 7.13 86 9.1 0 24 Avg Linear Visc 1.00# 24 7.06 109 8.93 0 95.0 Avg XLTemp 1.00# 89.5 Avg XLTemp 1.00# 86.0 Avg XLTemp 2.00# 25 7.03 81 8.95 0 8.9 Avg XL pH 2.00# 8.87 Avg XL pH 2.00# 24 7.22 87 8.89 0 8.9 Avg XL pH 3.00# 25 7.1 93 8.8 0 3.00#3.00# 4.00# 25 6.96 97 8.91 0 4.00#4.00# 24 7.15 86 8.91 0 4.50# 25 7 95 8.8 0 4.50#4.50# 5.00# 25 7.02 95 8.86 0 5.00# 25 6.9 82 8.97 0 5.00# 25 7.15 89 8.83 0 5.50#5.50#5.50# 6.00#6.00# 26 6.98 79 8.9 0 6.00# 27 7.12 89 8.9 0 6.50#6.50#6.50# 7.00#7.00# 26 84 8.93 0 7.00# 2 Pad 22 6.98 107 9.18 0 12 Pad 22 Pad277.12 90 8.85 0 .25# 24 6.99 106 8.94 0 .25#.25# 27 7.12 97 8.85 0 1.00# 24 6.97 101 8.83 0 1.00#1.00# 2.00# 26 7.07 100 8.86 0 24 Avg Linear Visc 2.00# 25 6.99 91 8.88 0 25 Avg Linear Visc 2.00# 26 7.14 94 8.83 0 26 Avg Linear Visc 3.00# 25 6.97 101 8.88 0 102.5 Avg XLTemp 3.00# 84.3 Avg XLTemp 3.00# 92.5 Avg XLTemp 4.00# 25 7.11 100 8.94 0 8.9 Avg XL pH 4.00# 8.88 Avg XL pH 4.00# 25 7.14 94 8.88 0 8.9 Avg XL pH 4.50#4.50#4.50# 5.00#5.00# 26 6.94 76 8.89 0 5.00# 25 7.1 95 8.85 0 5.50#5.50#5.50# 6.00#6.00# 26 7.02 84 8.93 0 6.00# 23 7.11 85 8.99 0 6.50#6.50# 24 7.01 86 8.82 0 6.50# 7.00#7.00#7.00# 3 Pad 21 7.28 93 8.85 0 13 Pad246.9492 8.8 0 23 Pad257.12 99 8.94 0 .25# 26 7.12 94 8.89 0 .25# 25 6.96 102 8.8 0 .25# 25 7.1 91 8.85 0 1.00#1.00#1.00# 2.00# 25 7.09 93 8.91 0 26 Avg Linear Visc 2.00# 24 6.94 93 8.89 0 25 Avg Linear Visc 2.00# 25 7.1 91 8.85 0 25 Avg Linear Visc 3.00# 89.3 Avg XLTemp 3.00# 92.6 Avg XLTemp 3.00# 91.3 Avg XLTemp 4.00# 26 7.05 86 8.85 0 8.9 Avg XL pH 4.00# 25 6.97 92 8.92 0 8.88 Avg XL pH 4.00# 25 7 89 8.8 0 8.8 Avg XL pH 4.50#4.50#4.50# 5.00# 29 7.09 84 8.83 0 5.00# 25 7.01 91 8.92 0 5.00# 25 7.12 89 8.81 0 5.50#5.50#5.50# 6.00# 29 7.01 86 8.82 6.00# 25 7.03 88 8.85 0 6.00# 23 7.11 90 8.81 0 6.50#6.5#6.50# 25 7.19 90 8.7 0 7.00#7.00# 26 7.01 90 9.01 0 7.00# 4 Pad 25 7.12 76 9.45 0 14 Pad 24 Pad .25# 27 6.98 81 8.95 0 .25# 24 6.96 91 8.98 0 .25# 1.00#1.00#1.00# 2.00# 28 6.97 82 8.87 0 26.86 Avg Linear Visc 2.00# 26 7.01 89 8.86 0 25 Avg Linear Visc 2.00# #DIV/0! Avg Linear Visc 3.00# 81.14 Avg XLTemp 3.00# 86.0 Avg XLTemp 3.00# #DIV/0! Avg XLTemp 4.00# 27 6.97 82 8.94 0 9.00 Avg XL pH 4.00# 24 6.98 88 8.92 0 8.93 Avg XL pH 4.00# #DIV/0! Avg XL pH 4.50#4.50#4.50# 5.00# 27 6.97 82 8.91 0 5.00# 25 7.01 85 8.94 0 5.00# 5.50#5.50#5.50# 6.00# 27 6.94 84 8.96 0 6.00# 26 7.01 82 8.92 0 6.00# 6.50# 27 6.91 81 8.93 0 6.50#6.50# 7.00#7.00# 26 6.99 81 8.95 0 7.00# 5 Pad 26 6.89 88 8.98 0 15 Pad 25 Pad .25# 22 6.88 87 8.97 0 .25# 24 7.01 97 8.87 0 .25# 1.00#1.00#1.00# 2.00# 26 6.91 91 8.96 0 26.43 Avg Linear Visc 2.00# 24 6.98 97 8.86 0 24 Avg Linear Visc 2.00# #DIV/0! Avg Linear Visc 3.00#84.43 Avg XLTemp 3.00# 95.8 Avg XLTemp 3.00# #DIV/0! Avg XLTemp 4.00# 8.96 Avg XL pH 4.00# 24 6.95 99 8.88 0 8.88 Avg XL pH 4.00# #DIV/0! Avg XL pH 4.50# 26 6.96 90 9 0 4.50#4.50# 5.00# 26 6.93 86 8.94 0 5.00# 24 6.98 96 8.85 0 5.00# 5.50#5.50#5.50# 6.00# 30 6.99 74 8.91 0 6.00# 24 7.02 93 8.91 0 6.00# 6.50#6.50#6.50# 7.00# 29 7.01 75 8.94 0 7.00# 24 93 8.92 0 7.00# 6 Pad 16 Pad 26 Pad .25# 24 7 93 9.23 0 .25# 23 7.01 100 8.8 0 .25# 1.00#1.00#1.00# 2.00# 27 7.04 88 9.03 0 25.50 Avg Linear Visc 2.00# 23 Avg Linear Visc 2.00# #DIV/0! Avg Linear Visc 3.00# 85.50 Avg XLTemp 3.00# 94.0 Avg XLTemp 3.00# #DIV/0! Avg XLTemp 4.00# 26 7.02 85 9.01 0 9.02 Avg XL pH 4.00# 23 7 95 8.86 0 8.86 Avg XL pH 4.00# #DIV/0! Avg XL pH 4.50#4.50#4.50# 5.00# 26 7.15 81 8.95 0 5.00#5.00# 5.50#5.50#5.50# 6.00# 26 7.1 87 8.97 0 6.00#6.00# 6.50#6.50#6.50# 7.00# 24 7.04 79 8.94 0 7.00# 24 6.98 87 8.93 0 7.00# 7 Pad 24 7.1 88 9.26 0 17 Pad 27 Pad .25# 25 7.08 85 8.95 0 .25# 20 7.01 103 8.8 0 .25# 1.00#1.00#1.00# 2.00# 27 Avg Linear Visc 2.00# 24 6.99 102 8.85 0 25 Avg Linear Visc 2.00# #DIV/0! Avg Linear Visc 3.00# 80.0 Avg XLTemp 3.00# 96.8 Avg XLTemp 3.00# #DIV/0! Avg XLTemp 4.00# 28 7.11 83 8.96 0 9.0 Avg XL pH 4.00# 28 7.03 93 8.88 0 8.85 Avg XL pH 4.00# #DIV/0! Avg XL pH 4.50#4.50#4.50# 5.00# 28 7 76 8.86 0 5.00#5.00# 5.50#5.50#5.50# 6.00# 28 6.98 74 8.85 0 6.00# 26 7.04 89 8.87 0 6.00# 6.50#6.50#6.50# 7.00# 26 7.14 74 8.86 0 7.00#7.00# 8 Pad 23 7.07 90 8.91 0 18 Pad257.2384 9 0 28 Pad .25# 26 6.96 90 8.73 0 .25# 25 7.2 84 9.02 .25# 1.00#1.00#1.00# 2.00# 25 6.9 99 8.79 0 25.17 Avg Linear Visc 2.00# 26 Avg Linear Visc 2.00# #DIV/0! Avg Linear Visc 3.00# 91.17 Avg XLTemp 3.00# 27 7.23 83 8.72 0 82.5 Avg XLTemp 3.00# #DIV/0! Avg XLTemp 4.00# 25 6.98 89 8.79 0 8.81 Avg XL pH 4.00# 27 7.12 83 8.9 0 8.9 Avg XL pH 4.00# #DIV/0! Avg XL pH 4.50#4.50#4.50# 5.00# 26 6.99 92 8.77 0 5.00# 24 7.13 84 8.8 0 5.00# 5.50#5.50#5.50# 6.00# 26 6.9 87 8.85 0 6.00# 27 7.23 77 8.87 0 6.00# 6.50#6.50#6.50# 7.00# 25 6.91 84 8.85 0 7.00#7.00# 9 Pad 26 6.89 95 8.67 0 19 Pad257.15878.92 0 29 Pad .25# 26 6..9 97 8.82 0 .25# 22 7.2 86 9.04 0 .25# 1.00#1.00#1.00# 2.00# 25 Avg Linear Visc 2.00# 24 Avg Linear Visc 2.00# #DIV/0! Avg Linear Visc 3.00# 94.4 Avg XLTemp 3.00# 78.4 Avg XLTemp 3.00# #DIV/0! Avg XLTemp 4.00# 24 6.97 93 8.79 0 8.78 Avg XL pH 4.00# 25 7.09 72 8.85 0 8.9 Avg XL pH 4.00# #DIV/0! Avg XL pH 4.50#4.50#4.50# 5.00# 24 6.82 96 8.73 0 5.00# 25 7.11 77 8.89 0 5.00# 5.50#5.50#5.50# 6.00# 26 7.04 91 8.87 0 6.00# 24 7.12 70 8.9 0 6.00# 6.50#6.50#6.50# 7.00# 24 6.99 84 8.91 0 7.00#7.00# 10 Pad 20 Pad 30 Pad .25# 24 7.04 94 8.86 0 .25# 25 7.23 87 8.9 0 .25# 1.00#1.00#1.00# 2.00# 25 Avg Linear Visc 2.00# 25 7.1 84 8.85 0 25 Avg Linear Visc 2.00# #DIV/0! Avg Linear Visc 3.00# 89.3 Avg XLTemp 3.00# 86.4 Avg XLTemp 3.00# #DIV/0! Avg XLTemp 4.00# 25 7.01 93 8.86 0 8.91 Avg XL pH 4.00# 25 7.1 85 8.82 0 8.9 Avg XL pH 4.00# #DIV/0! Avg XL pH 4.50#4.50#4.50# 5.00# 25 6.92 86 8.95 0 5.00# 25 7.12 87 8.87 0 5.00# 5.50#5.50#5.50# 6.00# 26 7.02 84 8.96 0 6.00# 24 7.3 89 8.9 0 6.00# 6.50#6.50#6.50# 7.00# 24 87 8.87 0 7.00#7.00# Comments Comments Comments Comments Comments Comments Comments Comments Comments Comments Comments Comments Comments Comments Comments Comments Comments Comments Comments Comments Comments Comments Comments Comments Comments Comments Comments Comments Comments Comments Customer:CONOCO PHILLIPS Wellname & #:3S-602 Date:April 13, 2025 Conoco Phillips - 3S-602 Real-Time QC 175 Seq No. Time Activity Code Comment Job Slurry Vol Treating Pressure Treating Pressure @Pump Slurry Rate Tubing Gauge BH Pres 1 05:58:46 (04/13/25) Start Job Starting Job 0 0 0 0 0 1 05:58:46 (04/13/25) Next Treatment Treatment Interval 1 0 0 0 0 0 2 8:01:47 Other Loop Test 2.53 20 0 0 1913 3 8:10:57 Prime Pumps Prime Pumps 0 93 77 0 1913 4 8:28:23 Pressure Test ePRV - Primary Tubing 0 858 266 0 1913 5 8:29:36 Pressure Test ePRV - Primary IA 0 947 302 0 1913 6 8:32:18 Pressure Test ePRV - Secondary Tubing 0 1007 664 0 1913 7 8:33:57 Pressure Test ePRV - Secondary IA 0 1008 245 0 1913 8 8:43:30 Pressure Test Pressure Test - Locals 0 230 274 0 1913 9 8:43:36 Pressure Test Pressure Test - Global 0 256 309 0 1913 10 8:47:35 Pressure Test Pressure Test - Max 0 9517 9566 0 1913 11 8:52:15 Pressure Test Pressure Test - Pass 0 9330 9381 0 1913 12 9:29:42 Open Well Open Well 0 547 557 0 2473 13 9:42:32 Other Arsenal Burst Disk 1 6957 7031 0 9021 14 9:46:51 Other Alpha Sleeve Shift 2.42 5749 5857 0.1 7921 15 9:54:02 ISIP ISIP 52.4 623 618 0 2797 16 9:59:10 Shut-In Pressure @ 5 Minutes Shut-In Pressure @ 5 Minutes 52.4 660 695 0 2889 17 10:04:15 Shut-In Pressure @ 10 Minutes Shut-In Pressure @ 10 Minutes 52.4 530 570 0 2770 18 10:09:16 Shut-In Pressure @ 15 Minutes Shut-In Pressure @ 15 Minutes 52.4 421 465 0 2666 19 10:29:43 Open Well Open Well 52.4 322 368 0 2463 20 10:32:06 Other Step 1 53.48 1035 1168 1.5 3260 21 10:34:39 Other Step 2 59.11 1137 1213 2.6 3296 22 10:35:52 Other Step 3 63.93 1294 1374 4.2 3419 23 10:36:57 Other Step 4 69.32 1343 1425 5.3 3460 24 10:37:51 Other Step 5 74.59 1412 1507 6.4 3518 25 10:45:16 Start Pad Start Pad 178.9 2277 2475 14.6 4092 26 10:50:10 Alarm Delta Stage At Top Perf = 4 322.11 4712 4944 36.1 6094 27 10:50:15 Alarm Delta Stage At Top Perf = 5 324.55 4697 4916 36.2 6064 28 10:51:37 Alarm Delta Stage At Top Perf = 7 374.93 4665 4891 36.6 6068 29 10:52:30 Alarm Delta Stage At Top Perf = 8 406.96 4705 4928 36.6 6082 30 10:55:05 Alarm Delta Stage At Top Perf = 9 501.26 4650 4849 36.6 5955 31 11:06:02 Other 1st Tracer Drop 902.82 4354 4586 36.7 5719 32 11:10:51 Alarm Delta Stage At Top Perf = 10 1079.67 4359 4595 36.7 5721 33 11:18:44 Alarm Delta Stage At Top Perf = 11 1368.88 4416 4662 36.6 5815 34 11:26:52 Alarm Delta Stage At Top Perf = 12 1666.87 4471 4761 36.7 5972 35 11:33:39 Other 2nd Tracer Drop 1914.46 4445 4694 36.5 5958 36 11:38:18 Alarm Delta Stage At Top Perf = 13 2084.09 4596 4870 36.5 6134 37 11:47:58 Other Bin Swap 2435.41 4616 4909 36.4 6216 38 11:50:15 Alarm Delta Stage At Top Perf = 14 2518.82 4718 5001 36.4 6311 39 11:58:01 Alarm Delta Stage At Top Perf = 15 2801.04 4802 5099 36.3 6449 40 11:59:04 Other Tracer 3rd Drop 2838.96 4841 5088 36.3 6463 2 12:02:28 (04/13/25) Next Treatment Treatment Interval 2 2963.4 4981 5222 36.8 6523 41 12:02:28 Drop Ball Drop Ball for Interval 2 2963.4 4981 5222 36.8 6524 42 12:04:07 Alarm Delta Stage At Top Perf = 16 3024.13 5145 5371 36.8 6557 43 12:10:49 Ball on Seat Ball for Interval 2 on Seat 3225.05 3018 3303 13.7 4538 44 12:11:01 Alarm Delta Stage At Top Perf = 17 3227.81 6256 6579 13.7 7498 45 12:11:17 Break Formation Break Formation 3231.48 2953 3304 13.7 4244 46 12:13:53 Alarm Delta Stage At Top Perf = 1 3279.72 4864 5108 30.2 6033 47 12:19:34 Other 1st Tracer Drop 3483.71 4586 4821 36.9 5991 48 12:29:15 Alarm Delta Stage At Top Perf = 2 3840.83 4530 4713 36.8 5945 49 12:37:06 Alarm Delta Stage At Top Perf = 3 4129.98 4503 4754 36.8 5910 50 12:45:13 Alarm Delta Stage At Top Perf = 4 4428.22 4607 4855 36.7 6092 51 12:48:43 Other 2nd Tracer Drop 4556.06 4518 4781 36.6 6045 52 12:55:55 Alarm Delta Stage At Top Perf = 5 4820.17 4471 4740 36.6 6079 53 13:08:19 Alarm Delta Stage At Top Perf = 6 5272.54 4543 4795 36.4 6207 54 13:11:33 Other ut Sand - Potential High Pressure Leak on Pum 5389.76 3468 3666 31.3 5274 55 13:14:32 Alarm Delta Stage At Top Perf = 7 5485.27 4671 4957 35.8 6299 56 13:15:13 Other 3rd Tracer Drop 5510.12 4658 4945 36.1 6324 57 13:19:32 Alarm Delta Stage At Top Perf = 8 5666.74 4458 4701 36.8 6174 3 13:20:54 (04/13/25) Next Treatment Treatment Interval 3 5716.95 4609 4842 36.8 6218 58 13:20:54 Drop Ball Drop Ball For Interval 3 5716.95 4611 4843 36.8 6218 59 13:21:40 Other Lost Pump 563 due to Packing 5744.86 4862 5081 36.8 6397 60 13:23:34 Alarm Delta Stage At Top Perf = 9 5804.78 4279 4444 30.7 5755 61 13:29:29 Break Formation Break Formation 5965.28 2448 2565 15.5 4263 62 13:29:50 Ball on Seat Ball on Seat for Interval 3 5970.74 2437 2549 15.5 4248 63 13:30:02 Alarm Delta Stage At Top Perf = 10 5974.12 3151 3397 15.4 6510 64 13:30:59 ISIP ISIP 5988.64 2495 2537 15.4 4750 65 14:40:53 Pressure Test Pressure Test - Max 5989.63 9425 9506 0 3233 66 14:45:53 Pressure Test Pressure Test - Pass 5989.63 9280 9331 0 3109 67 14:59:16 Open Well Open Well 5989.63 1035 1029 0 3018 68 15:02:50 Alarm Delta Stage At Top Perf = 1 6025.54 2569 2601 14.2 4318 69 15:07:56 Other Drop First Tracer 6128.83 3972 4106 35.2 5359 70 15:12:31 Alarm Delta Stage At Top Perf = 3 6298.31 4136 4296 37 5464 71 15:14:44 Alarm Delta Stage At Top Perf = 4 6379.98 4168 4316 37 5438 72 15:29:16 Alarm Delta Stage At Top Perf = 5 6919.05 4029 4188 37.1 5319 73 15:37:11 Alarm Delta Stage At Top Perf = 6 7209.82 4062 4265 36.8 5461 74 15:45:18 Alarm Delta Stage At Top Perf = 7 7508.39 4128 4340 36.8 5617 75 15:51:18 Other 2nd Tracer Drop 7728.34 4108 4312 36.6 5624 76 15:55:55 Alarm Delta Stage At Top Perf = 8 7897.17 4233 4456 36.6 5791 77 16:06:23 Alarm Delta Stage At Top Perf = 9 8279.18 4401 4656 36.3 6008 78 16:14:12 Alarm Delta Stage At Top Perf = 10 8562.85 4689 4975 36.2 6281 79 16:14:59 Other 3rd Tracer Drop 8590.29 4699 4990 36.2 6302 80 16:20:13 Alarm Delta Stage At Top Perf = 11 8782.51 5153 5405 36.7 6572 81 16:25:39 ISIP ISIP 8976.61 1332 449 0 3190 82 16:28:56 Other fanning out pumps 8976.61 226 374 0 3145 83 16:30:38 Shut-In Pressure @ 5 Minutes Shut-In Pressure @ 5 Minutes 8976.61 414 518 0 3125 84 16:35:39 Shut-In Pressure @ 10 Minutes Shut-In Pressure @ 10 Minutes 8976.61 17 65 0 3081 85 16:40:28 Shut-In Pressure @ 15 Minutes Shut-In Pressure @ 15 Minutes 8976.61 -18 13 0 3050 86 17:01:06 Other priming with brine 8976.61 8 -1 0 2948 Event Log 4.13.25 Conoco Phillips - 3S-602 Event Log 4.13 176 Seq No. Time Activity Code Comment Job Slurry Vol Treating Pressure Treating Pressure @Pump Slurry Rate Tubing Gauge BH Pres 1 07:19:00 (04/14/25) Start Job Starting Job 0 0 0 16 0 1 07:19:00 (04/14/25) Next Treatment Treatment Interval 1 0 0 0 16 0 4 07:19:23 (04/14/25) Next Treatment Treatment Interval 4 6 -50 -9 16 0 2 12:55:51 Prime Pumps Prime Pumps 6 196 262 0 2237 3 13:07:37 Pressure Test ePRV - Primary Tubing 6 795 841 0 2236 4 13:09:26 Pressure Test ePRV - Primary IA 6 872 840 0 2236 5 13:10:58 Pressure Test ePRV - Secondary Tubing 6 815 864 0 2236 6 13:12:00 Pressure Test ePRV - Secondary IA 6 844 897 0 2236 7 13:13:25 Pressure Test Pressure Test - Global 6 174 193 0 2235 8 13:13:30 Pressure Test Pressure Test - Local 6 189 213 0 2235 9 13:15:38 Pressure Test Pressure Test - Max 6 9522 9575 0 2235 10 13:20:37 Pressure Test Pressure Test - Pass 6 9335 9370 0 2235 11 13:41:16 Open Well Open Well 6 536 486 0 2241 12 13:43:19 Drop Ball Drop Ball For Interval 4 21.67 2197 2332 14.2 3754 13 13:51:39 Start Pad Start Pad 152.97 2079 2291 15.7 3895 14 13:57:09 Other First Tracer Drop 236.41 2412 2612 15.6 3881 15 13:59:34 Ball on Seat Ball for Interval 4 on Seat 273.97 2412 2615 15.6 3864 16 13:59:38 Break Formation Break Formation 275.28 2896 3084 15.6 4388 17 14:01:39 Alarm Delta Stage At Top Perf = 4 308.26 2893 3084 18.4 4248 18 14:03:08 Alarm Delta Stage At Top Perf = 5 340.52 3355 3569 25 4698 19 14:06:38 Alarm Delta Stage At Top Perf = 6 452.85 4521 4666 36.6 5800 20 14:18:03 Alarm Delta Stage At Top Perf = 7 872.11 4382 4563 36.7 5572 21 14:25:56 Alarm Delta Stage At Top Perf = 8 1160.6 4176 4398 36.5 5480 22 14:31:43 Alarm Delta Stage At Top Perf = 9 1371.14 4213 4464 36.3 5605 23 14:34:26 Other 2nd Tracer Drop 1469.66 4244 4486 36.3 5673 24 14:37:49 Alarm Delta Stage At Top Perf = 10 1592.89 4397 4636 36.1 5845 25 14:43:08 Other Pump 458 Engine Issue 1784.58 4536 4783 36 6035 26 14:44:00 Alarm Delta Stage At Top Perf = 11 1810.91 3558 3831 28.2 5225 27 14:51:26 Alarm Delta Stage At Top Perf = 12 2065.85 4875 5160 35.9 6452 28 14:57:57 Alarm Delta Stage At Top Perf = 13 2301.35 5398 5660 36.5 6943 29 15:00:49 Other 3rd Tracer Drop 2406.82 5516 5718 37.2 7042 30 15:02:01 Drop Ball Drop Ball for Interval 05 2450.6 5612 5781 37.1 7024 5 15:02:03 (04/14/25) Next Treatment Treatment Interval 5 2451.85 5616 5786 37.1 7034 31 15:03:31 Alarm Delta Stage At Top Perf = 14 2506.75 5750 5936 37 7066 32 15:05:16 Other 1st Tracer Drop 2571.6 5430 5580 37 6671 33 15:09:50 Alarm Delta Stage At Top Perf = 15 2692.04 2816 3080 14.7 4302 34 15:09:52 Ball on Seat Ball for Interval 5 on Seat 2692.29 2818 3082 14.7 4307 35 15:10:03 Break Formation Break Formation 2695.01 5244 6023 14.7 7374 36 15:13:00 Alarm Delta Stage At Top Perf = 1 2748.09 3558 3746 26.2 4665 37 15:19:26 Alarm Delta Stage At Top Perf = 2 2975.32 4223 4400 36.9 5477 38 15:27:15 Alarm Delta Stage At Top Perf = 3 3264.16 3961 4219 37 5436 39 15:28:35 Alarm Delta Stage At Top Perf = 4 3313.94 4076 4349 37 5572 40 15:30:20 Alarm Delta Stage At Top Perf = 5 3378.51 4262 4559 36.8 5779 41 15:33:16 Alarm Delta Stage At Top Perf = 6 3486 4481 4732 36.8 6018 42 15:37:00 Alarm Delta Stage At Top Perf = 7 3623.38 4649 4921 36.8 6186 43 15:40:54 Alarm Delta Stage At Top Perf = 8 3766.66 4985 5296 36.6 6395 44 15:45:15 Alarm Delta Stage At Top Perf = 9 3925.66 5313 5625 36.6 6714 45 15:46:56 Other Bin Swap 3987.17 5435 5746 36.5 6835 46 15:49:42 Alarm Delta Stage At Top Perf = 10 4088.75 5642 5937 36.5 7030 47 15:52:16 Other 3rd Tracer Drop 4182.09 5307 5548 36.5 6737 48 15:54:32 Alarm Delta Stage At Top Perf = 11 4265.72 5257 5447 37.2 6645 6 15:55:22 (04/14/25) Next Treatment Treatment Interval 6 4296.23 5338 5571 36.9 6694 49 15:55:22 Drop Ball Drop Ball For Interval 6 4296.23 5339 5572 36.9 6694 50 15:58:37 Alarm Delta Stage At Top Perf = 12 4416.7 5458 5660 36.9 6675 51 15:59:37 Other 1st Tracer Drop 4453.34 5105 5300 37 6302 52 16:03:25 Ball on Seat Ball For Interval 6 on Seat 4530.86 2923 3205 14.8 4349 53 16:03:32 Alarm Delta Stage At Top Perf = 13 4532.6 5283 5559 14.8 6408 54 16:03:36 Break Formation Break Formation 4533.6 5028 5738 14.8 7464 55 16:06:12 Alarm Delta Stage At Top Perf = 1 4584.76 3808 4043 27.3 4999 56 16:12:28 Alarm Delta Stage At Top Perf = 2 4810.59 4358 4575 37 5590 57 16:20:17 Alarm Delta Stage At Top Perf = 3 5099.61 4178 4476 37 5633 58 16:21:36 Alarm Delta Stage At Top Perf = 4 5148.2 4297 4588 37 5746 59 16:23:21 Alarm Delta Stage At Top Perf = 5 5212.83 4439 4740 36.9 5913 60 16:26:20 Alarm Delta Stage At Top Perf = 6 5322.83 4667 4948 36.9 6148 61 16:30:03 Alarm Delta Stage At Top Perf = 7 5459.92 4797 5099 36.8 6305 62 16:33:57 Alarm Delta Stage At Top Perf = 8 5603.59 4939 5233 36.7 6451 63 16:34:39 Other 2nd Tracer Drop 5628.97 4974 5259 36.8 6474 64 16:38:15 Alarm Delta Stage At Top Perf = 9 5761.27 5076 5345 36.7 6593 65 16:42:44 Alarm Delta Stage At Top Perf = 10 5925.46 5233 5502 36.7 6714 66 16:45:17 Other 3rd Tracer Drop 6019.13 5323 5641 36.6 6793 67 16:47:29 Drop Ball Drop Ball for Interval 7 6100.22 5535 5740 37 6887 68 16:47:31 Alarm Delta Stage At Top Perf = 11 6101.46 5538 5743 37 6890 7 16:47:31 (04/14/25) Next Treatment Treatment Interval 7 6101.46 5538 5743 37 6890 69 16:49:14 Other 1st Tracer Drop 6164.91 5655 5839 36.9 6940 70 16:50:39 Alarm Delta Stage At Top Perf = 12 6217.81 5302 5500 37 6559 71 16:55:03 Alarm Delta Stage At Top Perf = 13 6324.64 2751 3044 14.9 4197 72 16:55:18 Ball on Seat Ball for Interval 7 on Seat 6328.16 2769 3072 14.9 4205 73 16:55:27 Break Formation Break Formation 6330.67 5780 5987 14.9 7090 74 16:57:46 Other 1st Tracer Drop 6370.79 4069 4327 24.5 5200 75 16:58:12 Alarm Delta Stage At Top Perf = 1 6382.65 4174 4437 27.6 5338 76 17:04:30 Alarm Delta Stage At Top Perf = 2 6609.73 4561 4746 37 5792 77 17:11:18 Other 2nd Tracer Drop 6860.56 4155 4449 36.9 5587 78 17:12:18 Alarm Delta Stage At Top Perf = 3 6897.83 4195 4444 36.9 5634 79 17:13:39 Alarm Delta Stage At Top Perf = 4 6947.44 4191 4438 36.9 5646 80 17:15:26 Alarm Delta Stage At Top Perf = 5 7013.46 4246 4529 37 5732 81 17:18:22 Alarm Delta Stage At Top Perf = 6 7121.72 4422 4686 36.9 5922 82 17:22:05 Alarm Delta Stage At Top Perf = 7 7258.88 4602 4882 36.9 6093 83 17:26:00 Alarm Delta Stage At Top Perf = 8 7403.27 4801 5063 36.8 6292 84 17:30:20 Alarm Delta Stage At Top Perf = 9 7562.2 4944 5229 36.7 6450 85 17:34:50 Alarm Delta Stage At Top Perf = 10 7726.95 5071 5322 36.6 6560 86 17:36:23 Other 3rd Tracer Drop 7783.01 5118 5408 36.5 6607 87 17:39:38 Alarm Delta Stage At Top Perf = 11 7903.53 5397 5619 37.2 6783 88 17:42:58 Alarm Delta Stage At Top Perf = 12 8027.49 4889 5071 37.3 6247 89 17:45:54 ISIP ISIP 8135.76 172 227 15.9 2382 90 17:50:54 Shut-In Pressure @ 5 Minutes Shut-In Pressure @ 5 Minutes 8136.58 333 393 0 2400 91 17:52:53 Other blowing down lines 8136.58 64 203 0 2407 92 17:55:54 Shut-In Pressure @ 10 Minutes Shut-In Pressure @ 10 Minutes 8136.58 479 588 0 2419 93 18:00:42 Shut-In Pressure @ 15 Minutes Shut-In Pressure @ 15 Minutes 8136.58 11 40 0 2443 94 18:19:28 Other brine up lines 8136.58 76 84 0 2359 Event Log 4.14.25 Conoco Phillips - 3S-602 Event Log 4.14 177 Seq No. Time Activity Code Comment Job Slurry Vol Treating Pressure Treating Pressure @Pump Slurry Rate Tubing Gauge BH Pres 1 05:56:24 (04/15/25) Other Crew Arrived On Location ---- ---- ---- ---- ---- 2 6:13:35 Start Job Starting Job 0 0 0 0 0 1 06:13:35 (04/15/25) Next Treatment Treatment Interval 1 0 0 0 0 0 8 06:14:54 (04/15/25) Next Treatment Treatment Interval 8 0 64 15 0 2232 3 6:30:00 Pre-Job Safety Meeting Pre-Job Safety Meeting 0 60 17 0 2230 4 7:02:15 Prime Pumps Prime Pumps 0 41 -4 0 2227 5 7:33:39 Pressure Test ePRV - Primary Tubing 0 784 808 0 2224 6 7:37:23 Pressure Test ePRV - Primary IA 0 700 734 0 2223 7 7:39:42 Pressure Test ePRV - Secondary Tubing 0 653 697 0 2223 8 7:41:21 Pressure Test ePRV - Secondary IA 0 712 755 0 2223 9 7:45:22 Other Packing on Pump 458 0 18 16 0 2222 10 8:08:03 Pressure Test Pressure Test - Global 0 187 200 0 2220 11 8:11:56 Pressure Test Pressure Test - Locals 0 894 897 0 2220 12 8:16:44 Other Pump 329 Leak on High Pressure Seal 0 1655 1652 0 2220 13 8:28:43 Pressure Test Pressure Test - Max 0 9427 9498 0 2219 14 8:33:44 Pressure Test Pressure Test - Pass 0 9333 9379 0 2218 15 8:41:59 Other Mix Gel and Load Chemicals 0 21 34 0 2218 16 9:01:34 Open Well Open Well 0 370 406 0 2217 17 9:03:23 Drop Ball Drop Ball for interval 8 11.44 1588 1665 14 3205 18 9:09:17 Start Pad Start Pad 98.03 1594 1788 14.6 3391 19 9:18:23 Ball on Seat Ball for interval 8 on Seat 231.33 2065 2279 14.6 3521 20 9:18:32 Break Formation Break Formation 233.55 4733 5043 14.6 6127 21 9:19:39 Other 1st Tracer Drop 249.91 2626 2898 16.3 3967 22 9:20:37 Alarm Delta Stage At Top Perf = 4 270.35 3088 3280 25.9 4378 23 9:21:21 Alarm Delta Stage At Top Perf = 5 292.09 3190 3407 33.1 4556 24 9:23:27 Alarm Delta Stage At Top Perf = 6 368.2 3613 3794 36.6 4999 25 9:29:50 Alarm Delta Stage At Top Perf = 7 602.82 3393 3601 36.8 4676 26 9:37:41 Alarm Delta Stage At Top Perf = 8 889.61 3417 3699 36.2 4908 27 9:39:03 Alarm Delta Stage At Top Perf = 9 939.02 3473 3769 36.2 5003 28 9:40:47 Alarm Delta Stage At Top Perf = 10 1001.76 3577 3875 36.1 5102 29 9:43:47 Alarm Delta Stage At Top Perf = 11 1110.13 3709 3983 36.1 5270 30 9:47:36 Alarm Delta Stage At Top Perf = 12 1247.45 3815 4095 36.1 5375 31 9:49:22 Other 2nd Tracer Drop 1311.21 3828 4136 36 5415 32 9:51:36 Alarm Delta Stage At Top Perf = 13 1391.94 3907 4178 36 5479 33 9:56:00 Alarm Delta Stage At Top Perf = 14 1550.08 4029 4344 35.9 5612 34 10:00:34 Alarm Delta Stage At Top Perf = 15 1713.88 4183 4491 35.8 5799 35 10:02:10 Other 3rd Tracer Drop 1771.19 4227 4542 35.8 5837 36 10:05:29 Alarm Delta Stage At Top Perf = 16 1891.01 4407 4635 36.6 5957 37 10:05:55 Drop Ball Drop Ball For Interval 09 1906.4 4469 4702 36.6 5970 9 10:05:58 (04/15/25) Next Treatment Treatment Interval 9 1908.25 4474 4708 36.6 5979 38 10:07:38 Other 1st Tracer Drop 1969.83 4620 4829 36.5 5990 39 10:08:39 Alarm Delta Stage At Top Perf = 17 2006.71 4523 4724 36.5 5809 40 10:13:13 Ball on Seat Ball For Interval 9 on Seat 2119.59 2707 3018 14.6 4148 41 10:13:13 Alarm Delta Stage At Top Perf = 18 2119.84 2801 3087 14.6 4188 42 10:13:22 Break Formation Break Formation 2122.05 5754 6178 14.6 7087 43 10:15:51 Alarm Delta Stage At Top Perf = 1 2172.4 4198 4445 33.1 5283 44 10:22:02 Alarm Delta Stage At Top Perf = 2 2399.93 3847 4066 37 5155 45 10:29:51 Alarm Delta Stage At Top Perf = 3 2688.58 3797 4073 36.8 5323 46 10:31:11 Alarm Delta Stage At Top Perf = 4 2738.19 3843 4116 36.8 5376 47 10:32:56 Alarm Delta Stage At Top Perf = 5 2802.66 3852 4151 36.7 5425 48 10:35:53 Alarm Delta Stage At Top Perf = 6 2910.93 3920 4185 36.7 5501 49 10:37:22 Other 2nd Tracer Drop 2964.73 3931 4222 36.7 5518 50 10:39:37 Alarm Delta Stage At Top Perf = 7 3047.63 3934 4213 36.7 5544 51 10:43:30 Alarm Delta Stage At Top Perf = 8 3190.28 3981 4289 36.7 5612 52 10:47:56 Alarm Delta Stage At Top Perf = 9 3352.62 4011 4307 36.6 5646 53 10:52:23 Alarm Delta Stage At Top Perf = 10 3515.37 4040 4354 36.6 5697 54 10:52:45 Other Some ice on hopper Screens 3528.31 4057 4367 36.5 5702 55 10:53:49 Other 3rd Tracer Drop 3567.08 4074 4375 36.5 5707 56 10:57:11 Alarm Delta Stage At Top Perf = 11 3691.31 4203 4433 37.2 5845 57 10:57:55 Drop Ball Drop Ball For Interval 10 3718.17 4278 4503 37 5854 10 10:57:58 (04/15/25) Next Treatment Treatment Interval 10 3720.04 4283 4514 37 5842 58 11:00:18 Alarm Delta Stage At Top Perf = 12 3806.54 4373 4599 37 5742 59 11:01:01 Other 1st Tracer Drop 3832.73 4172 4397 37 5514 60 11:04:52 Alarm Delta Stage At Top Perf = 13 3922.07 2604 2923 14.7 4093 61 11:05:02 Ball on Seat Ball for Interval 10 Seat 3924.31 2619 2948 14.8 4102 62 11:05:10 Break Formation Break Formation 3926.55 5625 5909 14.7 7159 63 11:07:38 Alarm Delta Stage At Top Perf = 1 3976.39 4043 4279 33.5 5189 64 11:13:47 Alarm Delta Stage At Top Perf = 2 4203.05 3674 3892 37 5048 65 11:21:35 Alarm Delta Stage At Top Perf = 3 4491.1 3593 3871 36.6 5063 66 11:22:56 Alarm Delta Stage At Top Perf = 4 4540.44 3544 3818 36.6 5082 67 11:24:42 Alarm Delta Stage At Top Perf = 5 4605.4 3583 3889 36.9 5155 68 11:27:38 Alarm Delta Stage At Top Perf = 6 4713.79 3643 3934 37 5223 69 11:29:25 Other 2nd Tracer Drop 4779.06 3640 3970 36.9 5247 70 11:31:22 Alarm Delta Stage At Top Perf = 7 4851.18 3697 4005 36.9 5298 71 11:35:17 Alarm Delta Stage At Top Perf = 8 4995.81 3855 4162 36.8 5430 72 11:39:37 Alarm Delta Stage At Top Perf = 9 5155.13 3995 4329 36.8 5601 73 11:44:05 Alarm Delta Stage At Top Perf = 10 5319.21 4120 4424 36.7 5721 74 11:45:35 Other 3rd Tracer Drop 5373.6 4180 4498 36.6 5757 75 11:48:53 Alarm Delta Stage At Top Perf = 11 5495.76 4240 4465 37.1 5801 76 11:49:37 Drop Ball Drop Ball For Interval 11 5522.6 4329 4556 37 5826 11 11:49:38 (04/15/25) Next Treatment Treatment Interval 11 5523.22 4330 4559 37 5828 77 11:52:03 Alarm Delta Stage At Top Perf = 12 5612.92 4375 4598 37 5710 78 11:55:25 Other 1st Tracer Drop 5704.01 2466 2745 14.5 3991 79 11:56:31 Alarm Delta Stage At Top Perf = 13 5720.08 2559 2886 14.5 4027 80 11:56:41 Ball on Seat Ball For interval 11 on Seat 5722.28 2577 2908 14.5 4036 81 11:56:50 Break Formation Break Formation 5724.48 5782 6102 14.5 6985 82 11:59:21 Alarm Delta Stage At Top Perf = 1 5772.1 3266 3517 30.9 4404 83 12:05:37 Alarm Delta Stage At Top Perf = 2 6001.64 3072 3295 37.1 4395 84 12:13:27 Alarm Delta Stage At Top Perf = 3 6290.99 3090 3386 37 4603 85 12:14:49 Alarm Delta Stage At Top Perf = 4 6341.38 3150 3460 36.9 4693 86 12:16:34 Alarm Delta Stage At Top Perf = 5 6406.28 3231 3529 37.2 4796 87 12:19:30 Alarm Delta Stage At Top Perf = 6 6514.99 3383 3676 37 4955 88 12:21:10 Other 2nd Tracer Drop 6576.03 3400 3701 36.9 4975 89 12:23:15 Alarm Delta Stage At Top Perf = 7 6653.86 3423 3716 36.9 5026 90 12:27:08 Alarm Delta Stage At Top Perf = 8 6796.76 3533 3855 36.8 5140 91 12:31:28 Alarm Delta Stage At Top Perf = 9 6956.09 3615 3969 36.8 5264 92 12:35:56 Alarm Delta Stage At Top Perf = 10 7120.78 3793 4100 36.7 5399 93 12:36:28 Other 3rd Tracer Drop 7139.92 3792 4107 36.7 5402 94 12:40:44 Alarm Delta Stage At Top Perf = 11 7297.33 4033 4276 37.2 5552 12 12:41:57 (04/15/25) Next Treatment Treatment Interval 12 7342.3 4158 4402 37 5601 95 12:41:58 Drop Ball Drop Ball for Interval 12 7342.3 4160 4404 37 5599 96 12:43:54 Alarm Delta Stage At Top Perf = 12 7414.53 4227 4428 37 5562 97 12:47:22 Other 1st Tracer Drop 7515.85 2319 2603 14.5 3895 98 12:48:25 Alarm Delta Stage At Top Perf = 13 7530.99 2417 2746 14.5 3944 99 12:48:31 Ball on Seat Ball for Interval 12 on Seat 7532.46 2432 2767 14.5 3954 100 12:48:39 Break Formation Break Formation 7534.17 5581 5878 14.5 6997 101 12:51:16 Alarm Delta Stage At Top Perf = 1 7583.9 3893 4171 30.7 5048 102 12:57:29 Alarm Delta Stage At Top Perf = 2 7811.58 3660 3885 37 5001 103 13:05:18 Alarm Delta Stage At Top Perf = 3 8100.62 3495 3753 36.9 5008 104 13:06:40 Alarm Delta Stage At Top Perf = 4 8150.92 3380 3667 36.8 4928 105 13:08:24 Alarm Delta Stage At Top Perf = 5 8214.86 3370 3660 36.8 4936 106 13:11:20 Alarm Delta Stage At Top Perf = 6 8322.76 3492 3765 36.9 5042 107 13:13:08 Other 2nd Tracer Drop 8389.32 3508 3815 36.9 5096 108 13:15:02 Alarm Delta Stage At Top Perf = 7 8459.56 3593 3891 36.9 5148 109 13:18:57 Alarm Delta Stage At Top Perf = 8 8604.22 3686 3979 36.8 5270 110 13:23:16 Alarm Delta Stage At Top Perf = 9 8763.03 3750 4056 36.8 5342 111 13:27:41 Alarm Delta Stage At Top Perf = 10 8925.33 3816 4134 36.7 5431 112 13:30:11 Other 3rd Tracer Drop 9016.78 3846 4181 36.7 5450 113 13:32:30 Alarm Delta Stage At Top Perf = 11 9102.32 3934 4226 37.3 5518 114 13:32:33 Start Flush Start Flush 9103.57 3934 4230 37.3 5515 115 13:35:50 Alarm Delta Stage At Top Perf = 12 9225.56 4102 4406 37 5524 116 13:39:06 ISIP ISIP 9343.73 1491 410 0 3225 117 13:42:50 Other fanning out 9343.73 -30 105 0 3177 118 13:44:08 Shut-In Pressure @ 5 Minutes Shut-In Pressure @ 5 Minutes 9343.73 405 572 0 3166 119 13:49:07 Shut-In Pressure @ 10 Minutes Shut-In Pressure @ 10 Minutes 9343.73 -51 31 0 3136 120 13:54:07 Shut-In Pressure @ 15 Minutes Shut-In Pressure @ 15 Minutes 9343.73 -55 14 0 3114 121 14:12:50 Other brine lines 9343.73 22 75 0 3015 Event Log 4.15.25 Conoco Phillips - 3S-602 Event Log 4.15 178 Seq No. Time Activity Code Comment Job Slurry Vol Treating Pressure Treating Pressure @Pump Slurry Rate Tubing Gauge BH Pres 1 05:52:41 (04/20/25) Other Crew Arrived on Location ---- ---- ---- ---- ---- 2 6:05:07 Start Job Starting Job 0 0 0 0 0 1 06:05:07 (04/20/25) Next Treatment Treatment Interval 1 0 0 0 0 1 13 06:11:18 (04/20/25) Next Treatment Treatment Interval 13 0 6 -15 0 2103 3 6:30:08 Pre-Job Safety Meeting Pre-Job Safety Meeting 0 7 -15 0 2103 4 7:10:23 Other Loop Test 0 70 -8 0 2103 5 7:18:56 Prime Pumps Prime Pumps 0 80 16 0 2103 6 7:35:59 Pressure Test ePRV - Primary Tubing 0 935 987 0 2103 7 7:38:43 Pressure Test ePRV - Primary IA 0 970 664 0 2103 8 7:41:35 Pressure Test ePRV - Secondary Tubing 0 976 946 0 2103 9 7:42:53 Pressure Test ePRV - Secondary IA 0 995 974 0 2103 10 7:47:30 Pressure Test Pressure Test - Max 0 9529 9625 0 2103 11 7:48:25 Pressure Test Pressure Test - Fail 0 9052 9017 0 2103 12 7:49:23 Other Leak on High Pressure Seal on Chik 0 8162 8120 0 2103 13 8:05:22 Pressure Test Pressure Test - Global 0 240 249 0 2103 14 8:05:30 Pressure Test Pressure Test - Locals 0 271 289 0 2103 15 8:07:12 Pressure Test Pressure Test - Pass 0 9537 9516 0 2103 16 8:11:14 Pressure Test Pressure Test - Fail 0 9433 8921 0 2103 17 8:14:42 Pressure Test Pressure Test - Start 0 9531 9452 0 2103 18 8:20:19 Pressure Test Pressure Test - Pass 0 8927 8862 0 2103 19 8:24:31 Other Bring on Chems & Load Balls 0 70 11 0 2103 20 8:44:37 Open Well Open Well 0 380 256 0 2091 21 8:46:27 Drop Ball Drop Ball for Interval 13 14.82 1651 1667 14.7 3056 22 8:58:11 Ball on Seat Ball for Interval 13 on Seat 192.53 1469 1462 15.1 3182 23 8:58:17 Break Formation Break Formation 194.04 3704 3761 15.1 5484 24 9:01:39 Alarm Delta Stage At Top Perf = 4 231.29 1527 1512 10.1 3317 25 9:03:13 ISIP ISIP 245.78 1138 578 0 3026 26 9:08:04 Shut-In Pressure @ 5 Minutes Shut-In Pressure @ 5 Minutes 245.78 930 251 0 2699 27 9:13:06 Shut-In Pressure @ 10 Minutes Shut-In Pressure @ 10 Minutes 245.78 838 139 0 2300 28 9:18:01 Shut-In Pressure @ 15 Minutes Shut-In Pressure @ 15 Minutes 245.78 761 67 0 2178 29 9:26:02 Open Well Open Well 245.78 230 138 0 2173 30 9:28:08 Other Step 1 247.58 1004 1029 1.1 2982 31 9:30:32 Other Step 2 251.51 1056 1057 1.9 2996 32 9:31:40 Alarm Delta Stage At Top Perf = 5 254.59 1118 1131 2.9 3053 33 9:32:44 Other Step 3 258.59 1154 1158 3.9 3075 34 9:33:18 Other Step 4 261.18 1188 1205 4.9 3117 35 9:39:14 Other 1st Tracer Drop 369.59 2562 2736 30.6 4027 36 9:41:10 Alarm Delta Stage At Top Perf = 6 436.59 2823 2970 35.8 4173 37 9:42:19 Alarm Delta Stage At Top Perf = 8 477.96 2921 3080 36.1 4206 38 9:42:51 Alarm Delta Stage At Top Perf = 9 497.32 3068 3207 36.7 4296 39 9:44:38 Alarm Delta Stage At Top Perf = 10 563.26 3123 3287 37 4354 40 9:50:43 Alarm Delta Stage At Top Perf = 11 788.63 3219 3375 37 4407 41 9:54:55 Other Preload Kicked a Pump 943.54 3200 3381 37 4425 42 9:58:36 Alarm Delta Stage At Top Perf = 12 1077.01 3161 3369 36.8 4517 43 9:58:47 Other 2nd Tracer Drop 1083.77 3167 3385 36.9 4527 44 9:59:52 Alarm Delta Stage At Top Perf = 13 1123.75 3192 3415 36.9 4587 45 10:01:36 Alarm Delta Stage At Top Perf = 14 1187.79 3209 3425 37 4649 46 10:04:32 Alarm Delta Stage At Top Perf = 15 1296.21 3278 3507 36.9 4739 47 10:08:15 Alarm Delta Stage At Top Perf = 16 1433.59 3354 3578 36.9 4825 48 10:12:08 Alarm Delta Stage At Top Perf = 17 1576.93 3435 3666 36.9 4912 49 10:16:27 Alarm Delta Stage At Top Perf = 18 1736.42 3577 3822 37 5063 50 10:20:55 Alarm Delta Stage At Top Perf = 19 1901.44 3636 3867 36.9 5139 51 10:22:56 Other 3rd Tracer Drop 1975.87 3630 3880 36.9 5122 52 10:25:40 Alarm Delta Stage At Top Perf = 20 2076.8 3728 3965 37.3 5233 53 10:27:21 Drop Ball Drop Ball For Interval 14 2139.72 3778 3948 37.1 5209 14 10:27:24 (04/20/25) Next Treatment Treatment Interval 14 2141.58 3782 3957 37.1 5214 54 10:28:48 Alarm Delta Stage At Top Perf = 21 2193.46 3912 4071 37 5231 55 10:33:25 Alarm Delta Stage At Top Perf = 22 2312.94 2581 2811 14.3 3958 56 10:33:42 Ball on Seat Ball For Interval 14 on Seat 2316.75 2609 2844 14.3 3974 57 10:33:50 Break Formation Break Formation 2318.65 5567 5805 14.3 6871 58 10:34:26 Other 1st Tracer Drop 2327.45 2562 2784 14.3 3874 59 10:36:09 Alarm Delta Stage At Top Perf = 1 2365.97 3207 3371 33.7 4285 60 10:42:13 Alarm Delta Stage At Top Perf = 2 2589.71 2850 3022 37 4115 61 10:50:01 Alarm Delta Stage At Top Perf = 3 2877.36 2897 3120 36.6 4293 62 10:50:12 Other 2nd Tracer Drop 2883.44 2904 3116 36.6 4295 63 10:51:22 Alarm Delta Stage At Top Perf = 4 2926.68 2951 3185 36.8 4362 64 10:53:06 Alarm Delta Stage At Top Perf = 5 2990.82 2991 3201 37.1 4433 65 10:56:02 Alarm Delta Stage At Top Perf = 6 3099.3 3096 3331 36.9 4562 66 10:59:45 Alarm Delta Stage At Top Perf = 7 3236.47 3178 3420 36.9 4660 67 11:03:39 Alarm Delta Stage At Top Perf = 8 3380.13 3266 3513 36.8 4754 68 11:07:57 Alarm Delta Stage At Top Perf = 9 3538.38 3348 3602 36.8 4845 69 11:12:26 Alarm Delta Stage At Top Perf = 10 3703.13 3494 3744 36.7 4981 70 11:14:16 Other 3rd Tracer Drop 3769.86 3500 3761 36.7 4992 71 11:17:14 Alarm Delta Stage At Top Perf = 11 3879.31 3492 3770 36.9 5031 72 11:19:02 Drop Ball Drop Ball for Interval 15 3945.39 3532 3707 36.9 4983 15 11:19:05 (04/20/25) Next Treatment Treatment Interval 15 3947.24 3534 3714 36.9 4980 73 11:20:09 Other 1st Tracer Drop 3986.6 3647 3808 36.9 4999 74 11:20:19 Alarm Delta Stage At Top Perf = 12 3993.37 3652 3813 36.9 4994 75 11:25:00 Alarm Delta Stage At Top Perf = 13 4111.51 2490 2732 14.5 3884 76 11:25:16 Ball on Seat Ball For Interval 15 on Seat 4115.36 2527 2769 14.5 3901 77 11:25:24 Break Formation Break Formation 4117.29 5196 5535 14.5 6588 78 11:27:35 Alarm Delta Stage At Top Perf = 1 4164.21 3212 3305 35 4211 79 11:33:39 Alarm Delta Stage At Top Perf = 2 4389.1 2793 2965 37 4122 80 11:41:28 Alarm Delta Stage At Top Perf = 3 4677.57 2798 3011 36.7 4244 81 11:42:19 Other 2nd Tracer 4708.74 2814 3033 36.6 4270 82 11:42:49 Alarm Delta Stage At Top Perf = 4 4727.05 2822 3035 36.6 4284 83 11:44:34 Alarm Delta Stage At Top Perf = 5 4791.33 2864 3075 37.1 4349 84 11:47:30 Alarm Delta Stage At Top Perf = 6 4900.24 2905 3130 37.1 4428 85 11:51:00 Other Bin Swap 5030.1 2909 3136 37.1 4456 86 11:51:12 Alarm Delta Stage At Top Perf = 7 5037.52 2910 3148 37.1 4454 87 11:55:05 Alarm Delta Stage At Top Perf = 8 5181.72 2961 3150 37.2 4499 88 11:59:13 Alarm Delta Stage At Top Perf = 9 5334.86 2796 3033 37 4393 89 12:03:34 Alarm Delta Stage At Top Perf = 10 5495.84 2993 3221 36.9 4584 90 12:08:21 Alarm Delta Stage At Top Perf = 11 5672.52 3146 3397 36.9 4702 91 12:11:17 Drop Ball Drop Ball for Interval 16 5781.33 3371 3541 37.6 4841 92 12:11:19 Other 1st Tracer Drop 5783.21 3385 3548 37.6 4848 16 12:11:20 (04/20/25) Next Treatment Treatment Interval 16 5783.84 3386 3553 37.6 4849 93 12:11:28 Alarm Delta Stage At Top Perf = 12 5788.85 3393 3567 37.6 4849 94 12:17:10 Alarm Delta Stage At Top Perf = 13 5941.49 2407 2574 14.9 3817 95 12:17:27 Ball on Seat Ball for Interval 16 on Seat 5945.46 2429 2587 14.9 3832 96 12:17:34 Break Formation Break Formation 5947.2 5131 5671 14.8 6637 97 12:19:48 Alarm Delta Stage At Top Perf = 1 5993.25 3425 3681 33.6 4766 98 12:21:44 Alarm Delta Stage At Top Perf = 2 6064.2 3246 3419 37.2 4754 99 12:28:17 Other 2nd Tracer Drop 6306.86 3285 3486 36.8 4740 100 12:29:30 Alarm Delta Stage At Top Perf = 3 6352.33 3311 3522 37 4809 101 12:30:23 Alarm Delta Stage At Top Perf = 4 6384.97 3271 3471 37 4773 102 12:31:35 Alarm Delta Stage At Top Perf = 5 6429.38 3163 3391 37 4709 103 12:33:41 Alarm Delta Stage At Top Perf = 6 6507.04 3120 3347 37 4689 104 12:36:13 Alarm Delta Stage At Top Perf = 7 6600.73 3074 3306 37 4648 105 12:38:53 Alarm Delta Stage At Top Perf = 8 6699.38 3040 3271 37 4626 106 12:41:54 Alarm Delta Stage At Top Perf = 9 6810.73 3033 3265 36.9 4622 107 12:44:20 Other 3rd Tracer Drop 6900.6 3045 3299 37.1 4648 108 12:44:58 Alarm Delta Stage At Top Perf = 10 6924.1 3052 3293 37 4642 109 12:48:15 Alarm Delta Stage At Top Perf = 11 7045.91 3074 3274 37.3 4657 110 12:49:33 Drop Ball Drop Ball For Interval 17 7094.44 3192 3370 37.3 4693 17 12:49:34 (04/20/25) Next Treatment Treatment Interval 17 7094.44 3193 3372 37.3 4692 111 12:50:19 Alarm Delta Stage At Top Perf = 12 7123.01 3282 3463 37.2 4722 112 12:50:32 Ball on Seat 1st Tracer Drop 7130.45 3331 3484 37.2 4723 113 12:55:04 Alarm Delta Stage At Top Perf = 13 7241.67 2373 2610 14.5 3799 114 12:55:35 Ball on Seat Ball For Interval 17 on Seat 7248.94 2405 2654 14.6 3843 115 12:55:41 Break Formation Break Formation 7250.4 5138 5318 14.6 6475 116 12:57:46 Alarm Delta Stage At Top Perf = 1 7295.92 3689 3867 34.8 4787 117 12:59:42 Alarm Delta Stage At Top Perf = 2 7366.77 3228 3366 37.2 4621 118 13:07:26 Alarm Delta Stage At Top Perf = 3 7653.95 3152 3430 36.8 4567 119 13:07:50 Other 2nd Tracer 7668.69 3179 3474 36.8 4593 120 13:08:21 Alarm Delta Stage At Top Perf = 4 7687.72 3218 3511 36.9 4623 121 13:09:32 Alarm Delta Stage At Top Perf = 5 7731.45 3263 3543 37 4632 122 13:11:35 Alarm Delta Stage At Top Perf = 6 7807.28 3339 3647 37 4702 123 13:14:09 Alarm Delta Stage At Top Perf = 7 7902.1 3404 3739 37 4730 124 13:16:50 Alarm Delta Stage At Top Perf = 8 8001.22 3467 3825 36.9 4775 125 13:19:56 Alarm Delta Stage At Top Perf = 9 8115.62 3583 3920 37 4836 126 13:22:24 Other 3rd Tracer Drop 8206.91 3332 3579 37 4857 127 13:23:03 Alarm Delta Stage At Top Perf = 10 8230.95 3274 3512 37 4825 128 13:26:19 Alarm Delta Stage At Top Perf = 11 8352.75 3047 3313 37.5 4595 129 13:28:19 Alarm Delta Stage At Top Perf = 12 8427.25 3187 3415 37.2 4576 130 13:30:39 ISIP ISIP 8512.11 1635 1783 0 3289 131 13:33:59 Other blowing down pumps 8512.11 60 119 0 3239 132 13:35:40 Shut-In Pressure @ 5 Minutes Shut-In Pressure @ 5 Minutes 8512.11 489 587 0 3225 133 13:40:34 Shut-In Pressure @ 10 Minutes Shut-In Pressure @ 10 Minutes 8512.11 4 9 0 3196 134 13:45:30 Shut-In Pressure @ 15 Minutes Shut-In Pressure @ 15 Minutes 8512.11 906 187 0 3174 135 13:50:33 Shut-In Pressure @ 20 Minutes Shut-In Pressure @ 20 Minutes 8512.11 76 79 0 3153 136 13:55:25 Shut-In Pressure @ 25 Minutes Shut-In Pressure @ 25 Minutes 8512.11 59 68 0 3132 137 14:00:15 Shut-In Pressure @ 30 Minutes Shut-In Pressure @ 30 Minutes 8512.11 12 23 0 3110 Event Log 4.20.25 Conoco Phillips - 3S-602 Event Log 4.20 179 Seq No. Time Activity Code Comment Job Slurry Vol Treating Pressure Treating Pressure @Pump Slurry Rate Tubing Gauge BH Pres 1 06:10:29 (04/21/25) Start Job Starting Job 0 0 0 0 0 1 06:10:29 (04/21/25) Next Treatment Treatment Interval 1 0 0 0 0 0 2 6:29:42 Pre-Job Safety Meeting Pre-Job Safety Meeting 0 -17 -7 0 2152 3 7:08:02 Other Loop Test 0 -18 -3 0 2150 18 07:11:42 (04/21/25) Next Treatment Treatment Interval 18 0 -17 0 0 2150 4 7:17:25 Prime Pumps Prime Pumps 0 152 218 0 2149 5 7:29:17 Pressure Test ePRV - Primary Tubing 0 698 715 0 2149 6 7:30:50 Pressure Test ePRV - Primary IA 0 690 711 0 2149 7 7:33:26 Pressure Test ePRV - Secondary Tubing 0 732 747 0 2149 8 7:35:39 Pressure Test ePRV - Secondary IA 0 758 723 0 2149 9 7:37:33 Pressure Test Pressure Test - Global 0 760 188 0 2148 10 7:37:40 Pressure Test Pressure Test - Locals 0 760 222 0 2148 11 7:44:44 Pressure Test Pressure Test - Max 0 9415 9438 0 2148 12 7:49:48 Pressure Test Pressure Test - Pass 0 9396 9131 0 2148 13 8:17:53 Open Well Open Well 0 340 314 0 2118 14 8:20:05 Drop Ball Drop Ball for Interval 18 21.09 1290 1395 15 2874 15 8:29:20 Ball on Seat Ball for Interval 18 on Seat 163.06 1554 1715 15.3 3010 16 8:29:27 Break Formation Break Formation 164.85 2977 3202 15.3 4379 17 8:30:59 Alarm Delta Stage At Top Perf = 4 191.38 2433 2604 24.2 3653 18 8:32:05 Alarm Delta Stage At Top Perf = 5 224.95 2727 2877 36.4 3856 19 8:32:58 Other 1st Tracer Drop 257.64 2783 2922 37.1 4063 20 8:33:40 Alarm Delta Stage At Top Perf = 6 283.53 2838 2965 37 4111 21 8:35:30 Alarm Delta Stage At Top Perf = 7 351.43 2717 2869 37.1 3939 22 8:42:46 Other 2nd Tracer Drop 619.51 2703 2921 36.5 4017 23 8:43:18 Alarm Delta Stage At Top Perf = 8 638.98 2694 2905 36.5 4022 24 8:44:14 Alarm Delta Stage At Top Perf = 9 673.07 2675 2894 36.5 4041 25 8:45:22 Alarm Delta Stage At Top Perf = 10 714.47 2707 2951 36.5 4098 26 8:47:25 Alarm Delta Stage At Top Perf = 11 789.85 2853 3082 36.9 4237 27 8:50:02 Alarm Delta Stage At Top Perf = 12 886.42 2919 3153 36.9 4316 28 8:52:47 Alarm Delta Stage At Top Perf = 13 987.79 2979 3225 36.8 4379 29 8:55:48 Alarm Delta Stage At Top Perf = 14 1098.82 3065 3310 36.8 4454 30 8:58:53 Alarm Delta Stage At Top Perf = 15 1212.16 3166 3422 36.7 4529 31 9:00:37 Other 3rd Tracer Drop 1275.67 3265 3525 36.6 4581 32 9:02:14 Alarm Delta Stage At Top Perf = 16 1335.38 3398 3594 37.4 4661 33 9:03:21 Drop Ball Drop Ball For Interval 19 1376.38 3440 3614 37 4670 19 09:03:22 (04/21/25) Next Treatment Treatment Interval 19 1377.62 3443 3618 37 4667 34 9:04:08 Other 1st Tracer Drop 1405.96 3492 3642 36.9 4705 35 9:04:21 Alarm Delta Stage At Top Perf = 17 1413.96 3491 3641 36.9 4709 36 9:08:13 Alarm Delta Stage At Top Perf = 18 1509.45 2254 2473 15.1 3677 37 9:08:33 Ball on Seat Ball for Interval 19 on Seat 1514.23 2275 2508 15.1 3684 38 9:08:38 Break Formation Break Formation 1515.75 4572 4881 15.1 6010 39 9:10:44 Alarm Delta Stage At Top Perf = 1 1562.45 2937 3113 36.1 3910 40 9:12:43 Alarm Delta Stage At Top Perf = 2 1636.17 2739 2890 37.3 3942 41 9:19:06 Other 2nd Tracer Drop 1873.63 2554 2754 36.9 3863 42 9:20:14 Alarm Delta Stage At Top Perf = 3 1915.39 2510 2736 36.8 3871 43 9:21:10 Alarm Delta Stage At Top Perf = 4 1949.76 2510 2745 36.8 3901 44 9:22:24 Alarm Delta Stage At Top Perf = 5 1995.1 2534 2779 36.8 3932 45 9:24:27 Alarm Delta Stage At Top Perf = 6 2070.76 2672 2919 37 4059 46 9:27:02 Alarm Delta Stage At Top Perf = 7 2166.2 2835 3077 36.9 4197 47 9:29:47 Alarm Delta Stage At Top Perf = 8 2267.58 2901 3131 36.8 4278 48 9:32:50 Alarm Delta Stage At Top Perf = 9 2379.94 2880 3138 36.8 4285 49 9:35:55 Alarm Delta Stage At Top Perf = 10 2493.43 2889 3152 36.8 4303 50 9:36:15 Other 3rd Tracer Drop 2505.08 2888 3160 36.8 4299 51 9:39:14 Alarm Delta Stage At Top Perf = 11 2616 3022 3191 37.5 4356 52 9:40:05 Drop Ball Drop Ball for Interval 20 2647.06 3074 3241 37.1 4359 20 09:40:11 (04/21/25) Next Treatment Treatment Interval 20 2651.39 3084 3256 37.1 4364 53 9:41:09 Alarm Delta Stage At Top Perf = 12 2687.19 3105 3284 37 4404 54 9:41:38 Other 1st Tracer Drop 2704.48 3110 3270 37 4353 55 9:45:02 Alarm Delta Stage At Top Perf = 13 2774.82 2235 2471 15.1 3639 56 9:45:21 Ball on Seat Ball For Interval 20 on Seat 2779.36 2269 2505 15.2 3649 57 9:45:26 Break Formation Break Formation 2780.88 5045 5173 15.2 6073 58 9:47:29 Alarm Delta Stage At Top Perf = 1 2828.52 2916 3083 36.7 3920 59 9:49:25 Alarm Delta Stage At Top Perf = 2 2900.55 2820 2980 37.3 4039 60 9:57:03 Alarm Delta Stage At Top Perf = 3 3184.4 2645 2863 36.8 3977 61 9:57:58 Alarm Delta Stage At Top Perf = 4 3218.17 2605 2830 36.8 3954 62 9:59:13 Alarm Delta Stage At Top Perf = 5 3264.22 2566 2790 36.8 3961 63 10:01:16 Alarm Delta Stage At Top Perf = 6 3339.67 2590 2824 36.8 4028 64 10:03:54 Alarm Delta Stage At Top Perf = 7 3436.77 2634 2865 37.1 4073 65 10:06:35 Alarm Delta Stage At Top Perf = 8 3536.41 2667 2901 37.1 4110 66 10:09:36 Alarm Delta Stage At Top Perf = 9 3648.31 2686 2933 37.1 4130 67 10:12:35 Alarm Delta Stage At Top Perf = 10 3758.83 2720 2972 37 4156 68 10:13:59 Other 3rd Tracer Drop 3810.65 2756 3016 37 4168 69 10:15:55 Alarm Delta Stage At Top Perf = 11 3882.54 2846 3045 37.7 4223 70 10:17:03 Drop Ball Drop Ball For Interval 21 3925.07 2904 3067 37.2 4190 21 10:17:07 (04/21/25) Next Treatment Treatment Interval 21 3927.55 2908 3080 37.2 4194 71 10:17:39 Alarm Delta Stage At Top Perf = 12 3947.38 2943 3106 37.1 4223 72 10:18:12 Other 1st Tracer Drop 3967.81 2971 3130 37.2 4240 73 10:21:43 Alarm Delta Stage At Top Perf = 13 4044.34 1996 2232 15.2 3511 74 10:21:47 Ball on Seat Ball for Interval 21 on Seat 4045.1 1999 2235 15.2 3512 75 10:21:53 Break Formation Break Formation 4046.62 4657 4818 15.2 6053 76 10:24:01 Alarm Delta Stage At Top Perf = 1 4097.18 2537 2676 37.2 3553 77 10:25:52 Alarm Delta Stage At Top Perf = 2 4166.29 2519 2694 37.4 3711 78 10:33:35 Alarm Delta Stage At Top Perf = 3 4453.62 2307 2502 36.9 3653 79 10:34:29 Alarm Delta Stage At Top Perf = 4 4486.81 2254 2475 36.8 3641 80 10:35:43 Alarm Delta Stage At Top Perf = 5 4532.22 2262 2510 36.8 3677 81 10:36:17 Other 2nd Tracer Drop 4552.47 2270 2533 36.8 3677 82 10:37:21 Alarm Delta Stage At Top Perf = 6 4592.47 2345 2605 37.1 3738 83 10:39:55 Alarm Delta Stage At Top Perf = 7 4687.45 2416 2681 37 3811 84 10:42:36 Alarm Delta Stage At Top Perf = 8 4786.66 2462 2743 37 3859 85 10:45:38 Alarm Delta Stage At Top Perf = 9 4899.13 2525 2800 37 3900 86 10:48:41 Alarm Delta Stage At Top Perf = 10 5012.01 2613 2916 36.9 3956 87 10:50:40 Other 3rd Tracer Drop 5084.62 2676 2969 36.9 3969 88 10:52:01 Alarm Delta Stage At Top Perf = 11 5135.05 2730 3018 37 4021 89 10:54:07 Drop Ball Drop Ball for Interval 22 5212.81 2806 2996 37.3 4048 22 10:54:07 (04/21/25) Next Treatment Treatment Interval 22 5212.81 2806 2996 37.3 4048 90 10:54:09 Alarm Delta Stage At Top Perf = 12 5214.67 2808 2999 37.3 4042 91 10:54:53 Other 1st Tracer Drop 5241.36 2834 2999 37.2 4047 92 10:58:25 Alarm Delta Stage At Top Perf = 13 5322.69 2051 2288 15.1 3490 93 10:58:45 Ball on Seat Ball For Interval 22 on Seat 5327.49 2069 2320 15.1 3500 94 10:58:50 Break Formation Break Formation 5329.01 4758 4895 15.1 5876 95 11:00:59 Alarm Delta Stage At Top Perf = 1 5374.55 2589 2781 36.7 3572 96 11:02:55 Alarm Delta Stage At Top Perf = 2 5446.63 2408 2587 37.3 3616 97 11:10:25 Other 2nd Tracer Drop 5725.58 2236 2459 37 3559 98 11:10:39 Alarm Delta Stage At Top Perf = 3 5734.82 2233 2452 36.9 3557 99 11:11:36 Alarm Delta Stage At Top Perf = 4 5769.89 2194 2440 36.9 3562 100 11:12:49 Alarm Delta Stage At Top Perf = 5 5814.86 2199 2431 37.1 3589 101 11:14:52 Alarm Delta Stage At Top Perf = 6 5890.86 2200 2466 37 3629 102 11:17:23 Alarm Delta Stage At Top Perf = 7 5984 2220 2478 37 3651 103 11:20:06 Alarm Delta Stage At Top Perf = 8 6084.47 2270 2521 37.1 3693 104 11:23:09 Alarm Delta Stage At Top Perf = 9 6197.58 2305 2570 37.1 3726 105 11:24:08 Other Bin Swap 6233.4 2292 2583 37 3725 106 11:26:11 Alarm Delta Stage At Top Perf = 10 6310.11 2355 2631 37.1 3753 107 11:26:57 Other 3rd Tracer Drop 6337.9 2347 2620 37 3756 108 11:29:29 Alarm Delta Stage At Top Perf = 11 6432.29 2348 2625 36.9 3748 109 11:31:35 Drop Ball Drop Ball for Interval 23 6509.65 2544 2724 37.2 3829 23 11:31:35 (04/21/25) Next Treatment Treatment Interval 23 6510.27 2544 2724 37.2 3831 110 11:31:37 Alarm Delta Stage At Top Perf = 12 6510.89 2547 2728 37.2 3825 111 11:35:29 Alarm Delta Stage At Top Perf = 13 6612.1 1983 2215 15.1 3436 112 11:35:51 Ball on Seat Ball for Interval 23 on Seat 6617.89 2025 2263 15.1 3446 113 11:35:56 Break Formation Break Formation 6618.9 4113 4610 15.1 5315 114 11:37:42 Alarm Delta Stage At Top Perf = 1 6664.32 2485 2648 37 3525 115 11:39:48 Alarm Delta Stage At Top Perf = 2 6742.31 2321 2489 37.2 3552 116 11:47:33 Alarm Delta Stage At Top Perf = 3 7030.58 2171 2406 37 3492 117 11:48:31 Alarm Delta Stage At Top Perf = 4 7065.76 2144 2386 37 3494 118 11:49:44 Alarm Delta Stage At Top Perf = 5 7110.76 2108 2350 37 3487 119 11:51:48 Alarm Delta Stage At Top Perf = 6 7187.22 2109 2366 37.1 3509 120 11:53:41 Other 2nd Tracer Drop 7257.01 2105 2367 37 3518 121 11:54:18 Alarm Delta Stage At Top Perf = 7 7279.84 2109 2378 37 3533 122 11:57:02 Alarm Delta Stage At Top Perf = 8 7380.94 2128 2399 36.9 3550 123 12:00:05 Alarm Delta Stage At Top Perf = 9 7493.92 2161 2426 37.2 3580 124 12:03:08 Alarm Delta Stage At Top Perf = 10 7607.17 2195 2480 37.1 3596 125 12:05:02 Other 3rd Tracer Drop 7677.54 2218 2516 37 3601 126 12:06:27 Alarm Delta Stage At Top Perf = 11 7729.93 2288 2559 36.9 3622 127 12:08:44 Alarm Delta Stage At Top Perf = 12 7814.57 2479 2714 37.1 3695 128 12:11:24 ISIP ISIP 7911.07 1452 1171 0 3188 129 12:14:02 Other blowing down surface lines 7911.07 17 94 0 3164 130 12:16:26 Shut-In Pressure @ 5 Minutes Shut-In Pressure @ 5 Minutes 7911.07 416 537 0 3148 131 12:21:28 Shut-In Pressure @ 10 Minutes Shut-In Pressure @ 10 Minutes 7911.07 -19 6 0 3122 132 12:26:24 Shut-In Pressure @ 15 Minutes Shut-In Pressure @ 15 Minutes 7911.07 169 150 0 3103 133 12:31:22 Shut-In Pressure @ 20 Minutes Shut-In Pressure @ 20 Minutes 7911.07 59 77 0 3089 134 12:36:17 Shut-In Pressure @ 25 Minutes Shut-In Pressure @ 25 Minutes 7911.07 61 67 0 3078 135 12:41:20 Shut-In Pressure @ 30 Minutes Shut-In Pressure @ 30 Minutes 7911.07 40 39 0 3066 Event Log 4.21.25 Conoco Phillips - 3S-602 Event Log 4.21 180 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 6:00 6:30Test #1 (cp) -->3456 2839 2222 2592 2098 1975 1852 1901 2345 2592 2345 1975 2345 1852 1728 1481 1284 987 864 667 370 99 49 0 0 0 0 0Dial Reading140 115 90 105 85 80 75 77 95 105 95 80 95 75 70 60 52 40 35 27 15 4 2Test #2 (cp) -->0000000000000000000000000000Dial ReadingTest #3 (cp) -->0000000000000000000000000000Dial ReadingTest #4 (cp) -->0000000000000000000000000000Dial Reading110 8.95 1.00 30.00 0.60 1.00 0.25 1.75 1.75Temp 0F PH LOSURF-300D WG-36 CAT3 MO-67 CL-28M BC-140X2 OptiFlo-II OptiFlo-IIID. MartinezHydration Visc: 24 93Temperature was held at 140 degres for the duration of the testAll chemical concentrations below are in gallons per thousand / pounds per thousandWater pH: 7.02Torok Hydration pH: 7.353S-602 Stage(s): Break Test140 Water Source: CPF3ALASKA DISTRICT LABORATORY15 Minute Fann Model 35 Crosslinked Fluid ReportFluid System: Date: 4/12/2025ConocoPhillips Project No:0500100015002000250030003500400000:00 02:00 04:00 10:00 20:00 30:00 1:00 1:30 2:00 2:30 3:00 4:00 5:00 6:00Viscosity (cp)Time (min:sec)Prejob Crosslink Break Tests30# Opti II @ 1.75 and Opti III @ 1.75Fluid is broken at 200cpConoco Phillips - 3S-602Prejob Break Test181 Company:Well Name:BHST (ºF):Depth:Formation:Analyst:cp @3S-704 Stage(s): 1110 Water Source:ALASKA DISTRICT LABORATORY15 Minute Fann Model 35 Crosslinked Fluid ReportFluid System: Date: 3/19/2023ConocoPhillips Project No:Hydration Visc:Water pH: 7.18Hydration pH:0500100015002000250000:00 01:00 02:00 03:00 04:00 05:00 06:00 07:00 08:00 09:00 10:00 11:00 12:00 13:00 14:00 15:00Viscosity (cp)Time (min:sec)Zone 1 Crosslink TestsPad2 ppg4 ppg6 ppg7 ppg8 ppgFluid is broken at 200cpConoco Phillips - 3S-602Fann 15 Min Test Interval 1182 Company:Well Name:BHST (ºF):Depth:Formation:Analyst:cp @Lot Number--->Pad0.5 ppg 1 ppg 2 ppg3 ppg4 ppg0.60 1.7595 8.89 1.00 1.00 30.00 1.75 0.25Temp 0FPH LOSURF-300D CL-28M WG-36 MO-67 Optiflo-II Optiflo-III BC-140X2D. MartinezHydration Visc:All chemical concentrations below are in gallons per thousand / pounds per thousandWater pH: 7.303S-602 Stage(s): 1140 Water Source: cpf3ALASKA DISTRICT LABORATORY15 Minute Fann Model 35 Crosslinked Fluid ReportFluid System: Date: 4/13/2025ConocoPhillips Project No:05001000150020002500300035004000450000:00 01:00 02:00 03:00 04:00 05:00 06:00 07:00 08:00 09:00 10:00 11:00 12:00 13:00 14:00 15:00Viscosity (cp)Time (min:sec)Crosslink TestsPad1 ppg2 ppg3 ppg4 ppg5 ppgFluid is broken at 200cpConoco Phillips - 3S-602Zone 1183 Company:Well Name:BHST (ºF):Depth:Formation:Analyst:cp @Lot Number--->Pad0.5 ppg 1 ppg 2 ppg3 ppg4 ppg0.60 1.7595 8.80 1.00 1.00 30.00 1.75 0.25Temp 0FPH LOSURF-300D CL-28M WG-36 MO-67 Optiflo-II Optiflo-III BC-140X2D. MartinezHydration Visc:All chemical concentrations below are in gallons per thousand / pounds per thousandWater pH: 7.303S-602 Stage(s): 2140 Water Source: cpf3ALASKA DISTRICT LABORATORY15 Minute Fann Model 35 Crosslinked Fluid ReportFluid System: Date: 4/13/2025ConocoPhillips Project No:05001000150020002500300035004000450000:00 01:00 02:00 03:00 04:00 05:00 06:00 07:00 08:00 09:00 10:00 11:00 12:00 13:00 14:00 15:00Viscosity (cp)Time (min:sec)Crosslink TestsPad1 ppg2 ppg3 ppg4 ppg5 ppgFluid is broken at 200cpConoco Phillips - 3S-602Zone 2184 Company:Well Name:BHST (ºF):Depth:Formation:Analyst:cp @Lot Number--->Pad0.5 ppg 1 ppg 2 ppg3 ppg4 ppg0.60 1.7590 8.61 1.00 1.00 30.00 1.75 0.25Temp 0FPH LOSURF-300D CL-28M WG-36 MO-67 Optiflo-II Optiflo-III BC-140X2D. MartinezHydration Visc: 24 110All chemical concentrations below are in gallons per thousand / pounds per thousandWater pH: 7.45Hydration pH: 24.003S-602 Stage(s): 3140 Water Source: CPF 3ALASKA DISTRICT LABORATORY15 Minute Fann Model 35 Crosslinked Fluid ReportFluid System: Date: 4/13/2025ConocoPhillips Project No:0500100015002000250030003500400000:00 01:00 02:00 03:00 04:00 05:00 06:00 07:00 08:00 09:00 10:00 11:00 12:00 13:00 14:00 15:00Viscosity (cp)Time (min:sec)Crosslink TestsPad0.5 ppg2 ppg3 ppg4 ppg5 ppgFluid is broken at 200cpConoco Phillips - 3S-602Zone 3185 Company:Well Name:BHST (ºF):Depth:Formation:Analyst:cp @Lot Number--->Pad.50 ppg 1 ppg 2 ppg3 ppg4 ppg0.60 1.7582 8.87 1.00 1.00 30.00 1.75 0.25Temp 0F PH LOSURF-300D CL-28M WG-36 MO-67 Optiflo-II Optiflo-III BC-140X2D. MartinezHydration Visc:All chemical concentrations below are in gallons per thousand / pounds per thousandWater pH:Hydration pH:3S-602 Stage(s): 4140 Water Source: CPF3ALASKA DISTRICT LABORATORY15 Minute Fann Model 35 Crosslinked Fluid ReportFluid System: Date: 4/14/2025ConocoPhillips Project No:050010001500200025003000350040004500500000:00 01:00 02:00 03:00 04:00 05:00 06:00 07:00 08:00 09:00 10:00 11:00 12:00 13:00 14:00 15:00Viscosity (cp)Time (min:sec)Crosslink TestsPad1 ppg2 ppg3 ppg4 ppg5 ppgFluid is broken at 200cpConoco Phillips - 3S-602Zone 4 186 Company:Well Name:BHST (ºF):Depth:Formation:Analyst:cp @Lot Number--->Mini FracPad1 ppg 2 ppg3 ppg4 ppg0.60 1.7586 8.96 1.00 1.00 30.00 1.75 0.25Temp 0FPH LOSURF-300D CL-28M WG-36 MO-67 Optiflo-II Optiflo-III BC-140X2D. MartinezHydration Visc:All chemical concentrations below are in gallons per thousand / pounds per thousandWater pH: 7.23Hydration pH: 24.003S-602 Stage(s): 5140 Water Source: CPF3ALASKA DISTRICT LABORATORY15 Minute Fann Model 35 Crosslinked Fluid ReportFluid System: Date: 4/14/2025ConocoPhillips Project No:010002000300040005000600000:00 01:00 02:00 03:00 04:00 05:00 06:00 07:00 08:00 09:00 10:00 11:00 12:00 13:00 14:00 15:00Viscosity (cp)Time (min:sec)Crosslink TestsPad1 ppg2 ppg3 ppg4 ppg5 ppgFluid is broken at 200cpConoco Phillips - 3S-602Zone 5187 Company:Well Name:BHST (ºF):Depth:Formation:Analyst:cp @Lot Number--->Pad0.5 ppg 1 ppg 2 ppg3 ppg4 ppg0.60 1.7588 9.00 1.00 1.00 30.00 1.75 0.25Temp 0FPH LOSURF-300D CL-28M WG-36 MO-67 Optiflo-II Optiflo-III BC-140X2D. MartinezHydration Visc:All chemical concentrations below are in gallons per thousand / pounds per thousandWater pH:Hydration pH:3S-602 Stage(s): 6Water Source: CPF3ALASKA DISTRICT LABORATORY15 Minute Fann Model 35 Crosslinked Fluid ReportFluid System: Date: 4/14/2025ConocoPhillips Project No:010002000300040005000600000:00 01:00 02:00 03:00 04:00 05:00 06:00 07:00 08:00 09:00 10:00 11:00 12:00 13:00 14:00 15:00Viscosity (cp)Time (min:sec)Crosslink TestsPad1 ppg2 ppg3 ppg4 ppg5 ppgFluid is broken at 200cpConoco Phillips - 3S-602Zone 6 188 Company:Well Name:BHST (ºF):Depth:Formation:Analyst:cp @Lot Number--->Pad0.5 ppg 1 ppg 2 ppg3 ppg4 ppg0.60 1.7580 8.86 1.00 1.00 30.00 1.75 0.25Temp 0FPH LOSURF-300D CL-28M WG-36 MO-67 Optiflo-II Optiflo-III BC-140X2D. MartinezHydration Visc:All chemical concentrations below are in gallons per thousand / pounds per thousandWater pH:Hydration pH:3S-602 Stage(s): 7Water Source: CPF3ALASKA DISTRICT LABORATORY15 Minute Fann Model 35 Crosslinked Fluid ReportFluid System: Date: 4/14/2025ConocoPhillips Project No:050010001500200025003000350040004500500000:00 01:00 02:00 03:00 04:00 05:00 06:00 07:00 08:00 09:00 10:00 11:00 12:00 13:00 14:00 15:00Viscosity (cp)Time (min:sec)Crosslink TestsPad1 ppg2 ppg3 ppg4 ppg5 ppgFluid is broken at 200cpConoco Phillips - 3S-602Zone 7 189 Company:Well Name:BHST (ºF):Depth:Formation:Analyst:cp @Lot Number--->Pad0.5 ppg 1 ppg 2 ppg3 ppg4 ppg0.60 1.7591 8.81 1.00 1.00 30.00 1.75 0.25Temp 0FPH LOSURF-300D CL-28M WG-36 MO-67 Optiflo-II Optiflo-III BC-140X2D. ,MartinezHydration Visc:All chemical concentrations below are in gallons per thousand / pounds per thousandWater pH:Hydration pH:3S-602 Stage(s): 8Water Source: CPF3ALASKA DISTRICT LABORATORY15 Minute Fann Model 35 Crosslinked Fluid ReportFluid System: Date: 4/15/2025ConocoPhillips Project No:010002000300040005000600000:00 01:00 02:00 03:00 04:00 05:00 06:00 07:00 08:00 09:00 10:00 11:00 12:00 13:00 14:00 15:00Viscosity (cp)Time (min:sec)Crosslink TestsPad1 ppg2 ppg3 ppg4 ppg5 ppgFluid is broken at 200cpConoco Phillips - 3S-602Zone 8190 Company:Well Name:BHST (ºF):Depth:Formation:Analyst:cp @Lot Number--->Pad0.5 ppg 1 ppg 2 ppg3 ppg4 ppg0.60 1.7594 8.80 1.00 1.00 30.00 1.75 0.25Temp 0FPH LOSURF-300D CL-28M WG-36 MO-67 Optiflo-II Optiflo-III BC-140X2D. ,MartinezHydration Visc:All chemical concentrations below are in gallons per thousand / pounds per thousandWater pH:Hydration pH:3S-602 Stage(s): 9Water Source: CPF3ALASKA DISTRICT LABORATORY15 Minute Fann Model 35 Crosslinked Fluid ReportFluid System: Date:ConocoPhillips Project No:010002000300040005000600000:00 01:00 02:00 03:00 04:00 05:00 06:00 07:00 08:00 09:00 10:00 11:00 12:00 13:00 14:00 15:00Viscosity (cp)Time (min:sec)Crosslink TestsPad1 ppg2 ppg3 ppg4 ppg5 ppgFluid is broken at 200cpConoco Phillips - 3S-602Zone 9191 Company:Well Name:BHST (ºF):Depth:Formation:Analyst:cp @Lot Number--->Pad0.5 ppg 1 ppg 2 ppg3 ppg4 ppg0.60 1.7589 8.93 1.00 1.00 30.00 1.75 0.25Temp 0FPH LOSURF-300D CL-28M WG-36 MO-67 Optiflo-II Optiflo-III BC-140X2D. ,MartinezHydration Visc:All chemical concentrations below are in gallons per thousand / pounds per thousandWater pH:Hydration pH:3S-602 Stage(s): 10Water Source: CPF3ALASKA DISTRICT LABORATORY15 Minute Fann Model 35 Crosslinked Fluid ReportFluid System: Date: 4/15/2025ConocoPhillips Project No:0500100015002000250030003500400000:00 01:00 02:00 03:00 04:00 05:00 06:00 07:00 08:00 09:00 10:00 11:00 12:00 13:00 14:00 15:00Viscosity (cp)Time (min:sec)Crosslink TestsPad1 ppg2 ppg3 ppg4 ppg5 ppgFluid is broken at 200cpConoco Phillips - 3S-602Zone 10192 Company:Well Name:BHST (ºF):Depth:Formation:Analyst:cp @Lot Number--->Pad0.5 ppg 1 ppg 2 ppg3 ppg4 ppg0.60 1.7590 8.87 1.00 1.00 30.00 1.75 0.25Temp 0FPH LOSURF-300D CL-28M WG-36 MO-67 Optiflo-II Optiflo-III BC-140X2D. ,MartinezHydration Visc:All chemical concentrations below are in gallons per thousand / pounds per thousandWater pH:Hydration pH:3S-602 Stage(s): 11Water Source: CPF3ALASKA DISTRICT LABORATORY15 Minute Fann Model 35 Crosslinked Fluid ReportFluid System: Date: 4/15/2025ConocoPhillips Project No:05001000150020002500300035004000450000:00 01:00 02:00 03:00 04:00 05:00 06:00 07:00 08:00 09:00 10:00 11:00 12:00 13:00 14:00 15:00Viscosity (cp)Time (min:sec)Crosslink TestsPad1 ppg2 ppg3 ppg4 ppg5 ppgFluid is broken at 200cpConoco Phillips - 3S-602Zone 11193 Company:Well Name:BHST (ºF):Depth:Formation:Analyst:cp @Lot Number--->Pad0.5 ppg 1 ppg 2 ppg3 ppg4 ppg0.60 1.7591 8.88 1.00 1.00 30.00 1.75 0.25Temp 0FPH LOSURF-300D CL-28M WG-36 MO-67 Optiflo-II Optiflo-III BC-140X2D. ,MartinezHydration Visc:All chemical concentrations below are in gallons per thousand / pounds per thousandWater pH:Hydration pH:3S-602 Stage(s): 12Water Source: CPF3ALASKA DISTRICT LABORATORY15 Minute Fann Model 35 Crosslinked Fluid ReportFluid System: Date: 4/15/2025ConocoPhillips Project No:0500100015002000250030003500400000:00 01:00 02:00 03:00 04:00 05:00 06:00 07:00 08:00 09:00 10:00 11:00 12:00 13:00 14:00 15:00Viscosity (cp)Time (min:sec)Crosslink TestsPad1 ppg2 ppg3 ppg4 ppg5 ppgFluid is broken at 200cpConoco Phillips - 3S-602Zone 12194 Company:Well Name:BHST (ºF):Depth:Formation:Analyst:cp @Lot Number--->Pad0.5 ppg 1 ppg 2 ppg3 ppg4 ppg0.60 1.7593 8.90 1.00 1.00 30.00 1.75 0.25Temp 0FPH LOSURF-300D CL-28M WG-36 MO-67 Optiflo-II Optiflo-III BC-140X2D. ,MartinezHydration Visc:All chemical concentrations below are in gallons per thousand / pounds per thousandWater pH:Hydration pH:3S-602 Stage(s): 13Water Source: CPF3ALASKA DISTRICT LABORATORY15 Minute Fann Model 35 Crosslinked Fluid ReportFluid System: Date: 4/20/2025ConocoPhillips Project No:0100020003000400050006000700000:00 01:00 02:00 03:00 04:00 05:00 06:00 07:00 08:00 09:00 10:00 11:00 12:00 13:00 14:00 15:00Viscosity (cp)Time (min:sec)Crosslink TestsPad1 ppg2 ppg3 ppg4 ppg5 ppgFluid is broken at 200cpConoco Phillips - 3S-602Zone 13195 Company:Well Name:BHST (ºF):Depth:Formation:Analyst:cp @Lot Number--->Pad0.5 ppg 1 ppg 2 ppg3 ppg4 ppg0.60 1.7586 8.93 1.00 1.00 30.00 1.75 0.25Temp 0FPH LOSURF-300D CL-28M WG-36 MO-67 Optiflo-II Optiflo-III BC-140X2D. ,MartinezHydration Visc:All chemical concentrations below are in gallons per thousand / pounds per thousandWater pH:Hydration pH:3S-602 Stage(s): 14Water Source: CPF3ALASKA DISTRICT LABORATORY15 Minute Fann Model 35 Crosslinked Fluid ReportFluid System: Date: 4/20/2025ConocoPhillips Project No:010002000300040005000600000:00 01:00 02:00 03:00 04:00 05:00 06:00 07:00 08:00 09:00 10:00 11:00 12:00 13:00 14:00 15:00Viscosity (cp)Time (min:sec)Crosslink TestsPad1 ppg2 ppg3 ppg4 ppg5 ppgFluid is broken at 200cpConoco Phillips - 3S-602Zone 14196 Company:Well Name:BHST (ºF):Depth:Formation:Analyst:cp @Lot Number--->Pad0.5 ppg 1 ppg 2 ppg3 ppg4 ppg0.60 1.7596 8.88 1.00 1.00 30.00 1.75 0.25Temp 0FPH LOSURF-300D CL-28M WG-36 MO-67 Optiflo-II Optiflo-III BC-140X2D. ,MartinezHydration Visc:All chemical concentrations below are in gallons per thousand / pounds per thousandWater pH:Hydration pH:3S-602 Stage(s): 15Water Source: CPF3ALASKA DISTRICT LABORATORY15 Minute Fann Model 35 Crosslinked Fluid ReportFluid System: Date: 4/20/2025ConocoPhillips Project No:050010001500200025003000350040004500500000:00 01:00 02:00 03:00 04:00 05:00 06:00 07:00 08:00 09:00 10:00 11:00 12:00 13:00 14:00 15:00Viscosity (cp)Time (min:sec)Crosslink TestsPad1 ppg2 ppg3 ppg4 ppg5 ppgFluid is broken at 200cpConoco Phillips - 3S-602Zone 15197 Company:Well Name:BHST (ºF):Depth:Formation:Analyst:cp @Lot Number--->Pad0.5 ppg 1 ppg 2 ppg3 ppg4 ppg0.60 1.7594 8.86 1.00 1.00 30.00 1.75 0.25Temp 0FPH LOSURF-300D CL-28M WG-36 MO-67 Optiflo-II Optiflo-III BC-140X2D. ,MartinezHydration Visc:All chemical concentrations below are in gallons per thousand / pounds per thousandWater pH:Hydration pH:3S-602 Stage(s): 16Water Source: CPF3ALASKA DISTRICT LABORATORY15 Minute Fann Model 35 Crosslinked Fluid ReportFluid System: Date: 4/20/2025ConocoPhillips Project No:010002000300040005000600000:00 01:00 02:00 03:00 04:00 05:00 06:00 07:00 08:00 09:00 10:00 11:00 12:00 13:00 14:00 15:00Viscosity (cp)Time (min:sec)Crosslink TestsPad1 ppg2 ppg3 ppg4 ppg5 ppgFluid is broken at 200cpConoco Phillips - 3S-602Zone 16198 Company:Well Name:BHST (ºF):Depth:Formation:Analyst:cp @Lot Number--->Pad0.5 ppg 1 ppg 2 ppg3 ppg4 ppg0.60 1.7597 8.85 1.00 1.00 30.00 1.75 0.25Temp 0FPH LOSURF-300D CL-28M WG-36 MO-67 Optiflo-II Optiflo-III BC-140X2D. ,MartinezHydration Visc:All chemical concentrations below are in gallons per thousand / pounds per thousandWater pH:Hydration pH:3S-602 Stage(s): 17Water Source: CPF3ALASKA DISTRICT LABORATORY15 Minute Fann Model 35 Crosslinked Fluid ReportFluid System: Date: 4/20/2025ConocoPhillips Project No:05001000150020002500300000:00 01:00 02:00 03:00 04:00 05:00 06:00 07:00 08:00 09:00 10:00 11:00 12:00 13:00 14:00 15:00Viscosity (cp)Time (min:sec)Crosslink TestsPad1 ppg2 ppg3 ppg4 ppg5 ppgFluid is broken at 200cpConoco Phillips - 3S-602Zone 17199 Company:Well Name:BHST (ºF):Depth:Formation:Analyst:cp @Lot Number--->Pad0.5 ppg 1 ppg 2 ppg3 ppg4 ppg0.60 1.7595 8.89 1.00 1.00 30.00 1.75 0.25Temp 0FPH LOSURF-300D CL-28M WG-36 MO-67 Optiflo-II Optiflo-III BC-140X2D. ,MartinezHydration Visc:All chemical concentrations below are in gallons per thousand / pounds per thousandWater pH:Hydration pH:3S-602 Stage(s): 18Water Source: CPF3ALASKA DISTRICT LABORATORY15 Minute Fann Model 35 Crosslinked Fluid ReportFluid System: Date: 4/21/2025ConocoPhillips Project No:050010001500200025003000350040004500500000:00 01:00 02:00 03:00 04:00 05:00 06:00 07:00 08:00 09:00 10:00 11:00 12:00 13:00 14:00 15:00Viscosity (cp)Time (min:sec)Crosslink TestsPad1 ppg2 ppg3 ppg4 ppg5 ppgFluid is broken at 200cpConoco Phillips - 3S-602Zone 18200 Company:Well Name:BHST (ºF):Depth:Formation:Analyst:cp @Lot Number--->Pad0.5 ppg 1 ppg 2 ppg3 ppg4 ppg0.60 1.7587 8.85 1.00 1.00 30.00 1.75 0.25Temp 0FPH LOSURF-300D CL-28M WG-36 MO-67 Optiflo-II Optiflo-III BC-140X2D. ,MartinezHydration Visc:All chemical concentrations below are in gallons per thousand / pounds per thousandWater pH:Hydration pH:3S-602 Stage(s): 19Water Source: CPF3ALASKA DISTRICT LABORATORY15 Minute Fann Model 35 Crosslinked Fluid ReportFluid System: Date: 4/21/2025ConocoPhillips Project No:05001000150020002500300035004000450000:00 01:00 02:00 03:00 04:00 05:00 06:00 07:00 08:00 09:00 10:00 11:00 12:00 13:00 14:00 15:00Viscosity (cp)Time (min:sec)Crosslink TestsPad1 ppg2 ppg3 ppg4 ppg5 ppgFluid is broken at 200cpConoco Phillips - 3S-602Zone 19201 Company:Well Name:BHST (ºF):Depth:Formation:Analyst:cp @Lot Number--->Pad0.5 ppg 1 ppg 2 ppg3 ppg4 ppg0.60 1.7597 8.85 1.00 1.00 30.00 1.75 0.25Temp 0FPH LOSURF-300D CL-28M WG-36 MO-67 Optiflo-II Optiflo-III BC-140X2D. ,MartinezHydration Visc:All chemical concentrations below are in gallons per thousand / pounds per thousandWater pH:Hydration pH:3S-602 Stage(s): 20Water Source: CPF3ALASKA DISTRICT LABORATORY15 Minute Fann Model 35 Crosslinked Fluid ReportFluid System: Date: 4/21/2025ConocoPhillips Project No:050010001500200025003000350000:00 01:00 02:00 03:00 04:00 05:00 06:00 07:00 08:00 09:00 10:00 11:00 12:00 13:00 14:00 15:00Viscosity (cp)Time (min:sec)Crosslink TestsPad1 ppg2 ppg3 ppg4 ppg5 ppgFluid is broken at 200cpConoco Phillips - 3S-602Zone 20202 Company:Well Name:BHST (ºF):Depth:Formation:Analyst:cp @Lot Number--->Pad0.5 ppg 1 ppg 2 ppg3 ppg4 ppg0.60 1.7589 8.85 1.00 1.00 30.00 1.75 0.25Temp 0FPH LOSURF-300D CL-28M WG-36 MO-67 Optiflo-II Optiflo-III BC-140X2D. ,MartinezHydration Visc:All chemical concentrations below are in gallons per thousand / pounds per thousandWater pH:Hydration pH:3S-602 Stage(s): 21Water Source: CPF3ALASKA DISTRICT LABORATORY15 Minute Fann Model 35 Crosslinked Fluid ReportFluid System: Date: 4/21/2025ConocoPhillips Project No:050010001500200025003000350000:00 01:00 02:00 03:00 04:00 05:00 06:00 07:00 08:00 09:00 10:00 11:00 12:00 13:00 14:00 15:00Viscosity (cp)Time (min:sec)Crosslink TestsPad1 ppg2 ppg3 ppg4 ppg5 ppgFluid is broken at 200cpConoco Phillips - 3S-602Zone 21203 Company:Well Name:BHST (ºF):Depth:Formation:Analyst:cp @Lot Number--->Pad0.5 ppg 1 ppg 2 ppg3 ppg4 ppg0.60 1.7585 8.85 1.00 1.00 30.00 1.75 0.25Temp 0FPH LOSURF-300D CL-28M WG-36 MO-67 Optiflo-II Optiflo-III BC-140X2D. ,MartinezHydration Visc:All chemical concentrations below are in gallons per thousand / pounds per thousandWater pH:Hydration pH:3S-602 Stage(s): 22Water Source: CPF3ALASKA DISTRICT LABORATORY15 Minute Fann Model 35 Crosslinked Fluid ReportFluid System: Date: 4/21/2025ConocoPhillips Project No:050010001500200025003000350000:00 01:00 02:00 03:00 04:00 05:00 06:00 07:00 08:00 09:00 10:00 11:00 12:00 13:00 14:00 15:00Viscosity (cp)Time (min:sec)Crosslink TestsPad1 ppg2 ppg3 ppg4 ppg5 ppgFluid is broken at 200cpConoco Phillips - 3S-602Zone 22204 Company:Well Name:BHST (ºF):Depth:Formation:Analyst:cp @Lot Number--->Pad0.5 ppg 1 ppg 2 ppg3 ppg4 ppg0.60 1.7599 8.85 1.00 1.00 30.00 1.75 0.25Temp 0FPH LOSURF-300D CL-28M WG-36 MO-67 Optiflo-II Optiflo-III BC-140X2D. ,MartinezHydration Visc:All chemical concentrations below are in gallons per thousand / pounds per thousandWater pH:Hydration pH:3S-602 Stage(s): 23Water Source: CPF3ALASKA DISTRICT LABORATORY15 Minute Fann Model 35 Crosslinked Fluid ReportFluid System: Date: 4/21/2025ConocoPhillips Project No:050010001500200025003000350000:00 01:00 02:00 03:00 04:00 05:00 06:00 07:00 08:00 09:00 10:00 11:00 12:00 13:00 14:00 15:00Viscosity (cp)Time (min:sec)Crosslink TestsPad1 ppg2 ppg3 ppg4 ppg5 ppgFluid is broken at 200cpConoco Phillips - 3S-602Zone 23205 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% 16 341.1 348.1 7 7.0% 18 303.3 393.1 89.8 89.8% 20 297.5 301.3 3.8 3.8% 25 419.4 419.4 0 0.0% 30 281.5 281.5 0 0.0% 40 407.6 407.6 0 0.0% Pan 306.6 306.6 0 0.0% 0.00% <1.0% Total: 100.6 101% 93.60% >/= 90% Sample: 16 / 20 - 4/12/2025 Conoco Phillips 3S-602 16/20 Proppant 4/12/2025 Ceramic Proppant Sieves Conoco Phillips - 3S-602 Sand Sieve Analysis 206 Hydraulic Fracturing Fluid Product Component Information Disclosure 2025-04-13 Alaska HARRISON BAY 50-103-20906-00-00 CONOCOPHILLIPS 3S 602 -150.19497221 70.39430569 NAD83 none Oil 5200 1525053.05 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 SEAWATER (SG 8.52) Operator Base Fluid Density = 8.52 BC-140 X2 Halliburton Initiator BE-6(TM) Bactericide Halliburton Microbiocide 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%72.06971%12993452 Corundum 1302-74-5 60.00%13.92323%2510220 Mullite 1302-93-8 40.00%9.28215%1673480 Sodium chloride 7647-14-5 5.00%3.79314%683866 Crystalline silica, quartz 14808-60-7 100.00%0.38924%70177 Guar gum 9000-30-0 100.00%0.27255%49138 Water 7732-18-5 100.00%0.11656%21015 Borate salts Proprietary 60.00%0.05621%10135 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%0.04224%7616 Ammonium persulfate 7727-54-0 100.00%0.03217%5800 Monoethanolamine borate 26038-87-9 100.00%0.02113%3810 Oxyalkylated nonyl phenolic resin Proprietary 30.00%0.02112%3808 Halliburton Denise Tuck Denise.Tuck @Halliburton. com 281-871-6226 Heavy aromatic petroleum naphtha 64742-94-5 30.00%0.02112%3808 Sodium hydroxide 1310-73-2 30.00%0.01595%2876 Oxylated phenolic resin Proprietary 30.00%0.00965%1740 Halliburton Denise Tuck Denise.Tuck @Halliburton. com 281-871-6226 Oxyalkylated phenolic resin Proprietary 10.00%0.00704%1270 Halliburton Denise Tuck Denise.Tuck @Halliburton. com 281-871-6226 Ethylene glycol 107-21-1 30.00%0.00634%1143 Potassium chloride 7447-40-7 5.00%0.00468%845 Inorganic mineral 1317-65-3 5.00%0.00468%845 Poly(oxy-1,2-ethanediyl), alpha-(4- nonylphenyl)-omega-hydroxy-, branched 127087-87-0 5.00%0.00352%635 Naphthalene 91-20-3 5.00%0.00352%635 Flow Insurance Copper Proprietary 100.00%0.00245%442 Patina Energy Product Stewardship test@patinae nergy.com 7205324886 2-Bromo-2-nitro-1,3-propanediol 52-51-7 100.00%0.00141%255 Inorganic mineral Proprietary 1.00%0.00094%169 Halliburton Denise Tuck Denise.Tuck @Halliburton. com 281-871-6226 Polymer Proprietary 1.00%0.00094%169 Halliburton Denise Tuck Denise.Tuck @Halliburton. com 281-871-6226 Gluteraldehyde 111-30-8 1.00%0.00094%169 Calcium magnesium carbonate 16389-88-1 1.00%0.00094%169 Glycol Ether Proprietary 85.00%0.00087%157 ResMetrics Product Stewardship info@resmetri cs.com 8325921900 1,2,4 Trimethylbenzene 95-63-6 1.00%0.00070%127 Sodium chloride 7647-14-5 1.00%0.00053%96 Confidential Proprietary 20.00%0.00031%56 ResMetrics Product Stewardship info@resmetri cs.com 8325921900 Ethylene Glycol 107-21-1 20.00%0.00021%39 C.I. pigment Orange 5 3468-63-1 1.00%0.00016%29 Methanesulfonic acid, 1-hydroxy-, sodium salt 870-72-4 0.10%0.00009%17 Sodium bisulfate 7681-38-1 0.10%0.00009%17 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 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 Magensium chloride 7786-30-3 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 directed 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: Page 1/1 3S-602 Report Printed: 5/13/2025 Daily STIM Report ORIG SPUD DATE: [ 2/26/2025 ] DRLG RIG RELEASE: [ 3/24/2025 ] ON PRODUCTION: [ ] DAYS FROM SPUD: [ 44.02 ] REPORT # [ 1] REPORT DATE: [ 4/11/2025] API / UWI 5010320906 Original KB/RT Elevation (ft) 67.70 Ground Elevation (ft) 27.70 Original Spud Date 2/26/2025 Primary Job Type INITIAL COMPLETION Secondary Job Type Total AFE (Cost) 8,443,262.00 AFE / RFE / Maint.# GKA.00108.E.W001.CO.I W;GKA.00108.E.W001.C O.IS;GKA.00108.E.W001. CO.IF Network/Order Number 10463819;10441038;104 63818 AFE+Supp Amt (Cost) 8,443,262.00 Daily Cost Total (Cost) 7,872.00 Cumulative Cost (Cost) 7,872.00 Weather Temperature (°F) Road Condition Wind Last 24hr Summary PRESSURE TEST TREE PRE-FRAC TO 9850 *PASS* (JOB COMPLETE) 24hr Forecast General Remarks INT T/I/O = 0/100/0 END T/I/O = 0/100/0 ZX Code ZX03 General Pumping (Load Well / Freeze Protect / Contact Name Title Mobile Time Log Start Time End Time Dur (hr) Phase Activity Code Time P- T-X Operation 06:00 07:30 1.50 COMPZN, STIM TRAV P LOAD AND TRAV TO LOC 07:30 11:30 4.00 COMPZN, STIM WOCP P WAIT FOR WELL SUPERVISOR, ATTEMP TO CONTACT HARDLINE. WAIT FOR HARDLINE PARTS. SWAP UNIT TO 10K CAPABLE 11:30 12:00 0.50 COMPZN, STIM TRAV P RU HARDLINE TO PT FRAC TREE 12:00 12:45 0.75 COMPZN, STIM RURD P PRESSURE UP LINES AND TREE to 9850psi *PASS* 12:45 13:30 0.75 COMPZN, STIM RURD P RDMO, WSR, PJSM, CONTACT DSO. SWAP UNIT BACK TO 5K 13:30 14:00 0.50 COMPZN, STIM TRAV P TRAV FROM LOC Report Fluids Summary Fluid To well (bbl) Cum to Well (bbl) DIESEL 1.0 1.0 Contractor Rig Name/# Rig Supervisor Rig Accept Date RR Date Rig Type LRS 74-H BURKETT, CHAD,Wells Supervisor 4/11/2025 06:00 4/11/2025 14:00 PUMPING HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/11/2025 14:00 4/11/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/12/2025 00:00 4/12/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/13/2025 00:00 4/13/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/14/2025 00:00 4/14/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/15/2025 00:00 4/15/2025 15:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/16/2025 00:00 4/16/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/17/2025 00:00 4/17/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/18/2025 00:00 4/18/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/19/2025 00:00 4/19/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/20/2025 00:00 4/20/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/21/2025 00:00 4/21/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/22/2025 00:00 4/22/2025 12:00 FRAC Offline Activities Type Subtype Des Start Date End Date FRAC FRAC EQUIP FRAC RELOAD ACTIVITIES 4/15/2025 16:00 4/16/2025 23:59 PUMPING 74-H 4/20/2025 06:00 4/21/2025 14:00 Page 1/1 3S-602 Report Printed: 5/13/2025 Daily STIM Report ORIG SPUD DATE: [ 2/26/2025 ] DRLG RIG RELEASE: [ 3/24/2025 ] ON PRODUCTION: [ ] DAYS FROM SPUD: [ 44.44 ] REPORT # [ 2] REPORT DATE: [ 4/11/2025] API / UWI 5010320906 Original KB/RT Elevation (ft) 67.70 Ground Elevation (ft) 27.70 Original Spud Date 2/26/2025 Primary Job Type INITIAL COMPLETION Secondary Job Type Total AFE (Cost) 8,443,262.00 AFE / RFE / Maint.# GKA.00108.E.W001.CO.I W;GKA.00108.E.W001.C O.IS;GKA.00108.E.W001. CO.IF Network/Order Number 10463819;10441038;104 63818 AFE+Supp Amt (Cost) 8,443,262.00 Daily Cost Total (Cost) 102,950.00 Cumulative Cost (Cost) 110,822.00 Weather Temperature (°F) Road Condition Wind Last 24hr Summary CONTINUE RIG UP 24hr Forecast General Remarks ZX Code ZX02 Fracturing Contact Name Title Mobile OSSELBURN, DEREK SL 724-494-3261 LAWSON, JACOB Supervisor 971-606-0075 YEATS, SPENCER LAUNCH TECH 403-896-8933 Time Log Start Time End Time Dur (hr) Phase Activity Code Time P- T-X Operation 14:01 23:59 9.98 COMPZN, STIM RURD P CONTINUR RIG UP OPPERATIONS. NIPPLED UP LAUNCHER STACK, RAN HARD LINE TO 3S-602 VAVE SHED, Report Fluids Summary Fluid To well (bbl) Cum to Well (bbl) DIESEL 1.0 Contractor Rig Name/# Rig Supervisor Rig Accept Date RR Date Rig Type LRS 74-H BURKETT, CHAD,Wells Supervisor 4/11/2025 06:00 4/11/2025 14:00 PUMPING HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/11/2025 14:00 4/11/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/12/2025 00:00 4/12/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/13/2025 00:00 4/13/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/14/2025 00:00 4/14/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/15/2025 00:00 4/15/2025 15:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/16/2025 00:00 4/16/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/17/2025 00:00 4/17/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/18/2025 00:00 4/18/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/19/2025 00:00 4/19/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/20/2025 00:00 4/20/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/21/2025 00:00 4/21/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/22/2025 00:00 4/22/2025 12:00 FRAC Offline Activities Type Subtype Des Start Date End Date FRAC FRAC EQUIP FRAC RELOAD ACTIVITIES 4/15/2025 16:00 4/16/2025 23:59 PUMPING 74-H 4/20/2025 06:00 4/21/2025 14:00 Page 1/1 3S-602 Report Printed: 5/13/2025 Daily STIM Report ORIG SPUD DATE: [ 2/26/2025 ] DRLG RIG RELEASE: [ 3/24/2025 ] ON PRODUCTION: [ ] DAYS FROM SPUD: [ 45.44 ] REPORT # [ 3] REPORT DATE: [ 4/12/2025] API / UWI 5010320906 Original KB/RT Elevation (ft) 67.70 Ground Elevation (ft) 27.70 Original Spud Date 2/26/2025 Primary Job Type INITIAL COMPLETION Secondary Job Type Total AFE (Cost) 8,443,262.00 AFE / RFE / Maint.# GKA.00108.E.W001.CO.I W;GKA.00108.E.W001.C O.IS;GKA.00108.E.W001. CO.IF Network/Order Number 10463819;10441038;104 63818 AFE+Supp Amt (Cost) 8,443,262.00 Daily Cost Total (Cost) 76,935.11 Cumulative Cost (Cost) 187,757.11 Weather Temperature (°F) Road Condition Wind Last 24hr Summary COMPLETE RIG UP, REHEAT WATER, FUNCTION TEST EQUIPMENT 24hr Forecast General Remarks ZX Code ZX02 Fracturing Contact Name Title Mobile OSSELBURN, DEREK SL 724-494-3261 LAWSON, JACOB Supervisor 971-606-0075 YEATS, SPENCER LAUNCH TECH 403-896-8933 Time Log Start Time End Time Dur (hr) Phase Activity Code Time P- T-X Operation 00:00 06:30 6.50 COMPZN, STIM RURD P STAGE CHEM TRUCKS, TRIP EQUIPMENT 06:30 17:30 11.00 COMPZN, STIM RURD P COMPLETE RIG IN, HANG RISERS, SET BLEED OFF MANIFOLD AND THE CVA 17:30 00:00 6.50 COMPZN, STIM RURD P REHEAT WATER, PREP EQUIPMENT Report Fluids Summary Fluid To well (bbl) Cum to Well (bbl) DIESEL 1.0 Contractor Rig Name/# Rig Supervisor Rig Accept Date RR Date Rig Type LRS 74-H BURKETT, CHAD,Wells Supervisor 4/11/2025 06:00 4/11/2025 14:00 PUMPING HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/11/2025 14:00 4/11/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/12/2025 00:00 4/12/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/13/2025 00:00 4/13/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/14/2025 00:00 4/14/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/15/2025 00:00 4/15/2025 15:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/16/2025 00:00 4/16/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/17/2025 00:00 4/17/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/18/2025 00:00 4/18/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/19/2025 00:00 4/19/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/20/2025 00:00 4/20/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/21/2025 00:00 4/21/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/22/2025 00:00 4/22/2025 12:00 FRAC Offline Activities Type Subtype Des Start Date End Date FRAC FRAC EQUIP FRAC RELOAD ACTIVITIES 4/15/2025 16:00 4/16/2025 23:59 PUMPING 74-H 4/20/2025 06:00 4/21/2025 14:00 Page 1/2 3S-602 Report Printed: 5/13/2025 Daily STIM Report ORIG SPUD DATE: [ 2/26/2025 ] DRLG RIG RELEASE: [ 3/24/2025 ] ON PRODUCTION: [ ] DAYS FROM SPUD: [ 46.44 ] REPORT # [ 4] REPORT DATE: [ 4/13/2025] API / UWI 5010320906 Original KB/RT Elevation (ft) 67.70 Ground Elevation (ft) 27.70 Original Spud Date 2/26/2025 Primary Job Type INITIAL COMPLETION Secondary Job Type Total AFE (Cost) 8,443,262.00 AFE / RFE / Maint.# GKA.00108.E.W001.CO.I W;GKA.00108.E.W001.C O.IS;GKA.00108.E.W001. CO.IF Network/Order Number 10463819;10441038;104 63818 AFE+Supp Amt (Cost) 8,443,262.00 Daily Cost Total (Cost) 524,690.56 Cumulative Cost (Cost) 712,447.67 Weather Temperature (°F) Road Condition Wind Last 24hr Summary STIM INTERVALS 1-3, TOTAL SLURRY VOLUME 9,054 BBL, TOTAL PROPPANT PLACED 607,023 LB INTERVAL 1 PUMPED TO DESIGN, TOTAL PROPPANT PLACED 202,260, TOTAL CLEAN VOLUME 2,792 BBL, INTERVAL 2 PUMPED TO DESIGN, BALL LANDED 15 BBL EARLY, TOTAL PROPPANT PLACED 203,282, LB, TOTAL CLEAN VOLUME 2,529 BBL,PUMP ISSUES FORCED SHUT DOWN AFTER BALL SEATED FOR INTERVAL 3 INTERVAL 3 PUMPED TO DESIGN, BALL LANDED 14 BBL EARLY, TOTAL PROPPANT PLACED 201,481 , TOTAL CLEAN VOLUME 3,088 BBL 24hr Forecast General Remarks INT T/I/O =0/100/0 END T/I/O = 1131/700/489 ZX Code ZX02 Fracturing Contact Name Title Mobile OSSELBURN, DEREK SL 724-494-3261 LAWSON, JACOB Supervisor 971-606-0075 YEATS, SPENCER LAUNCH TECH 403-896-8933 Time Log Start Time End Time Dur (hr) Phase Activity Code Time P- T-X Operation 00:00 06:30 6.50 COMPZN, STIM RURD P REHEATING WATER, FIRE UP AND FUNCTION TEST EQUIPMENT 06:30 07:30 1.00 COMPZN, STIM RURD P SITE SAFETY MEETING 07:30 08:30 1.00 COMPZN, STIM RURD P PRE JOB PREPERATIONS 08:30 08:54 0.40 COMPZN, STIM RURD P PRIME AND TEST STARTING PSI 9547, ENDING PSI 9326, GOOD TEST 08:54 09:30 0.60 COMPZN, STIM RURD P MIX GEL, LOAD BALLS, 09:30 10:24 0.90 COMPZN, STIM PUMP P EQUALIZE TO 600, OPENING PSI IS 549 PSI ARSENAL DISC BURST @ 6962, 9060 BHP, ALPHA SHIFTED 5761, DHG 9671, PERFORM DFIT, HARD SHUT DOWN, MONITOUR PSI RESPONCE, 10:24 12:09 1.75 COMPZN, STIM PUMP P OPENING PSI 322 SURFACE 3260 DHG, PERFORMED STEP RATE TEST, ROLLED INTO STIM, INTERVAL PUMPED TO DESIGN, TOTAL CLEAN 2792, TOTAL SLURRY 3,007, TOTAL PROPPANT 202,260, 300 LB 100 MESH, 199,260 16/20 BALL 1 LAUNCHED FOR INTERVAL 2@ 2963 BBL JSV 12:09 13:30 1.35 COMPZN, STIM PUMP P BALL ON SEAT 15 BBL EARLY, SURF PEAK 6276, BH PEAK 7498, SURFACE DIFFERENTIAL 3258, BH DIFFERENTIAL 2906, PUMPED INTERVAL TO DESIGN, TOTAL CLEAN VOLUME 2,529 BBL, TOTAL SLURRY VOLUME 2,745 BBL, TOTAL PROPPANT PLACED 203,282 BALL LAUNCHED @ 5,717 BBL JSV FOR INTERVAL 3. DURING THE 5 LB SAND STAGE PUMP 579 LOST A HIGH PRESSURE SEAL, CONTINUED THE STAGE, DURING THE FINAL SAND STAGE PUMP 563 LOST THE PACKING, WENT TO FLUSH, LANDED THE BALL ON SEAT AND SHUT DOWN TO WORK ON EQUIPMENT. 13:30 13:33 0.05 COMPZN, STIM PUMP P BALL ON SEAT @ 5972 JSV 14 BBL EARLY, SHUT DOWN FOR PUMP REPAIR. 13:33 15:03 1.50 COMPZN, STIM WOUR T DOWN FOR PUMP REPAIR 15:03 16:27 1.40 COMPZN, STIM PUMP P PRIME AND PT, PT START 9425, PSI END 9326, GOOD TEST EQUALIZED TO 1100, OPENED UP @1111 PSI ESTABLISHED RATE CAME UP TO 15 BPM, ESTABLISHED GOOD XL, PUMPED INTERVAL TO DESIGN, TOTAL CLEAN VOLUME 3,088 BBL, TOTAL SLURRY VOLUME 3,202 BBL, TOTAL PROPPANT PLACED 201,481 FLUSHED WELL, HARD SHUT DOWN. 16:27 16:42 0.25 COMPZN, STIM WAIT P MONITOUR PSI, 5,10,15 16:42 17:24 0.70 COMPZN, STIM WAIT P FAN EQUIPMENT OUT, BLOW DOWN, LRS RIG DOWN AND RIG UP TO THE TUBING 17:24 17:54 0.50 COMPZN, STIM PUMP P LRS PUMP 35 BBL DIESEL FREEZE PROTECT 17:54 23:59 6.09 COMPZN, STIM WAIT P LOAD /HEAT WATER, PLANNED PUMP MAINTENANCE Report Fluids Summary Fluid To well (bbl) Cum to Well (bbl) DIESEL 1.0 Page 2/2 3S-602 Report Printed: 5/13/2025 Daily STIM Report ORIG SPUD DATE: [ 2/26/2025 ] DRLG RIG RELEASE: [ 3/24/2025 ] ON PRODUCTION: [ ] DAYS FROM SPUD: [ 46.44 ] REPORT # [ 4] REPORT DATE: [ 4/13/2025] Contractor Rig Name/# Rig Supervisor Rig Accept Date RR Date Rig Type LRS 74-H BURKETT, CHAD,Wells Supervisor 4/11/2025 06:00 4/11/2025 14:00 PUMPING HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/11/2025 14:00 4/11/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/12/2025 00:00 4/12/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/13/2025 00:00 4/13/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/14/2025 00:00 4/14/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/15/2025 00:00 4/15/2025 15:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/16/2025 00:00 4/16/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/17/2025 00:00 4/17/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/18/2025 00:00 4/18/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/19/2025 00:00 4/19/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/20/2025 00:00 4/20/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/21/2025 00:00 4/21/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/22/2025 00:00 4/22/2025 12:00 FRAC Offline Activities Type Subtype Des Start Date End Date FRAC FRAC EQUIP FRAC RELOAD ACTIVITIES 4/15/2025 16:00 4/16/2025 23:59 PUMPING 74-H 4/20/2025 06:00 4/21/2025 14:00 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 4/13/2025 09:29 4/13/2025 12:02 18,671.2 18,675.5 203,000.0 202,260.0 2,791.69 3,006.54 2 4/13/2025 12:02 4/13/2025 13:29 18,190.6 18,194.9 203,000.0 203,254.0 2,529.00 2,745.01 3 4/13/2025 15:03 4/13/2025 16:25 17,709.3 17,713.6 203,000.0 201,555.7 3,087.93 3,302.05 Page 1/2 3S-602 Report Printed: 5/13/2025 Daily STIM Report ORIG SPUD DATE: [ 2/26/2025 ] DRLG RIG RELEASE: [ 3/24/2025 ] ON PRODUCTION: [ ] DAYS FROM SPUD: [ 47.44 ] REPORT # [ 5] REPORT DATE: [ 4/14/2025] API / UWI 5010320906 Original KB/RT Elevation (ft) 67.70 Ground Elevation (ft) 27.70 Original Spud Date 2/26/2025 Primary Job Type INITIAL COMPLETION Secondary Job Type Total AFE (Cost) 8,443,262.00 AFE / RFE / Maint.# GKA.00108.E.W001.CO.I W;GKA.00108.E.W001.C O.IS;GKA.00108.E.W001. CO.IF Network/Order Number 10463819;10441038;104 63818 AFE+Supp Amt (Cost) 8,443,262.00 Daily Cost Total (Cost) 525,024.56 Cumulative Cost (Cost) 1,237,472.23 Weather Temperature (°F) Road Condition Wind Last 24hr Summary PUMP STAGES 4-7 TOTAL SLURRY VOLUME PUMPED, 8170 BBL, TOTAL PROPPANT PLACED 816,100 LB. INTERVAL 4 PUMPED TO DESIGN, BALL LANDED 9 BBL EARLY, TOTAL PROPPANT PLACED,205,710 , TOTAL CLEAN VOLUME 2,264 BBL, INTERVAL 5 PUMPED TO DESIGN, BALL LANDED 10 BBL EARLY, TOTAL PROPPANT PLACED 203,996 , LB, TOTAL CLEAN VOLUME 1620 BBL, INTERVAL 6 PUMPED TO DESIGN, BALL LANDED 11 BBL EARLY, TOTAL PROPPANT PLACED 202,978 CLEAN VOLUME 1,581 BBL INTERVAL 7 PUMPED TO DESIGN, BALL LANDED 8 BBL EARLY, TOTAL PROPPANT PLACED 203,416 TOTAL CLEAN VOLUME 1836 BBL 24hr Forecast General Remarks INT T/I/O =566/0/422 END T/I/O = 980/700/498 ZX Code ZX02 Fracturing Contact Name Title Mobile OSSELBURN, DEREK SL 724-494-3261 LAWSON, JACOB Supervisor 971-606-0075 YEATS, SPENCER LAUNCH TECH 403-896-8933 Time Log Start Time End Time Dur (hr) Phase Activity Code Time P- T-X Operation 00:00 05:30 5.50 COMPZN, STIM WAIT P MAINTENACED 3 PUMPS, LOADED HEATED WATER/ LOADED GEL 05:30 12:15 6.75 COMPZN, STIM WOW T PHASE 2 CALLED 12:15 12:45 0.50 COMPZN, STIM WAIT SAFETY MEETING 12:45 13:24 0.65 COMPZN, STIM WAIT PRIME AND PT EQUIPMENT PSI TEST START 9525, ENDING PSI 9335 GOOD TEST 13:24 13:42 0.30 COMPZN, STIM WAIT LOAD BALLS MIX GEL 13:42 15:09 1.45 COMPZN, STIM PUMP EQUALIZED TO 1000 PSI, OPENING PSI 566, ESTABLISHED INJECTION, LAUNCHED BALL 3 FOR STAGE 4, LAUNCHED @ 21 JSV, BALL ON SEAT@ 274 JSV 9 BBL EARLY , SURFACE PEAK, 2906, BH PEAK 4402, DIFFERENTIAL SURFACE 494, BH DIFFERENTIAL 538, INTERVAL PUMPED TO DESIGN, TOTAL CLEAN VOLUME 2,264 BBL, TOTAL SLURRY VOLUME 2,482, TOTAL PROPPANT,205,710, BALL 4 INTERVAL 5 LAUNCHED @ 2449 JSV 15:09 16:01 0.88 COMPZN, STIM PUMP INTERVAL 5 BALL ON SEAT @ 2693 JSV 10 BBL EARLY, SURFACE PEAK 6064, BH PEAK 7411, SURFACE DIFFERENTIAL 3246, BH DIFFERENTIAL 3104, TOTAL CLEAN, 1,620, TOTAL SLURRY 1,836, TOTAL PROPPANT 203,996, LAUNCHED BALL 4 FOR INTERVAL 5 @ 4296 JSV 16:01 16:55 0.90 COMPZN, STIM PUMP INTERVAL 6 BALL ON SEAT 4531 JSV, SURFACE PEAK 6255, BH PEAK 7483, SURFACE DIFFERENTIAL 3332, BH DIFFERENTIAL 3134, INTERVAL PUMPED TO DESIGN TOTAL CLEAN PUMPED 1,581, TOTAL SLURRY 1,797, TOTAL PROPPANT PLACED 202,978, BALL LAUNCHED @ 6099 JSV 16:55 18:01 1.10 COMPZN, STIM PUMP INTERVAL 7 BALL ON SEAT @ 6329 8BBL EARLY, SURFACE PEAK 5782, BH PEAK 7093, SURFACE DIFFERENTIAL 3013, BH DIFFERENTIAL 2888, INTERVAL PUMPED TO DESIGN, TOTAL CLEAN 1,839, TOTAL SLURRY 2,055, TOTAL PROPPANT 203,416 HARD SHUT DOWN 15 MIN PSI MONITORING. 18:01 18:16 0.25 COMPZN, STIM WAIT 5, 10,15, MINUTE. 18:16 19:01 0.75 COMPZN, STIM WAIT FAN OUT BLOW DOWN 19:01 19:37 0.60 COMPZN, STIM PUMP LRS PUMPED 35 BBL DIESEL FREEZE PROTECT. 19:37 20:07 0.50 COMPZN, STIM CONTINUED CLEAN UP 20:07 23:59 3.86 COMPZN, STIM LOAD/HEAT WATER Report Fluids Summary Fluid To well (bbl) Cum to Well (bbl) DIESEL 1.0 Contractor Rig Name/# Rig Supervisor Rig Accept Date RR Date Rig Type LRS 74-H BURKETT, CHAD,Wells Supervisor 4/11/2025 06:00 4/11/2025 14:00 PUMPING HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/11/2025 14:00 4/11/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/12/2025 00:00 4/12/2025 23:59 FRAC Page 2/2 3S-602 Report Printed: 5/13/2025 Daily STIM Report ORIG SPUD DATE: [ 2/26/2025 ] DRLG RIG RELEASE: [ 3/24/2025 ] ON PRODUCTION: [ ] DAYS FROM SPUD: [ 47.44 ] REPORT # [ 5] REPORT DATE: [ 4/14/2025] Contractor Rig Name/# Rig Supervisor Rig Accept Date RR Date Rig Type HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/13/2025 00:00 4/13/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/14/2025 00:00 4/14/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/15/2025 00:00 4/15/2025 15:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/16/2025 00:00 4/16/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/17/2025 00:00 4/17/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/18/2025 00:00 4/18/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/19/2025 00:00 4/19/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/20/2025 00:00 4/20/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/21/2025 00:00 4/21/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/22/2025 00:00 4/22/2025 12:00 FRAC Offline Activities Type Subtype Des Start Date End Date FRAC FRAC EQUIP FRAC RELOAD ACTIVITIES 4/15/2025 16:00 4/16/2025 23:59 PUMPING 74-H 4/20/2025 06:00 4/21/2025 14:00 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) 4 4/14/2025 13:41 4/14/2025 03:02 17,229.7 17,234.1 203,000.0 205,646.0 2,263.83 2,482.35 5 4/14/2025 03:02 4/14/2025 15:55 16,707.1 16,711.4 203,000.0 203,914.0 1,619.76 1,836.46 6 4/14/2025 15:55 4/14/2025 16:47 16,184.8 16,189.1 203,000.0 202,934.0 1,581.14 1,796.76 7 4/14/2025 16:47 4/14/2025 17:45 15,662.4 15,666.7 203,000.0 203,399.2 1,838.52 2,054.60 Page 1/2 3S-602 Report Printed: 5/13/2025 Daily STIM Report ORIG SPUD DATE: [ 2/26/2025 ] DRLG RIG RELEASE: [ 3/24/2025 ] ON PRODUCTION: [ ] DAYS FROM SPUD: [ 48.10 ] REPORT # [ 6] REPORT DATE: [ 4/15/2025] API / UWI 5010320906 Original KB/RT Elevation (ft) 67.70 Ground Elevation (ft) 27.70 Original Spud Date 2/26/2025 Primary Job Type INITIAL COMPLETION Secondary Job Type Total AFE (Cost) 8,443,262.00 AFE / RFE / Maint.# GKA.00108.E.W001.CO.I W;GKA.00108.E.W001.C O.IS;GKA.00108.E.W001. CO.IF Network/Order Number 10463819;10441038;104 63818 AFE+Supp Amt (Cost) 8,443,262.00 Daily Cost Total (Cost) 523,354.56 Cumulative Cost (Cost) 1,760,826.79 Weather Temperature (°F) Road Condition Wind Last 24hr Summary PUMP STAGES 8-12, TOTAL SLURRY PUMPED 9,390 BBL, TOTAL PROPPANT PLACED 1,017,792 LB INTERVAL 8 PUMPED TO DESIGN, BALL LANDED 9 BBL EARLY, TOTAL PROPPANT PLACED,203,874,LB,TOTAL CLEAN VOLUME 1729 BBL INTERVAL 9 PUMPED TO DESIGN, BALL LANDED 9 BBL EARLY, TOTAL PROPPANT PLACED 202,174,LB,TOTAL CLEAN VOLUME 1589 BBL INTERVAL 10 PUMPED TO DESIGN, BALL LANDED 4 BBL EARLY, TOTAL PROPPANT PLACED 203,153 LB.TOAL CLEAN VOLUME 1579 BBL INTERVAL 11 PUMPED TO DESIGN, BALL LANDED 7 BBL EARLY, TOTAL PROPPANT PLACED 204,926 LB.TOTAL CLEAN VOLUME 1593 BBL INTERVAL 12 PUMPED TO DESIGN, BALL LANDED 8 BBL EARLY, TOTAL PROPPANT PLACED 203,665 LB.TOTAL CLEAN VOLUME 1820 BBL 24hr Forecast General Remarks INT T/I/O =634/0/389 END T/I/O = 1025/700/506 ZX Code ZX02 Fracturing Contact Name Title Mobile OSSELBURN, DEREK SL 724-494-3261 LAWSON, JACOB Supervisor 971-606-0075 YEATS, SPENCER LAUNCH TECH 403-896-8933 Time Log Start Time End Time Dur (hr) Phase Activity Code Time P- T-X Operation 00:00 06:30 6.50 COMPZN, STIM WAIT P LOAD/HEAT WATER, PUMP MAINTENANCE, LOAD GEL 06:30 07:00 0.50 COMPZN, STIM WAIT P SAFETY MEETING 07:00 08:06 1.10 COMPZN, STIM WAIT P PRIME PUMPS, TESTED ePRVS, FOUND A PACKING NEEDING REPLACED ON PUMP 458. 08:06 08:36 0.50 COMPZN, STIM WAIT P STARTED TO PT, FOUND A HP SEAL WAS MISSING ON PUMP 329, INSERTED AND RESUMED PT, PT START 9429 @ 8:29 AM, END 9324, GOOD TEST. 08:36 09:00 0.40 COMPZN, STIM WAIT P MIX GEL, LOAD BALLS, AND PULL ON CHEMS. 09:00 10:05 1.09 COMPZN, STIM PUMP P EQUALIZED TO 1100, OPENED WELL OPENING PSI 648, LAUNCHED BALL 7 FOR INTERVAL 8 @ 12 JSV, BALL ON SEAT @ 233 JSV, 9 BBL EARLY SURFACE PEAK 4734, BH PEAK 628, SURFACE DIFFERENTIAL 2669, BH DIFFERENTIAL 2607, COMPLETED INTERVAL 8 TO DESIGN, TOTAL CLEAN VOLUME 1729, TOTAL SLURRY VOLUME 1946, TOTAL PROPPANT 203,874,3000LB 100 MESH 200,876 16/20 LAUNCHED BALL 8 FOR INTERVAL 9 @ 1907 JSV 10:05 10:57 0.87 COMPZN, STIM PUMP P BALL 8 FOR INTERVAL 9 ON SEAT @ 2120 JSV, 9 BBL EARLY SURFACE PEAK 5991, BH PEAK 7101 SURFACE DIFFERENTIAL 3284, BH DIFFERENTIAL 2953, COMPLETED INTERVAL 9 TO DESIGN, TOTAL CLEAN VOLUME 1589, TOTAL SLURRY VOLUME 1803, TOTAL PROPPANT 202,174,3000LB 100 MESH, 199,174 16/20 BALL 9 FOR INTRERVAL10 @ 3718 JSV 10:57 11:49 0.86 COMPZN, STIM PUMP P BALL 9 FOR INTERVAL 10 ON SEAT @ 3929 JSV, 4 BBL EARLY SURFACE PEAK 5965, BH PEAK 7170 SURFACE DIFFERENTIAL 3346, BH DIFFERENTIAL 3068, COMPLETED INTERVAL TO DESIGN, TOTAL CLEAN VOLUME 1579 , TOTAL SLURRY VOLUME 1795 TOTAL PROPPANT 203,153, 3000LB 100 MESH 200,153 LB 16/20 BALL 10 FOR INTRERVAL11 @ 5523 JSV 11:49 12:49 1.00 COMPZN, STIM PUMP P BALL 10 FOR INTERVAL 11 ON SEAT @ 3929 JSV, 7 BBL EARLY ,SURFACE PEAK 5796 , BH PEAK 6994, SURFACE DIFFERENTIAL 3219, BH DIFFERENTIAL 6994, COMPLETED INTERVAL TO DESIGN, TOTAL CLEAN VOLUME 1593, TOTAL SLURRY VOLUME 1810, TOTAL PROPPANT 203,926 3000LB 100 MESH 200,926 16/20 BALL 10 FOR INTRERVAL11 LAUNCHED @ 5523 JSV 12:49 13:43 0.90 COMPZN, STIM PUMP P BALL 11 FOR INTERVAL 12 ON SEAT @ 7532 JSV, 7 BBL EARLY ,SURFACE PEAK 5607, BH PEAK 7018, SURFACE DIFFERENTIAL 3175, BH DIFFERENTIAL 3064, COMPLETED INTERVAL TO DESIGN, TOTAL CLEAN VOLUME 1820 , TOTAL SLURRY VOLUME 2036, TOTAL PROPPANT 203,665 3000LB 100 MESH 200,665 16/20, 15 MINUTE PRESSURE MONITORING 13:43 13:58 0.25 COMPZN, STIM WAIT 15 MINUTES ISIP 13:58 14:58 1.00 COMPZN, STIM WAIT FAN OUT BLOW DOWN, BRINE UP, Page 2/2 3S-602 Report Printed: 5/13/2025 Daily STIM Report ORIG SPUD DATE: [ 2/26/2025 ] DRLG RIG RELEASE: [ 3/24/2025 ] ON PRODUCTION: [ ] DAYS FROM SPUD: [ 48.10 ] REPORT # [ 6] REPORT DATE: [ 4/15/2025] Time Log Start Time End Time Dur (hr) Phase Activity Code Time P- T-X Operation 14:58 15:28 0.51 COMPZN, STIM PUMP LRS PUMP 35 BBL DIESEL FREEZE PROTECT.start 14:55 15:28 15:59 0.51 COMPZN, STIM RIG OUT EQUIPMENT FOR SLICKLINE OPERATIONS Report Fluids Summary Fluid To well (bbl) Cum to Well (bbl) DIESEL 1.0 Contractor Rig Name/# Rig Supervisor Rig Accept Date RR Date Rig Type LRS 74-H BURKETT, CHAD,Wells Supervisor 4/11/2025 06:00 4/11/2025 14:00 PUMPING HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/11/2025 14:00 4/11/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/12/2025 00:00 4/12/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/13/2025 00:00 4/13/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/14/2025 00:00 4/14/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/15/2025 00:00 4/15/2025 15:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/16/2025 00:00 4/16/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/17/2025 00:00 4/17/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/18/2025 00:00 4/18/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/19/2025 00:00 4/19/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/20/2025 00:00 4/20/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/21/2025 00:00 4/21/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/22/2025 00:00 4/22/2025 12:00 FRAC Offline Activities Type Subtype Des Start Date End Date FRAC FRAC EQUIP FRAC RELOAD ACTIVITIES 4/15/2025 16:00 4/16/2025 23:59 PUMPING 74-H 4/20/2025 06:00 4/21/2025 14:00 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) 8 4/15/2025 09:01 4/15/2025 10:05 15,140.2 15,144.6 203,000.0 203,874.0 1,729.14 1,945.78 9 4/15/2025 10:05 4/15/2025 10:57 14,618.2 14,622.5 203,000.0 202,174.0 1,588.67 1,803.48 10 4/15/2025 10:57 4/15/2025 11:49 14,098.9 14,103.3 203,000.0 203,153.0 1,578.93 1,794.79 11 4/15/2025 11:49 4/15/2025 12:48 13,576.4 13,580.8 203,000.0 204,926.0 1,592.69 1,810.45 12 4/15/2025 12:48 4/15/2025 13:39 13,053.8 13,058.2 203,000.0 203,665.2 1,819.62 2,035.98 Page 1/1 3S-602 Report Printed: 5/13/2025 Daily STIM Report ORIG SPUD DATE: [ 2/26/2025 ] DRLG RIG RELEASE: [ 3/24/2025 ] ON PRODUCTION: [ ] DAYS FROM SPUD: [ 49.44 ] REPORT # [ 7] REPORT DATE: [ 4/16/2025] API / UWI 5010320906 Original KB/RT Elevation (ft) 67.70 Ground Elevation (ft) 27.70 Original Spud Date 2/26/2025 Primary Job Type INITIAL COMPLETION Secondary Job Type Total AFE (Cost) 8,443,262.00 AFE / RFE / Maint.# GKA.00108.E.W001.CO.I W;GKA.00108.E.W001.C O.IS;GKA.00108.E.W001. CO.IF Network/Order Number 10463819;10441038;104 63818 AFE+Supp Amt (Cost) 8,443,262.00 Daily Cost Total (Cost) 64,685.11 Cumulative Cost (Cost) 1,825,511.90 Weather Temperature (°F) Road Condition Wind Last 24hr Summary JOB ON HOLD FOR SL TO PULL ISO SLEEVE 24hr Forecast General Remarks ZX Code ZX02 Fracturing Contact Name Title Mobile OSSELBURN, DEREK SL 724-494-3261 LAWSON, JACOB Supervisor 971-606-0075 YEATS, SPENCER LAUNCH TECH 403-896-8933 Time Log Start Time End Time Dur (hr) Phase Activity Code Time P- T-X Operation 00:00 23:59 23.99 COMPZN, STIM WAIT P SL PULL NEXA SLEEVE FOR INSPECTION Report Fluids Summary Fluid To well (bbl) Cum to Well (bbl) DIESEL 1.0 Contractor Rig Name/# Rig Supervisor Rig Accept Date RR Date Rig Type LRS 74-H BURKETT, CHAD,Wells Supervisor 4/11/2025 06:00 4/11/2025 14:00 PUMPING HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/11/2025 14:00 4/11/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/12/2025 00:00 4/12/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/13/2025 00:00 4/13/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/14/2025 00:00 4/14/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/15/2025 00:00 4/15/2025 15:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/16/2025 00:00 4/16/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/17/2025 00:00 4/17/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/18/2025 00:00 4/18/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/19/2025 00:00 4/19/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/20/2025 00:00 4/20/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/21/2025 00:00 4/21/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/22/2025 00:00 4/22/2025 12:00 FRAC Offline Activities Type Subtype Des Start Date End Date FRAC FRAC EQUIP FRAC RELOAD ACTIVITIES 4/15/2025 16:00 4/16/2025 23:59 PUMPING 74-H 4/20/2025 06:00 4/21/2025 14:00 Other In Hole Des Run Date OD (in) Top (ftKB) Btm (ftKB) ISO-SLEEVE 4/16/2025 04:29 3.830 5,879.0 5,868.0 ISO-SLEEVE 4/16/2025 04:29 3.790 5,962.0 5,925.0 Page 1/1 3S-602 Report Printed: 5/13/2025 Daily STIM Report ORIG SPUD DATE: [ 2/26/2025 ] DRLG RIG RELEASE: [ 3/24/2025 ] ON PRODUCTION: [ ] DAYS FROM SPUD: [ 50.44 ] REPORT # [ 8] REPORT DATE: [ 4/17/2025] API / UWI 5010320906 Original KB/RT Elevation (ft) 67.70 Ground Elevation (ft) 27.70 Original Spud Date 2/26/2025 Primary Job Type INITIAL COMPLETION Secondary Job Type Total AFE (Cost) 8,443,262.00 AFE / RFE / Maint.# GKA.00108.E.W001.CO.I W;GKA.00108.E.W001.C O.IS;GKA.00108.E.W001. CO.IF Network/Order Number 10463819;10441038;104 63818 AFE+Supp Amt (Cost) 8,443,262.00 Daily Cost Total (Cost) 64,685.11 Cumulative Cost (Cost) 1,890,197.01 Weather Temperature (°F) Road Condition Wind Last 24hr Summary DOWN FOR WEATHER 24hr Forecast General Remarks ZX Code ZX02 Fracturing Contact Name Title Mobile OSSELBURN, DEREK SL 724-494-3261 LAWSON, JACOB Supervisor 971-606-0075 Time Log Start Time End Time Dur (hr) Phase Activity Code Time P- T-X Operation 00:00 06:30 6.50 COMPZN, STIM WAIT P EQUIPMENT MAINT, LOAD/HEAT WATER 06:30 07:00 0.50 COMPZN, STIM WAIT P PJSM 07:00 09:00 2.00 COMPZN, STIM WAIT P REPLACE 4" GROUND VALVES 09:00 23:59 14.99 COMPZN, STIM WOW T PHASE 2 Report Fluids Summary Fluid To well (bbl) Cum to Well (bbl) DIESEL 1.0 Contractor Rig Name/# Rig Supervisor Rig Accept Date RR Date Rig Type LRS 74-H BURKETT, CHAD,Wells Supervisor 4/11/2025 06:00 4/11/2025 14:00 PUMPING HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/11/2025 14:00 4/11/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/12/2025 00:00 4/12/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/13/2025 00:00 4/13/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/14/2025 00:00 4/14/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/15/2025 00:00 4/15/2025 15:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/16/2025 00:00 4/16/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/17/2025 00:00 4/17/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/18/2025 00:00 4/18/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/19/2025 00:00 4/19/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/20/2025 00:00 4/20/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/21/2025 00:00 4/21/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/22/2025 00:00 4/22/2025 12:00 FRAC Offline Activities Type Subtype Des Start Date End Date FRAC FRAC EQUIP FRAC RELOAD ACTIVITIES 4/15/2025 16:00 4/16/2025 23:59 PUMPING 74-H 4/20/2025 06:00 4/21/2025 14:00 Page 1/1 3S-602 Report Printed: 5/13/2025 Daily STIM Report ORIG SPUD DATE: [ 2/26/2025 ] DRLG RIG RELEASE: [ 3/24/2025 ] ON PRODUCTION: [ ] DAYS FROM SPUD: [ 51.44 ] REPORT # [ 9] REPORT DATE: [ 4/18/2025] API / UWI 5010320906 Original KB/RT Elevation (ft) 67.70 Ground Elevation (ft) 27.70 Original Spud Date 2/26/2025 Primary Job Type INITIAL COMPLETION Secondary Job Type Total AFE (Cost) 8,443,262.00 AFE / RFE / Maint.# GKA.00108.E.W001.CO.I W;GKA.00108.E.W001.C O.IS;GKA.00108.E.W001. CO.IF Network/Order Number 10463819;10441038;104 63818 AFE+Supp Amt (Cost) 8,443,262.00 Daily Cost Total (Cost) 64,685.11 Cumulative Cost (Cost) 1,954,882.12 Weather Temperature (°F) Road Condition Wind Last 24hr Summary DOWN FOR WEATHER - PHASE 3 24hr Forecast General Remarks ZX Code ZX02 Fracturing Contact Name Title Mobile OSSELBURN, DEREK SL 724-494-3261 LAWSON, JACOB Supervisor 971-606-0075 Time Log Start Time End Time Dur (hr) Phase Activity Code Time P- T-X Operation 00:00 23:59 23.99 COMPZN, STIM WOW T DOWN FOR WEATHER Report Fluids Summary Fluid To well (bbl) Cum to Well (bbl) DIESEL 1.0 Contractor Rig Name/# Rig Supervisor Rig Accept Date RR Date Rig Type LRS 74-H BURKETT, CHAD,Wells Supervisor 4/11/2025 06:00 4/11/2025 14:00 PUMPING HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/11/2025 14:00 4/11/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/12/2025 00:00 4/12/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/13/2025 00:00 4/13/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/14/2025 00:00 4/14/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/15/2025 00:00 4/15/2025 15:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/16/2025 00:00 4/16/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/17/2025 00:00 4/17/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/18/2025 00:00 4/18/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/19/2025 00:00 4/19/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/20/2025 00:00 4/20/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/21/2025 00:00 4/21/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/22/2025 00:00 4/22/2025 12:00 FRAC Offline Activities Type Subtype Des Start Date End Date FRAC FRAC EQUIP FRAC RELOAD ACTIVITIES 4/15/2025 16:00 4/16/2025 23:59 PUMPING 74-H 4/20/2025 06:00 4/21/2025 14:00 Page 1/1 3S-602 Report Printed: 5/13/2025 Daily STIM Report ORIG SPUD DATE: [ 2/26/2025 ] DRLG RIG RELEASE: [ 3/24/2025 ] ON PRODUCTION: [ ] DAYS FROM SPUD: [ 52.44 ] REPORT # [ 10] REPORT DATE: [ 4/19/2025] API / UWI 5010320906 Original KB/RT Elevation (ft) 67.70 Ground Elevation (ft) 27.70 Original Spud Date 2/26/2025 Primary Job Type INITIAL COMPLETION Secondary Job Type Total AFE (Cost) 8,443,262.00 AFE / RFE / Maint.# GKA.00108.E.W001.CO.I W;GKA.00108.E.W001.C O.IS;GKA.00108.E.W001. CO.IF Network/Order Number 10463819;10441038;104 63818 AFE+Supp Amt (Cost) 8,443,262.00 Daily Cost Total (Cost) 64,685.11 Cumulative Cost (Cost) 2,019,567.23 Weather Temperature (°F) Road Condition Wind Last 24hr Summary CLEAN UP POST PHASE 3 , RIG UP DART REVOLVER, FUNCTION TEST EQUIPMENT, REHEAT WATER 24hr Forecast General Remarks ZX Code ZX02 Fracturing Contact Name Title Mobile OSSELBURN, DEREK SL 724-494-3261 LAWSON, JACOB Supervisor 971-606-0075 Time Log Start Time End Time Dur (hr) Phase Activity Code Time P- T-X Operation 00:00 06:00 6.00 COMPZN, STIM WAIT T PHASE 3 06:00 13:00 7.00 COMPZN, STIM WAIT T CLEAN UP/REMOVE SNOW FROM WORK AREAS, 13:00 16:00 3.00 COMPZN, STIM WAIT P RIG UP DART REVOLVER, HANG STAND PIPES 16:00 18:00 2.00 COMPZN, STIM WAIT P FUNCTION TEST EQUIPMENT, CHECK PUMPS AND VALVES. COMMS WITH VAN GOOD 18:00 23:59 5.99 COMPZN, STIM WAIT P MIX CHEMICALS, CONTINUE TO REMOVE SNOW FROM WORK AREAS Report Fluids Summary Fluid To well (bbl) Cum to Well (bbl) DIESEL 1.0 Contractor Rig Name/# Rig Supervisor Rig Accept Date RR Date Rig Type LRS 74-H BURKETT, CHAD,Wells Supervisor 4/11/2025 06:00 4/11/2025 14:00 PUMPING HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/11/2025 14:00 4/11/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/12/2025 00:00 4/12/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/13/2025 00:00 4/13/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/14/2025 00:00 4/14/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/15/2025 00:00 4/15/2025 15:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/16/2025 00:00 4/16/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/17/2025 00:00 4/17/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/18/2025 00:00 4/18/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/19/2025 00:00 4/19/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/20/2025 00:00 4/20/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/21/2025 00:00 4/21/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/22/2025 00:00 4/22/2025 12:00 FRAC Offline Activities Type Subtype Des Start Date End Date FRAC FRAC EQUIP FRAC RELOAD ACTIVITIES 4/15/2025 16:00 4/16/2025 23:59 PUMPING 74-H 4/20/2025 06:00 4/21/2025 14:00 Page 1/2 3S-602 Report Printed: 5/13/2025 Daily STIM Report ORIG SPUD DATE: [ 2/26/2025 ] DRLG RIG RELEASE: [ 3/24/2025 ] ON PRODUCTION: [ ] DAYS FROM SPUD: [ 53.44 ] REPORT # [ 11] REPORT DATE: [ 4/20/2025] API / UWI 5010320906 Original KB/RT Elevation (ft) 67.70 Ground Elevation (ft) 27.70 Original Spud Date 2/26/2025 Primary Job Type INITIAL COMPLETION Secondary Job Type Total AFE (Cost) 8,443,262.00 AFE / RFE / Maint.# GKA.00108.E.W001.CO.I W;GKA.00108.E.W001.C O.IS;GKA.00108.E.W001. CO.IF Network/Order Number 10463819;10441038;104 63818 AFE+Supp Amt (Cost) 8,443,262.00 Daily Cost Total (Cost) 1,091,574.76 Cumulative Cost (Cost) 3,111,141.99 Weather Temperature (°F) Road Condition Wind Last 24hr Summary STIMULATE STAGE 13- 17 PER DESIGN w/ 15000 LBS OF 100 MESH & 887086 LBS OF 16/20 PROPPANT UP TO 7 PPG, TOTAL JOB PROPPANT 902086 LB, JOB CLEAN VOLUME PUMPED 7517 BBL (RESMETRICS TRACER ADDED PER SCHEDULE) 24hr Forecast General Remarks INITIAL T/I/O=381/0/0 FINAL T/I/O=1280/700/330 ZX Code ZX02 Fracturing Contact Name Title Mobile OSSELBURN, DEREK SL 724-494-3261 LAWSON, JACOB Supervisor 971-606-0075 Time Log Start Time End Time Dur (hr) Phase Activity Code Time P- T-X Operation 00:00 06:30 6.50 COMPZN, STIM WAIT P HEAT SW, EQUIPMENT MAINT, START EQUIPMENT FOR DAY SHIFT, DELINEATE RZ. 06:30 08:45 2.25 COMPZN, STIM WAIT P PJSM, FLOOD/PRIME EQUIPMENT PRESSURE TEST PT MAX - 9529 PSI PT FAIL - 9052 PSI, LEAK FOUND AT CHIKSAN PT MAX - 9530 PSI PT 5 MIN - 9501 PSI GOOD TEST MEASURE/LOAD BALLS INTO REVOLVER, MIX GEL, PULL CHEMICALS ONTO BLENDER 08:45 10:30 1.75 COMPZN, STIM PUMP P EQUALIZE TO 1203 PSI, OPEN AT 381 PSI STAGE 13, BALL 12 - 2.489" ON SEAT AT 193 JSV, 13 BBL EARLY, SURFACE PEAK 3712 PSI, SURFACE DIFFERENTIAL 2243 PSI, BHP PEAK 5489 PSI, BHP DIFFERENTIAL 2307 PSI, TOTAL CLEAN VOLUME PUMPED 1916 BBL, TOTAL PROPPANT PLACED 204496 LBS, 100 MESH 3000 LBS, 16/20-201496 LBS, AVG PSI 3167 PSI, AVG RATE 34.1 BPM PERFORMED DFIT AT 10 BPM, SHUT IN MONITOR PSI FOR 23 MIN. CLOSURE 2816 PSI PERFORMED SRT IN 2 BBL INCREMENTS TO 6 BPM, 1 BBL INCREMENTS AFTER TO A MAX RATE OF 15 BPM 10:30 11:15 0.75 COMPZN, STIM PUMP P STAGE 14, BALL 13 - 2.525" ON SEAT AT 2317 JSV, 6 BBL EARLY, SURFACE PEAK 5691 PSI, SURFACE DIFFERENTIAL 3082 PSI, BHP PEAK 6978 PSI, BHP DIFFERENTIAL 3004 PSI, TOTAL CLEAN VOLUME PUMPED 1582 BBL, TOTAL PROPPANT PLACED 202937 LBS, 100 MESH 3000 LBS, 16/20 199937 LBS, AVG PSI 3134 PSI, AVG RATE 35.2 BPM 11:15 12:00 0.75 COMPZN, STIM PUMP P STAGE 15, BALL 14 - 2.561" ON SEAT AT 4116 JSV, 5 BBL EARLY, SURFACE PEAK 5269 PSI, SURFACE DIFFERENTIAL 2742 PSI, BHP PEAK 6617 PSI, BHP DIFFERENTIAL 2716 PSI, TOTAL CLEAN VOLUME PUMPED 1610 BBL, TOTAL PROPPANT PLACED 205414 LBS, 100 MESH 3000 LBS, 16/20 - 202414 LBS, AVG PSI 2932 PSI, AVG RATE 36.5 BPM 12:00 12:45 0.75 COMPZN, STIM PUMP P STAGE 16, BALL 15 - 2.598" ON SEAT AT 5946 JSV, 4 BBL EARLY, SURFACE PEAK 5187 PSI, SURFACE DIFFERENTIAL 2758 PSI, BHP PEAK 6639 PSI, BHP DIFFERENTIAL 2807 PSI, TOTAL CLEAN VOLUME PUMPED 1152 BBL, TOTAL PROPPANT PLACED 144020 LBS, 100 MESH 3000 LBS, 16/20 - 141020 LBS, AVG PSI 3078 PSI, AVG RATE 34.5 BPM Page 2/2 3S-602 Report Printed: 5/13/2025 Daily STIM Report ORIG SPUD DATE: [ 2/26/2025 ] DRLG RIG RELEASE: [ 3/24/2025 ] ON PRODUCTION: [ ] DAYS FROM SPUD: [ 53.44 ] REPORT # [ 11] REPORT DATE: [ 4/20/2025] Time Log Start Time End Time Dur (hr) Phase Activity Code Time P- T-X Operation 12:45 13:30 0.75 COMPZN, STIM PUMP P STAGE 17, BALL 16 - 2.635" ON SEAT AT 7249 JSV, 3 BBL EARLY, SURFACE PEAK 5198 PSI, SURFACE DIFFERENTIAL 2793 PSI, BHP PEAK 6476 PSI, BHP DIFFERENTIAL 2633 PSI, TOTAL CLEAN VOLUME PUMPED 1257 BBL, TOTAL PROPPANT PLACED 145219 LBS, 100 MESH 3000 LBS, 16/20 - 142219 LBS, AVG PSI 3247 PSI, AVG RATE 36.5 BPM 13:30 15:15 1.75 COMPZN, STIM PUMP P ISIP-3289 PSI 5 MIN- 3225 PSI 10 MIN-3196 PSI 15 MIN-3174PSI 20 MIN-3153 PSI 25 MIN-3132 PSI 30 MIN-3110 PSI 30 BBL DIESEL FREEZE PROTECT ON TUBING 15:15 23:59 8.74 COMPZN, STIM WAIT P LOAD/HEAT SW, EQUIPMENT MAINT, CHECK EQUIPMENT FLUIDS Report Fluids Summary Fluid To well (bbl) Cum to Well (bbl) DIESEL 30.0 31.0 SEAWATER 7,517.0 7,517.0 Contractor Rig Name/# Rig Supervisor Rig Accept Date RR Date Rig Type LRS 74-H BURKETT, CHAD,Wells Supervisor 4/11/2025 06:00 4/11/2025 14:00 PUMPING HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/11/2025 14:00 4/11/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/12/2025 00:00 4/12/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/13/2025 00:00 4/13/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/14/2025 00:00 4/14/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/15/2025 00:00 4/15/2025 15:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/16/2025 00:00 4/16/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/17/2025 00:00 4/17/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/18/2025 00:00 4/18/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/19/2025 00:00 4/19/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/20/2025 00:00 4/20/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/21/2025 00:00 4/21/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/22/2025 00:00 4/22/2025 12:00 FRAC Offline Activities Type Subtype Des Start Date End Date FRAC FRAC EQUIP FRAC RELOAD ACTIVITIES 4/15/2025 16:00 4/16/2025 23:59 PUMPING 74-H 4/20/2025 06:00 4/21/2025 14:00 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) 13 4/20/2025 08:44 4/20/2025 10:27 12,531.2 12,535.6 203,000.0 204,379.0 1,970.88 2,188.04 14 4/20/2025 10:27 4/20/2025 11:19 12,009.5 12,013.9 203,000.0 202,823.0 1,581.74 1,797.23 15 4/20/2025 11:19 4/20/2025 12:11 11,487.3 11,491.6 203,000.0 205,247.0 1,609.98 1,828.07 16 4/20/2025 12:11 4/20/2025 12:49 10,966.1 10,970.5 143,000.0 143,948.0 1,151.67 1,304.63 17 4/20/2025 12:49 4/20/2025 13:30 10,447.4 10,451.7 143,000.0 145,156.0 1,287.38 1,441.62 Page 1/2 3S-602 Report Printed: 5/13/2025 Daily STIM Report ORIG SPUD DATE: [ 2/26/2025 ] DRLG RIG RELEASE: [ 3/24/2025 ] ON PRODUCTION: [ ] DAYS FROM SPUD: [ 54.44 ] REPORT # [ 12] REPORT DATE: [ 4/21/2025] API / UWI 5010320906 Original KB/RT Elevation (ft) 67.70 Ground Elevation (ft) 27.70 Original Spud Date 2/26/2025 Primary Job Type INITIAL COMPLETION Secondary Job Type Total AFE (Cost) 8,443,262.00 AFE / RFE / Maint.# GKA.00108.E.W001.CO.I W;GKA.00108.E.W001.C O.IS;GKA.00108.E.W001. CO.IF Network/Order Number 10463819;10441038;104 63818 AFE+Supp Amt (Cost) 8,443,262.00 Daily Cost Total (Cost) 1,041,268.28 Cumulative Cost (Cost) 4,152,410.27 Weather Temperature (°F) Road Condition Wind Last 24hr Summary STIMULATE STAGE 18- 23 PER DESIGN w/ 18000 LBS OF 100 MESH & 839172 LBS OF 16/20 PROPPANT UP TO 7 PPG, TOTAL JOB PROPPANT 857172 LB, JOB CLEAN VOLUME PUMPED 6965 BBL (RESMETRICS TRACER ADDED PER SCHEDULE) 24hr Forecast General Remarks INITIAL T/I/O=340/0/192 FINAL T/I/O=1154/700/257 ZX Code ZX02 Fracturing Contact Name Title Mobile OSSELBURN, DEREK SL 724-494-3261 LAWSON, JACOB Supervisor 971-606-0075 Time Log Start Time End Time Dur (hr) Phase Activity Code Time P- T-X Operation 00:00 06:30 6.50 COMPZN, STIM WAIT P NIGHT SHIFT MOVE EQUIPMENT AROUND FOR FLOWBACK RIG UP, START EQUIPMENT, FINISH PUMP MAINT. 06:30 08:15 1.75 COMPZN, STIM WAIT P PJSM, FLOOD/PRIME EQUIPMENT, TEST ePRV'S PT MAX - 9415 PSI PT 5 MIN - 9396 PSI GOOD TEST MEASURE/LOAD BALLS, MIX GEL, PULL CHEMICAL SONTO BLENDER 08:15 09:00 0.75 COMPZN, STIM PUMP P EQUALIZE TO 1107 PSI, OPEN WELL AT 340 PSI. ESTABLISH INJECTION TO 15 BPM AND ESTABLISH FLUIDS. STAGE 18, BALL 17 - 2.672" ON SEAT AT 164 JSV, 8 BBL EARLY, SURFACE PEAK 2981 PSI, SURFACE DIFFERENTIAL 1427 PSI, BHP PEAK 4405 PSI, BHP DIFFERENTIAL 1395 PSI, TOTAL CLEAN VOLUME PUMPED 1216 BBL, TOTAL PROPPANT PLACED 144067 LBS, 100 MESH 3000 LBS, 16/20 - 141067 LBS, AVG PSI 2879 PSI, AVG RATE 34.8 BPM 09:00 09:42 0.70 COMPZN, STIM PUMP P STAGE 19, BALL 18 - 2.710" ON SEAT AT 1377 JSV, 5 BBL EARLY, SURFACE PEAK 4919 PSI, SURFACE DIFFERENTIAL 2655 PSI, BHP PEAK 6014 PSI, BHP DIFFERENTIAL 2330 PSI, TOTAL CLEAN VOLUME PUMPED 1117 BBL, TOTAL PROPPANT PLACED 141777 LBS, 100 MESH 3000 LBS, 16/20 - 138777 LBS, AVG PSI 2720 PSI, AVG RATE 34.6 BPM 09:42 10:18 0.60 COMPZN, STIM PUMP P STAGE 20, BALL 19 - 2.749" ON SEAT AT 2780 JSV, 3 BBL EARLY, SURFACE PEAK 5052 PSI, SURFACE DIFFERENTIAL 2783 PSI, BHP PEAK 6076 PSI, BHP DIFFERENTIAL 2427 PSI, TOTAL CLEAN VOLUME PUMPED 1118 BBL, TOTAL PROPPANT PLACED 143059 LBS, 100 MESH 3000 LBS, 16/20 - 140059 LBS, AVG PSI 2662 PSI, AVG RATE 35.1 BPM 10:18 10:54 0.60 COMPZN, STIM PUMP P STAGE 21, BALL 20 - 2.787" ON SEAT AT 3925 JSV, 7 BBL EARLY, SURFACE PEAK 4707 PSI, SURFACE DIFFERENTIAL 2708 PSI, BHP PEAK 6121 PSI, BHP DIFFERENTIAL 2609 PSI, TOTAL CLEAN VOLUME PUMPED 1128 BBL, TOTAL PROPPANT PLACED 142203 LBS, 100 MESH 3000 LBS, 16/20 - 139203 LBS, AVG PSI 2444 PSI, AVG RATE 34.9 BPM 10:54 11:30 0.60 COMPZN, STIM PUMP P STAGE 22, BALL 21 - 2.826" ON SEAT AT 5212 JSV, 4 BBL EARLY, SURFACE PEAK 4789 PSI, SURFACE DIFFERENTIAL 2720 PSI, BHP PEAK 5944 PSI, BHP DIFFERENTIAL 2444 PSI, TOTAL CLEAN VOLUME PUMPED 1139 BBL, TOTAL PROPPANT PLACED 142939LBS, 100 MESH 3000 LBS, 16/20 - 139939 LBS, AVG PSI 2287 PSI, AVG RATE 35.8 BPM 11:30 12:06 0.60 COMPZN, STIM PUMP P STAGE 23, BALL 22 - 2.866" ON SEAT AT 6509 JSV, 4 BBL EARLY, SURFACE PEAK 4206 PSI, SURFACE DIFFERENTIAL 2181 PSI, BHP PEAK 5365 PSI, BHP DIFFERENTIAL 1919 PSI, TOTAL CLEAN VOLUME PUMPED 1243 BBL, TOTAL PROPPANT PLACED 143127 LBS, 100 MESH 3000 LBS, 16/20 - 140127 LBS, AVG PSI 2214 PSI, AVG RATE 36.7 BPM Page 2/2 3S-602 Report Printed: 5/13/2025 Daily STIM Report ORIG SPUD DATE: [ 2/26/2025 ] DRLG RIG RELEASE: [ 3/24/2025 ] ON PRODUCTION: [ ] DAYS FROM SPUD: [ 54.44 ] REPORT # [ 12] REPORT DATE: [ 4/21/2025] Time Log Start Time End Time Dur (hr) Phase Activity Code Time P- T-X Operation 12:06 13:30 1.40 COMPZN, STIM PUMP P ISIP-3188 PSI 5 MIN-3148 PSI 10 MIN-3122 PSI 15 MIN-3103 PSI 20 MIN-3089 PSI 25 MIN-3078 PSI 30 MIN- 3066 PSI 30 BBL DIESEL FREEZE PROTECT ON TUBING 13:30 23:59 10.49 COMPZN, STIM DMOB P BLOW DOWN EQUIPMENT/IRON, RIG DOWN STANDING IRON, RIG DOWN FRONT YARD IRON, RELOAD CHEMICALS FOR NEXT JOB. Report Fluids Summary Fluid To well (bbl) Cum to Well (bbl) DIESEL 30.0 61.0 SEAWATER 6,965.0 14,482.0 Contractor Rig Name/# Rig Supervisor Rig Accept Date RR Date Rig Type LRS 74-H BURKETT, CHAD,Wells Supervisor 4/11/2025 06:00 4/11/2025 14:00 PUMPING HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/11/2025 14:00 4/11/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/12/2025 00:00 4/12/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/13/2025 00:00 4/13/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/14/2025 00:00 4/14/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/15/2025 00:00 4/15/2025 15:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/16/2025 00:00 4/16/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/17/2025 00:00 4/17/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/18/2025 00:00 4/18/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/19/2025 00:00 4/19/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/20/2025 00:00 4/20/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/21/2025 00:00 4/21/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/22/2025 00:00 4/22/2025 12:00 FRAC Offline Activities Type Subtype Des Start Date End Date FRAC FRAC EQUIP FRAC RELOAD ACTIVITIES 4/15/2025 16:00 4/16/2025 23:59 PUMPING 74-H 4/20/2025 06:00 4/21/2025 14:00 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) 18 4/21/2025 08:17 4/21/2025 09:03 9,925.6 9,929.9 143,000.0 143,947.0 1,265.21 1,418.19 19 4/21/2025 09:03 4/21/2025 09:40 9,402.5 9,406.9 143,000.0 141,668.0 1,117.29 1,267.87 20 4/21/2025 09:40 4/21/2025 10:17 8,879.9 8,884.2 143,000.0 142,923.0 1,118.26 1,270.17 21 4/21/2025 10:17 4/21/2025 10:54 8,358.2 8,362.5 143,000.0 142,132.0 1,128.33 1,279.37 22 4/21/2025 10:54 4/21/2025 11:31 7,878.1 7,882.4 143,000.0 142,870.0 1,139.45 1,291.27 23 4/21/2025 11:31 4/21/2025 12:11 7,399.7 7,404.1 143,000.0 143,057.8 1,272.76 1,424.77 Page 1/1 3S-602 Report Printed: 5/13/2025 Daily STIM Report ORIG SPUD DATE: [ 2/26/2025 ] DRLG RIG RELEASE: [ 3/24/2025 ] ON PRODUCTION: [ ] DAYS FROM SPUD: [ 54.94 ] REPORT # [ 13] REPORT DATE: [ 4/22/2025] API / UWI 5010320906 Original KB/RT Elevation (ft) 67.70 Ground Elevation (ft) 27.70 Original Spud Date 2/26/2025 Primary Job Type INITIAL COMPLETION Secondary Job Type Total AFE (Cost) 8,443,262.00 AFE / RFE / Maint.# GKA.00108.E.W001.CO.I W;GKA.00108.E.W001.C O.IS;GKA.00108.E.W001. CO.IF Network/Order Number 10463819;10441038;104 63818 AFE+Supp Amt (Cost) 8,443,262.00 Daily Cost Total (Cost) 145,100.00 Cumulative Cost (Cost) 4,297,510.27 Weather Temperature (°F) Road Condition Wind Last 24hr Summary RIG DOWN BALL LAUNCHER, RIG DOWN FRONT YARD IRON, BREAK BACK TREATING LINE TO 3S-714 24hr Forecast General Remarks ZX Code ZX02 Fracturing Contact Name Title Mobile OSSELBURN, DEREK SL 724-494-3261 LAWSON, JACOB Supervisor 971-606-0075 Time Log Start Time End Time Dur (hr) Phase Activity Code Time P- T-X Operation 00:00 07:00 7.00 COMPZN, STIM DMOB P RIG DOWN FRONT YARD IRON, CLEAN UP AROUND EQUIPMENT 07:00 12:00 5.00 COMPZN, STIM DMOB P RIG DOWN BALL LAUNCHER, CONTINUE TO RIG DOWN/BREAK BACK IRON TO 3S- 714 Report Fluids Summary Fluid To well (bbl) Cum to Well (bbl) DIESEL 61.0 SEAWATER 14,482.0 Contractor Rig Name/# Rig Supervisor Rig Accept Date RR Date Rig Type LRS 74-H BURKETT, CHAD,Wells Supervisor 4/11/2025 06:00 4/11/2025 14:00 PUMPING HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/11/2025 14:00 4/11/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/12/2025 00:00 4/12/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/13/2025 00:00 4/13/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/14/2025 00:00 4/14/2025 23:59 FRAC HES Frac Equipment BURKETT, CHAD,Wells Supervisor 4/15/2025 00:00 4/15/2025 15:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/16/2025 00:00 4/16/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/17/2025 00:00 4/17/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/18/2025 00:00 4/18/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/19/2025 00:00 4/19/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/20/2025 00:00 4/20/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/21/2025 00:00 4/21/2025 23:59 FRAC HES Frac Equipment FAUR, DAN,Wells Supervisor 4/22/2025 00:00 4/22/2025 12:00 FRAC Offline Activities Type Subtype Des Start Date End Date FRAC FRAC EQUIP FRAC RELOAD ACTIVITIES 4/15/2025 16:00 4/16/2025 23:59 PUMPING 74-H 4/20/2025 06:00 4/21/2025 14:00 t >>ED W/η^ Zs/ KZ Zη&/ >ED ^ Zs/ ^Z/Wd/KE >/s Z> ^Z/Wd/KE ddzW d >K'' K>KZWZ/Ed^ ͲĞůŝǀĞƌLJ3S-602 50-103-20906-00-00 225-003 KUPARUK RIVER MEMORY Top Of CementPROCESSED 19-Mar-25 1dƌĂŶƐŵŝƚƚĂůZĞĐĞŝƉƚͺͺͺͺͺͺͺͺͺͺͺͺͺͺͺͺͺͺͺͺͺͺͺͺͺͺͺͺͺͺͺͺ yͺͺͺͺͺͺͺͺͺͺͺͺͺͺͺͺͺͺͺͺͺͺͺͺͺͺͺͺͺͺͺͺͺͺͺͺͺͺͺͺͺͺͺͺWƌŝŶƚEĂŵĞ ^ŝŐŶĂƚƵƌĞ ĂƚĞWůĞĂƐĞƌĞƚƵƌŶǀŝĂĐŽƵƌŝĞƌŽƌƐŝŐŶͬƐĐĂŶĂŶĚĞŵĂŝůĂĐŽƉLJƚŽ^ĐŚůƵŵďĞƌŐĞƌ͘ďŚĂƚƚĂĐŚĂƌLJĂΛƐůď͘ĐŽŵ^>ƵĚŝƚŽƌͲdƌĂŶƐŵŝƚƚĂůZĞĐĞŝƉƚƐŝŐŶĂƚƵƌĞĐŽŶĨŝƌŵƐƚŚĂƚĂƉĂĐŬĂŐĞ;ďŽdž͕ĞŶǀĞůŽƉĞ͕ĞƚĐ͘ͿŚĂƐďĞĞŶƌĞĐĞŝǀĞĚĂŶĚƚŚĞĐŽŶƚĞŶƚƐŽĨƚŚĞƉĂĐŬĂŐĞŚĂǀĞďĞĞŶǀĞƌŝĨŝĞĚƚŽŵĂƚĐŚƚŚĞŵĞĚŝĂŶŽƚĞĚĂďŽǀĞ͘dŚĞƐƉĞĐŝĨŝĐĐŽŶƚĞŶƚŽĨƚŚĞƐĂŶĚͬŽƌŚĂƌĚĐŽƉLJƉƌŝŶƚƐŵĂLJŽƌŵĂLJŶŽƚŚĂǀĞďĞĞŶǀĞƌŝĨŝĞĚĨŽƌĐŽƌƌĞĐƚŶĞƐƐŽƌƋƵĂůŝƚLJůĞǀĞůĂƚƚŚŝƐƉŽŝŶƚ͘η^ĐŚůƵŵďĞƌŐĞƌͲWƌŝǀĂƚĞ225-003T40247Gavin GluyasDigitally signed by Gavin Gluyas Date: 2025.04.01 08:41:57 -08'00' T + 1 337.856-7201 1058 Baker Hughes Drive Broussard, LA 70518, USA Mar 28, 2025 AOGCC Attention: Meredith Guhl/ Gavin Gluyas 333 W. 7th Ave., Suite 100 Anchorage, Alaska 99501-3539 Subject:Final Log Distribution for ConocoPhillips Alaska, Inc. KRU 3S-602 Kuparuk River API #: 50-103-20906-00-00 Permit No: 225-003 Rig: Doyon 25 The final Coil deliverables were uploaded via https://copsftp.sharefile.com/ for the above well. Items delivered: Digital Las Data, Graphic Images CGM/PDF and Survey Files. Thank you. Signature of receiver & date received: Please return transmittal letter to: Hampton, Jerissa Jerissa.Hampton@conocophillips.com Luis G Arismendi Luis.arismendi@bakerhughes.com 225-003 T40244 Gavin Gluyas Digitally signed by Gavin Gluyas Date: 2025.03.28 09:46:24 -08'00' 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 3S-602 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): 18732 5204 18723 5204 1915 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 3/24/2025 Length AOGCC USE ONLY 11590 Tubing Grade:Tubing MD (ft): TNT Packer: 6861' MD/ 5106' TVD SLZXP: 9973' MD / 5138' 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: STATE OF ALASKA ALASKA OIL AND GAS CONSERVATION COMMISSION APPLICATION FOR SUNDRY APPROVALS 20 AAC 25.280 ADL380107 / ADL380106 / ADL 393883 225-003 P.O. Box 100360, Anchorage, Alaska 99510-0360 50-103-20906-00-00 ConocoPhillips Alaska Inc. Kuparuk Field Will perfs require a spacing exception due to property boundaries? Current Pools: Size Proposed Pools: MD PRESENT WELL CONDITION SUMMARY 6890 5210 117 2527 4778 117 2930 TVD Burst MPSP (psi):Plugs (MD): 7-5/8"4739 2890 7129 6160 20" 10-3/4" 77 969 4-1/2" 4/7/2025 1872311750 4-1/2" 5204 Halliburton TNT Prod Packer Baker SLZXP, No SSSV L-80 10860 Perforation Depth TVD (ft):Perforation Depth MD (ft): 51817-5/8" 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 325-163 By Grace Christianson at 8:09 am, Mar 25, 2025 4/7/2025 DSR-4/1/25VTL 3/27/2025 CDW 03/26/2025 10-404 SFD 3/26/2025 Fracture Stimulate *&: Jessie L. Chmielowski Digitally signed by Jessie L. Chmielowski Date: 2025.04.02 15:29:30 -08'00' 04/02/25 RBDMS JSB 040325 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) 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 COYOTR02 TRACT OPERATION COYOTR02 501032084701 3S-701A ACTIVE Injector Produced Water KUP COYOTR03 TRACT OPERATION COYOTR03 501032084800 3S-704 ACTIVE Oil KUP COYOTR05 TRACT OPERATION COYOTR05 501032088400 3S-718 ACTIVE Oil KUP COYOTR06 TRACT OPERATION COYOTR06 501032088600 3S-722 ACTIVE Injector Produced Water KUP COYOTR07 TRACT OPERATION COYOTR07 501032090300 3S-714 ACTIVE Oil KUP KRU KUPARUK RIVER UNIT 501032043200 3S-09 ACTIVE Injector Miscible Water Alternating Gas KUP KRU KUPARUK RIVER UNIT 501032043000 3S-07 ACTIVE Oil KUP KRU KUPARUK RIVER UNIT 501032044500 3S-16 ACTIVE Injector Miscible Water Alternating Gas KUP KRU KUPARUK RIVER UNIT 501032045003 3S-08C ACTIVE Oil KUP KRU KUPARUK RIVER UNIT 501032045060 3S-08CL1 ACTIVE Oil KUP MORTR02 TRACT OPERATION MORTR02 501032069500 3S-620 ACTIVE Oil KUP MORTR03 TRACT OPERATION MORTR03 501032073500 3S-613 ACTIVE Injector Produced Water KUP MORTR04 TRACT OPERATION MORTR04 501032077700 3S-612 ACTIVE Injector Miscible Water Alternating Gas KUP MORTR04 TRACT OPERATION MORTR04 501032077400 3S-611 ACTIVE Oil KUP MORTR05 TRACT OPERATION MORTR05 501032084200 3S-625 ACTIVE Injector Produced Water KUP MORTR05 TRACT OPERATION MORTR05 501032084400 3S-615 ACTIVE Oil KUP MORTR06 TRACT OPERATION MORTR06 501032086800 3S-624 ACTIVE Oil Yes Yes KUP MORTR07 TRACT OPERATION MORTR07 501032087000 3S-606 ACTIVE Injector Produced Water Yes Yes KUP MORTR08 TRACT OPERATION MORTR08 501032087500 3S-610 ACTIVE Oil KUP MORTR09 TRACT OPERATION MORTR09 501032086400 3S-617 ACTIVE Injector Produced Water Yes Yes KUP COYOTR01 TRACT OPERATION COYOTR01 501032045602 3S-24B PA Plugged and Abandoned KUP COYOTR02 TRACT OPERATION COYOTR02 501032084700 3S-701 PA Plugged and Abandoned KUP KRU KUPARUK RIVER UNIT 501032043300 3S-18 PA Plugged and Abandoned KUP KRU KUPARUK RIVER UNIT 501032043900 3S-14 PA Plugged and Abandoned Yes - P&A Yes - P&A KUP KRU KUPARUK RIVER UNIT 501032044000 3S-10 PA Plugged and Abandoned KUP KRU KUPARUK RIVER UNIT 501032036100 PALM 1 PA Plugged and Abandoned KUP KRU KUPARUK RIVER UNIT 501032036101 3S-26 PA Plugged and Abandoned KUP KRU KUPARUK RIVER UNIT 501032045400 3S-06 PA Plugged and Abandoned Yes - P&A Yes - P&A KUP KRU KUPARUK RIVER UNIT 501032045401 3S-06A PA Plugged and Abandoned Yes-P&A Yes - P&A KUP KRU KUPARUK RIVER UNIT 501032045600 3S-24 PA Plugged and Abandoned KUP KRU KUPARUK RIVER UNIT 501032045601 3S-24A PA Plugged and Abandoned KUP KRU KUPARUK RIVER UNIT 501032044400 3S-15 PA Plugged and Abandoned Yes-P&A Yes - P&A KUP KRU KUPARUK RIVER UNIT 501032044600 3S-22 PA Plugged and Abandoned KUP KRU KUPARUK RIVER UNIT 501032044800 3S-17 PA Plugged and Abandoned KUP KRU KUPARUK RIVER UNIT 501032044801 3S-17A PA Plugged and Abandoned KUP KRU KUPARUK RIVER UNIT 501032045000 3S-08 PA Plugged and Abandoned KUP KRU KUPARUK RIVER UNIT 501032045001 3S-08A PA Plugged and Abandoned KUP KRU KUPARUK RIVER UNIT 501032045002 3S-08B PA Plugged and Abandoned KUP KRU KUPARUK RIVER UNIT 501032045070 3S-08CL1PB1 PA Plugged and Abandoned KUP KRU KUPARUK RIVER UNIT 501032045200 3S-21 PA Plugged and Abandoned KUP KRU KUPARUK RIVER UNIT 501032045300 3S-23 PA Plugged and Abandoned KUP MORTR04 TRACT OPERATION MORTR04 501032077470 3S-611PB1 PA Plugged and Abandoned KUP MORTR10 TRACT OPERATION MORTR10 501032087870 3S-626PB1 PA Plugged and Abandoned KUP KRU KUPARUK RIVER UNIT 501032045800 3S-03 SUSP Suspended KUP KRU KUPARUK RIVER UNIT 501032046000 3S-19 SUSP Suspended KUP KRU KUPARUK RIVER UNIT 501032045301 3S-23A SUSP Suspended KUP MORTR10 TRACT OPERATION MORTR10 501032087800 3S-626 SUSP Suspended 3S-602 Frac Sundry Well - Wells within 1/2 Mile Buffer of Well Track 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”. Agree: Aquifers affected by this well are exempt. This well lies within the Kuparuk River Unit (KRU) boundary of 1984 that forms the basis for the aquifer exemption granted by Title 40 CFR 147.102(b)(3) according to a recent opinion by the EPA, which states in part: "In short, EPA finds that the boundary of Alaska’s aquifer exemption at 40 C.F.R. 147.102(b)(3) was determined on May 11, 1984. After a program is approved or promulgated, additions to aquifer exemptions, including boundary expansions to aquifers or parts thereof, submitted as part of a UIC program cannot change unless EPA approves those additions in accordance with EPA’s UIC program regulations (See 40 C.F.R. 144.7(b)(1) and (3)).” (Reference: Email from Evan Osborne, US EPA Region 10, to Steve Davies, AOGCC, dated December 2, 2024.) SFD 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. Agree. SFD 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. 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 03/01/2025 was pumped with 509 barrels of 11.0 ppg lead cement and 75 barrels 15.8 ppg tail cement. This was displaced with 274 bbl 9.5 ppg spud mud. The plug bumped and the floats held. 160 bbls lost. Cement was still at surface. The 7-5/8” casing cement report on 03/08/2025 shows that the job was pumped as designed, indicating competent cementing operations. The cement job was pumped with 104 barrels of 14.0 ppg lead cement, followed with 31 barrels of 15.3 ppg tail cement. This was displaced with 322 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 @ 4,500 MD (3,610’ TVD). 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. SECTION 7 – PRESSURE TEST INFORMATION AND PLANS TO PRESSURE- TEST CASINGS AND TUBINGS INSTALLED IN THE WELL 20 AAC 25.283(a)(7) On 03/03/2025 the 10-3/4” casing was pressure tested to 3,000 psi for 30 minutes On 03/09/2025 the 7-5/8” casing was pressure tested to 4,000 psi for 30 minutes. On 03/23/2025 the 4-1/2” tubing was pressure tested to 4,200 psi. On 03/23/2025 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 211 ft TVD over the course of the lateral section of well 3S-602, from where it intersects the top formation at 7,118’ MD (5,111’ 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 718’ TVD along the 3S-602 trajectory. The top of the Torok confining interval in the well starts at 4,599’ TVDSS (6,000’ MD). 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 5,270 ft TVDSS at the heel while it was intersected at 5,260 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: 3S-624: The 7-5/8” casing cement report on 12/24/2023 shows that the job was pumped as designed, indicating competent cementing operations. The cement job was pumped with 125 barrels of 15.3ppg primary cement with LCM and 22 barrels of 15.3ppg primary cement without LCM. The plug was bumped and the floats held. A cement bond log indicates competent cement with a cement top @ 3,435’ MD (2,778’ TVD). 3S-606: The 7-5/8” casing cement report on 2/11/2024 shows that the job was pumped as designed, indicating competent cementing operations. The cement job was pumped with 111 barrels of 15.3 ppg with BM-II (Bridge Maker II), followed with 29 barrels of 15.3 ppg without BMII. The plug was bumped, pressure increased to 1500 psi and held for 5 minutes. A cement bond log indicates competent cement with a cement top @ 3,950 MD (3,164’ TVD). 3S-617: The 7 & 5/8” casing cement report on 11/5/2023 shows that the job was pumped as designed, indicating competent cementing operations. The cement job was pumped with 142 barrels of 15.3 ppg. The plug was not bumped. Pressure was being monitored and no pressure built up indicating that the floats held. A cement bond log indicates competent cement with a cement top @ 3,841’ MD (3,157’ TVD). 3S-14: ConocoPhillips Alaska, Inc. performed Plug and Abandonment operations on 3S-14, commencing operations on 8/9/2023 and completing the Plug and Abandonment on January 18, 2024. The top cement job was performed on 12/24/2023. The casing was cemented with TOC at 3,514’ MD (tag depth). Source: 202-221 Laserfiche WebLink 3S-06/-06A: ConocoPhillips Alaska, Inc. performed Plug and Abandonment operations on 3S-06 and 3S-06A (sidetrack from 3S-06 on 5/14/2003), commencing operations on 9/4/2023 and completing the Plug and Abandonment on 10/16/2023. The top cement job was performed on 9/30/2023. The casing was cemented with TOC at 5,215’ MD (tag depth). Source: 203-088 Laserfiche WebLink 3S-15: The well is targeting Kuparuk formation. The well is completely plugged and abandoned per state regulations on 9/8/2020. Per Form 10-407 report on the AOGCC website, casing was cemented with TOC at 297’ MD based on observation from THA (Tubing Head Adapter ). Top cement job was performed to surface on 8/30/2020. The 7” CBL log data was re-evaluated. The log was run from 7,650’ to 8,202’ MD. The effective top of the CBL was 7,807’ MD where the WLEG was entered. The top of quality cement is confirmed at 8,130’ MD (5,923’ TVDRKB), above this poor cement distribution was seen to the WLEG. We have no data to evaluate cement coverage across the Moraine and Coyote intervals. However, given the vertical and longitudinal orientation of our planned stimulation operations in both zones, the hydraulic fractures will not intersect the 3S- 15 well in either the Moraine or Coyote sand. Source: 202-254 Laserfiche WebLink 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 no faults or conductive fracture zones transect the Torok Oil Pool reservoir within one half mile radius of the 3S- 602 wellbore trajectory If there is any indication that a fracture has intersected the 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) 3S-602 was completed in March 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 ball 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. Balls 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 is tested to ~10,000 psi post-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 2,370’ MD/ 2,148’ 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 23 by following attached pump schedule at ~37 bpm with a maximum expected treating pressure of ~7,050 psi. 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 70.39430569LEASE3S-602SALES ORDERBHST (°F)140LONG-150.1949722FORMATIONMoraineDATE 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-6TreatmentStage Fluid Stage Proppant Conc Rate Volume Volume Volume Total Time TimeCrosslinker Crosslinker Surfactant Buffer Gel Breaker BreakerBiocideInterval 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-In1:56:32 1-2 Freeze Protect Prime Up Pressure Test 5 1,000 24 24 0:04:46 1:56:32 1-3 Shut-In Shut-In1:51:47 1-4 30# Linear Arsenal Sleeve Shift 5 1,260 30 30 0:06:00 1:51:47 1.00 0.50 30.00 2.00 2.000.151-5 30# Linear DFIT 10 2,100 50 50 0:05:00 1:45:47 1.00 0.50 30.00 2.00 2.000.151-6 Shut-In Shut-In1:40:47 1-7 Shut-In Step Rate Test 15 8,400 200 200 0:13:20 1:40:47 1-8 30# Hybor G-i Establish Stable Fluid 15 8,400 200 200 0:13:20 1:27:27 1.00 0.25 1.00 0.50 30.00 2.00 2.000.151-9 30# Hybor G-i Pad 37 24,250 577 577 0:15:36 1:14:07 1.00 0.25 1.00 0.50 30.00 2.00 2.000.151-10 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 0.50 30.00 2.00 2.000.151-11 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 0.50 30.00 2.00 2.000.151-12 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 0.50 30.00 2.00 2.000.151-13 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 0.50 30.00 2.00 2.000.151-14 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 0.50 30.00 2.00 2.000.151-15 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 0.50 30.00 2.00 2.000.151-16 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 0.50 30.00 2.00 2.000.151-17 30# Hybor G-i Spacer and Dart Drop 37 1,260 30 30 0:00:49 0:00:49 1.00 0.25 1.00 0.50 30.00 2.00 2.000.152-1 30# Hybor G-i Pad 37 23,550 561 561 0:15:09 1:12:42 1.00 0.25 1.00 0.50 30.00 2.00 2.000.152-2 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:57:33 1.00 0.25 1.00 0.50 30.00 2.00 2.000.152-3 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 12,000 286 298 12,000 0:08:04 0:49:45 1.00 0.25 1.00 0.50 30.00 2.00 2.000.152-4 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 15,000 357 389 30,000 0:10:32 0:41:40 1.00 0.25 1.00 0.50 30.00 2.00 2.000.152-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 16,600 395 448 49,800 0:12:09 0:31:08 1.00 0.25 1.00 0.50 30.00 2.00 2.000.152-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 7,500 179 210 30,000 0:05:42 0:19:00 1.00 0.25 1.00 0.50 30.00 2.00 2.000.152-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 6,200 148 177 27,900 0:04:49 0:13:17 1.00 0.25 1.00 0.50 30.00 2.00 2.000.152-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 5,220 124 152 26,100 0:04:07 0:08:29 1.00 0.25 1.00 0.50 30.00 2.00 2.000.152-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 4,400 105 130 24,200 0:03:32 0:04:21 1.00 0.25 1.00 0.50 30.00 2.00 2.000.152-10 30# Hybor G-i Spacer and Dart Drop 37 1,260 30 30 0:00:49 0:00:49 1.00 0.25 1.00 0.50 30.00 2.00 2.000.153-1 30# Hybor G-i Pad 37 22,650 539 539 0:14:35 1:20:52 1.00 0.25 1.00 0.50 30.00 2.00 2.000.153-2 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 1:06:17 1.00 0.25 1.00 0.50 30.00 2.00 2.000.153-3 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 12,000 286 298 12,000 0:08:04 0:58:29 1.00 0.25 1.00 0.50 30.00 2.00 2.000.153-4 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 15,000 357 389 30,000 0:10:32 0:50:24 1.00 0.25 1.00 0.50 30.00 2.00 2.000.153-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 14,000 333 378 42,000 0:10:14 0:39:52 1.00 0.25 1.00 0.50 30.00 2.00 2.000.153-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 10,000 238 281 40,000 0:07:37 0:29:38 1.00 0.25 1.00 0.50 30.00 2.00 2.000.153-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 8,000 190 233 40,000 0:06:19 0:22:01 1.00 0.25 1.00 0.50 30.00 2.00 2.000.153-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 6,000 143 181 36,000 0:04:55 0:15:42 1.00 0.25 1.00 0.50 30.00 2.00 2.000.153-9 30# Hybor G-i Flush 37 11,320 270 270 0:07:17 0:10:47 1.00 0.25 1.00 0.50 30.00 2.00 2.000.153-10 Freeze Protect Freeze Protect 10 1,470 35 35 0:03:30 0:03:30 3-11 Shut-In Shut-InInterval 1Moraine@ 18671.17 - 18675.51 ft 138.8 °F"Alpha SleeveInterval 2Moraine@ 18190.6 - 18194.94 ft 138.9 °F"Frac Sleeve 1Interval 3Moraine@ 17709.27 - 17713.61 ft 138.7 °F"Frac Sleeve 2Liquid AdditivesDry Additives50-103-20906Conoco Phillips - 3S-602Planned Design1 CUSTOMERConoco Phillips FALSEAPIBFD (lb/gal)8.48LAT 70.39430569LEASE3S-602SALES ORDERBHST (°F)140LONG-150.1949722FORMATIONMoraineDATE 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-6TreatmentStage Fluid Stage Proppant Conc Rate Volume Volume Volume Total Time TimeCrosslinker Crosslinker Surfactant Buffer Gel Breaker BreakerBiocideInterval Number Description Description Description(ppg) (bpm) (gal) (bbl) (bbl) (lbs) (hh:mm:ss) (hh:mm:ss)(gpt) (gpt) (gpt) (gpt) (ppt) (ppt) (ppt) (ppt)Liquid AdditivesDry Additives50-103-209064-1 Shut-In Shut-In1:20:35 4-2 Freeze Protect Prime Up Pressure Test 5 1,000 24 24 0:04:46 1:20:35 4-3 Shut-In Shut-In1:15:49 4-4 30# Linear Spacer and Dart Drop 15 1,260 30 30 0:02:00 1:15:49 1.00 0.50 30.00 2.00 2.000.154-5 30# Hybor G-i Establish Stable Fluid 15 8,400 200 200 0:13:20 1:13:49 1.00 0.25 1.00 0.50 30.00 2.00 2.000.154-6 30# Hybor G-i Pad 37 17,480 416 416 0:11:15 1:00:29 1.00 0.25 1.00 0.50 30.00 2.00 2.000.154-7 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:49:14 1.00 0.25 1.00 0.50 30.00 2.00 2.000.154-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 8,500 202 211 8,500 0:05:43 0:41:26 1.00 0.25 1.00 0.50 30.00 2.00 2.000.154-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 8,500 202 220 17,000 0:05:58 0:35:43 1.00 0.25 1.00 0.50 30.00 2.00 2.000.154-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 8,000 190 216 24,000 0:05:51 0:29:44 1.00 0.25 1.00 0.50 30.00 2.00 2.000.154-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 9,000 214 253 36,000 0:06:51 0:23:53 1.00 0.25 1.00 0.50 30.00 2.00 2.000.154-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 8,000 190 233 40,000 0:06:19 0:17:02 1.00 0.25 1.00 0.50 30.00 2.00 2.000.154-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 7,000 167 211 42,000 0:05:44 0:10:43 1.00 0.25 1.00 0.50 30.00 2.00 2.000.154-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37 5,000 119 154 32,500 0:04:10 0:04:59 1.00 0.25 1.00 0.50 30.00 2.00 2.000.154-15 30# Hybor G-i Spacer and Dart Drop 37 1,260 30 30 0:00:49 0:00:49 1.00 0.25 1.00 0.50 30.00 2.00 2.000.155-1 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 2.000.155-2 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 2.000.155-3 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 2.000.155-4 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 2.000.155-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.000 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 2.000.155-6 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 2.000.155-7 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 2.000.155-8 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 2.000.155-9 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 2.000.155-10 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 2.000.155-11 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 2.000.155-12 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 2.000.155-13 30# Hybor G-i Spacer and Dart Drop 37 1,260 30 30 0:00:49 0:00:49 1.00 0.25 1.00 0.50 30.00 2.00 2.000.156-1 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 2.000.156-2 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 2.000.156-3 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 2.000.156-4 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 2.000.156-5 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 2.000.156-6 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 2.000.156-7 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 2.000.156-8 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 2.000.156-9 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 2.000.156-10 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 2.000.156-11 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 2.000.156-12 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 2.000.156-13 30# Hybor G-i Spacer and Dart Drop 37 1,260 30 30 0:00:49 0:00:49 1.00 0.25 1.00 0.50 30.00 2.00 2.000.157-1 30# Hybor G-i Pad 37 9,710 231 231 0:06:15 0:56:56 1.00 0.25 1.00 0.50 30.00 2.00 2.000.157-2 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:50:41 1.00 0.25 1.00 0.50 30.00 2.00 2.000.157-3 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.0000 37 2,000 48 50 2,000 0:01:21 0:42:53 1.00 0.25 1.00 0.50 30.00 2.00 2.000.157-4 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 2,500 60 65 5,000 0:01:45 0:41:32 1.00 0.25 1.00 0.50 30.00 2.00 2.000.157-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 4,000 95 108 12,000 0:02:56 0:39:47 1.00 0.25 1.00 0.50 30.00 2.00 2.000.157-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 4,850 115 136 19,400 0:03:41 0:36:51 1.00 0.25 1.00 0.50 30.00 2.00 2.000.157-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 5,000 119 143 22,500 0:03:53 0:33:10 1.00 0.25 1.00 0.50 30.00 2.00 2.000.157-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 5,410 129 158 27,050 0:04:17 0:29:17 1.00 0.25 1.00 0.50 30.00 2.00 2.000.157-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 5,500 131 163 30,250 0:04:26 0:25:00 1.00 0.25 1.00 0.50 30.00 2.00 2.000.157-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 5,800 138 175 34,800 0:04:45 0:20:35 1.00 0.25 1.00 0.50 30.00 2.00 2.000.157-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37 4,000 95 123 26,000 0:03:20 0:15:50 1.00 0.25 1.00 0.50 30.00 2.00 2.000.157-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37 3,000 71 94 21,000 0:02:33 0:12:29 1.00 0.25 1.00 0.50 30.00 2.00 2.000.157-13 30# Linear Flush 37 10,011 238 238 0:06:27 0:09:57 1.00 0.50 30.00 2.00 2.000.157-14 Freeze Protect Freeze Protect 10 1,470 35 35 0:03:30 0:03:30 7-15 Shut-In Shut-InInterval 4Moraine@ 17229.72 - 17234.06 ft 138.6 °F"Frac Sleeve 3Interval 5Moraine@ 16707.05 - 16711.39 ft 138.6 °F"Frac Sleeve 4Interval 6Moraine@ 16184.78 - 16189.12 ft 138.7 °F"Frac Sleeve 5Interval 7Moraine@ 15662.36 - 15666.7 ft 138.8 °F"Frac Sleeve 6Conoco Phillips - 3S-602Planned Design2 CUSTOMERConoco Phillips FALSEAPIBFD (lb/gal)8.48LAT 70.39430569LEASE3S-602SALES ORDERBHST (°F)140LONG-150.1949722FORMATIONMoraineDATE 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-6TreatmentStage Fluid Stage Proppant Conc Rate Volume Volume Volume Total Time TimeCrosslinker Crosslinker Surfactant Buffer Gel Breaker BreakerBiocideInterval Number Description Description Description(ppg) (bpm) (gal) (bbl) (bbl) (lbs) (hh:mm:ss) (hh:mm:ss)(gpt) (gpt) (gpt) (gpt) (ppt) (ppt) (ppt) (ppt)Liquid AdditivesDry Additives50-103-209068-1 Shut-In Shut-In1:25:56 8-2 Freeze Protect Prime Up Pressure Test 5 1,000 24 24 0:04:46 1:25:56 8-3 Shut-In Shut-In1:21:10 8-4 30# Linear Spacer and Dart Drop 15 1,260 30 30 0:02:00 1:21:10 1.00 0.50 30.00 2.00 2.000.158-5 30# Linear Displacement 15 9,678 230 230 0:15:22 1:19:10 1.00 0.50 30.00 2.00 2.000.158-6 30# Linear DFIT 15 1,680 40 40 0:02:40 1:03:48 1.00 0.50 30.00 2.00 2.000.158-7 30# Hybor G-i Establish Stable Fluid 15 8,400 200 200 0:13:20 1:01:08 1.00 0.25 1.00 0.50 30.00 2.00 2.000.158-8 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 2.000.158-9 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 2.000.158-10 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 2.000.158-11 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 2.000.158-12 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 2.000.158-13 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 2.000.158-14 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 2.000.158-15 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 2.000.158-16 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 2.000.158-17 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 2.000.158-18 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 2.000.158-19 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 2.000.158-20 30# Hybor G-i Spacer and Dart Drop 37 1,260 30 30 0:00:49 0:00:49 1.00 0.25 1.00 0.50 30.00 2.00 2.000.159-1 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 2.000.159-2 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 2.000.159-3 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 2.000.159-4 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 2.000.159-5 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 2.000.159-6 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 2.000.159-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.5000 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 2.000.159-8 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 2.000.159-9 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 2.000.159-10 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 2.000.159-11 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 2.000.159-12 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 2.000.159-13 30# Hybor G-i Spacer and Dart Drop 37 1,260 30 30 0:00:49 0:00:49 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1510-1 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 2.000.1510-2 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 2.000.1510-3 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 2.000.1510-4 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 2.000.1510-5 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 2.000.1510-6 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 2.000.1510-7 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 2.000.1510-8 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 2.000.1510-9 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 2.000.1510-10 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 2.000.1510-11 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 2.000.1510-12 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 2.000.1510-13 30# Hybor G-i Spacer and Dart Drop 37 1,260 30 30 0:00:49 0:00:49 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1511-1 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 2.000.1511-2 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 2.000.1511-3 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.0000 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 2.000.1511-4 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 2.000.1511-5 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 2.000.1511-6 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 2.000.1511-7 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 2.000.1511-8 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 2.000.1511-9 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 2.000.1511-10 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 2.000.1511-11 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 2.000.1511-12 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 2.000.1511-13 30# Hybor G-i Spacer and Dart Drop 37 1,260 30 30 0:00:49 0:00:49 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1512-1 30# Hybor G-i Pad 37 9,710 231 231 0:06:15 0:55:52 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1512-2 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:49:37 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1512-3 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 2,000 48 50 2,000 0:01:21 0:41:48 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1512-4 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 2,500 60 65 5,000 0:01:45 0:40:27 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1512-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 4,000 95 108 12,000 0:02:56 0:38:42 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1512-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 4,850 115 136 19,400 0:03:41 0:35:47 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1512-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 5,000 119 143 22,500 0:03:53 0:32:05 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1512-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 5,410 129 158 27,050 0:04:17 0:28:13 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1512-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 5,500 131 163 30,250 0:04:26 0:23:56 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1512-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 5,800 138 175 34,800 0:04:45 0:19:30 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 6.50 37 4,000 95 123 26,000 0:03:20 0:14:45 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 7.00 37 3,000 71 94 21,000 0:02:33 0:11:25 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1512-13 30# Linear Flush 37 8,344 199 199 0:05:22 0:08:52 1.00 0.50 30.00 2.00 2.000.1512-14 Freeze Protect Freeze Protect 10 1,470 35 35 0:03:30 0:03:30 12-15 Shut-In Shut-In 0.30Interval 9Moraine@ 14618.15 - 14622.49 ft 139.4 °F"Frac Sleeve 8Interval 10Moraine@ 14098.94 - 14103.28 ft 139.6 °F"Frac Sleeve 9Interval 11Moraine@ 13576.44 - 13580.78 ft 140 °F"Frac Sleeve 10Interval 8Moraine@ 15140.23 - 15144.57 ft 139.1 °F"Frac Sleeve 7Interval 12Moraine@ 13053.84 - 13058.18 ft 139.8 °F"Frac Sleeve 11Conoco Phillips - 3S-602Planned Design3 CUSTOMERConoco Phillips FALSEAPIBFD (lb/gal)8.48LAT 70.39430569LEASE3S-602SALES ORDERBHST (°F)140LONG-150.1949722FORMATIONMoraineDATE 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-6TreatmentStage Fluid Stage Proppant Conc Rate Volume Volume Volume Total Time TimeCrosslinker Crosslinker Surfactant Buffer Gel Breaker BreakerBiocideInterval Number Description Description Description(ppg) (bpm) (gal) (bbl) (bbl) (lbs) (hh:mm:ss) (hh:mm:ss)(gpt) (gpt) (gpt) (gpt) (ppt) (ppt) (ppt) (ppt)Liquid AdditivesDry Additives50-103-2090613-1 Shut-In Shut-In1:38:57 13-2 Freeze Protect Prime Up Pressure Test 5 1,000 24 24 0:04:46 1:38:57 13-3 Shut-In Shut-In1:34:11 13-4 30# Linear Spacer and Dart Drop 15 1,260 30 30 0:02:00 1:34:11 1.00 0.50 30.00 2.00 2.000.1513-5 30# Linear Displace Dart to Seat 15 8,010 191 191 0:12:43 1:32:11 1.00 0.50 30.00 2.00 2.000.1513-6 30# Linear DFIT 10 2,100 50 50 0:05:00 1:19:28 1.00 0.50 30.00 2.00 2.000.1513-7 Shut-In Shut-In1:14:28 13-8 30# Linear Step Rate Test 15 8,400 200 200 0:13:20 1:14:28 1.00 0.50 30.00 2.00 2.000.1513-9 30# Hybor G-i Establish Stable Fluid 15 8,400 200 200 0:13:20 1:01:08 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1513-10 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 2.000.1513-11 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 2.000.1513-12 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 2.000.1513-13 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 2.000.1513-14 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 2.000.1513-15 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 2.000.1513-16 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 2.000.1513-17 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 2.000.1513-18 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 2.000.1513-19 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 2.000.1513-20 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 2.000.1513-21 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 2.000.1513-22 30# Hybor G-i Spacer and Dart Drop 37 1,260 30 30 0:00:49 0:00:49 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1514-1 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 2.000.1514-2 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 2.000.1514-3 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 2.000.1514-4 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 2.000.1514-5 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 2.000.1514-6 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 2.000.1514-7 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 2.000.1514-8 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 2.000.1514-9 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 2.000.1514-10 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 2.000.1514-11 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 2.000.1514-12 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 2.000.1514-13 30# Hybor G-i Spacer and Dart Drop 37 1,260 30 30 0:00:49 0:00:49 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1515-1 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 2.000.1515-2 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 2.000.1515-3 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 2.000.1515-4 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 2.000.1515-5 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 2.000.1515-6 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 2.000.1515-7 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 2.000.1515-8 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 2.000.1515-9 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 2.000.1515-10 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 2.000.1515-11 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 2.000.1515-12 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 2.000.1515-13 30# Hybor G-i Spacer and Dart Drop 37 1,260 30 30 0:00:49 0:00:49 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1516-1 30# Hybor G-i Pad 37 3,160 75 75 0:02:02 0:40:55 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1516-2 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:38:53 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1516-3 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 1,400 33 35 1,400 0:00:57 0:31:04 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1516-4 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 1,750 42 45 3,500 0:01:14 0:30:08 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1516-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 2,800 67 76 8,400 0:02:03 0:28:54 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1516-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 3,400 81 95 13,600 0:02:35 0:26:51 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1516-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 3,500 83 100 15,750 0:02:43 0:24:16 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1516-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 3,850 92 112 19,250 0:03:03 0:21:33 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1516-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 3,800 90 113 20,900 0:03:04 0:18:30 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1516-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 4,050 96 122 24,300 0:03:19 0:15:27 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 6.50 37 2,800 67 86 18,200 0:02:20 0:12:08 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 7.00 37 2,100 50 66 14,700 0:01:47 0:09:48 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1516-13 30# Linear Flush 37 7,010 167 167 0:04:31 0:08:01 1.00 0.50 30.00 2.00 2.000.1516-14 Freeze Protect Freeze Protect 10 1,470 35 35 0:03:30 0:03:30 16-15 Shut-In Shut-InInterval 13Moraine@ 12531.21 - 12535.55 ft 139.6 °F"Frac Sleeve 12Interval 14Moraine@ 12009.52 - 12013.86 ft 139.4 °F"Frac Sleeve 13Interval 15Moraine@ 11487.28 - 11491.62 ft 139.4 °F"Frac Sleeve 14Interval 16Moraine@ 10966.12 - 10970.46 ft 139.4 °F"Frac Sleeve 15Conoco Phillips - 3S-602Planned Design4 CUSTOMERConoco Phillips FALSEAPIBFD (lb/gal)8.48LAT 70.39430569LEASE3S-602SALES ORDERBHST (°F)140LONG-150.1949722FORMATIONMoraineDATE 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-6TreatmentStage Fluid Stage Proppant Conc Rate Volume Volume Volume Total Time TimeCrosslinker Crosslinker Surfactant Buffer Gel Breaker BreakerBiocideInterval Number Description Description Description(ppg) (bpm) (gal) (bbl) (bbl) (lbs) (hh:mm:ss) (hh:mm:ss)(gpt) (gpt) (gpt) (gpt) (ppt) (ppt) (ppt) (ppt)Liquid AdditivesDry Additives50-103-2090617-1 Shut-In Shut-In0:55:49 17-2 Freeze Protect Prime Up Pressure Test 5 1,000 24 24 0:04:46 0:55:49 17-3 Shut-In Shut-In0:51:03 17-4 30# Linear Spacer and Dart Drop 15 1,260 30 30 0:02:00 0:51:03 1.00 0.50 30.00 2.00 2.000.1517-5 30# Linear Spacer and Dart Drop 15 1,260 30 30 0:02:00 0:49:03 1.00 0.50 30.00 2.00 2.000.1517-6 30# Hybor G-i Establish Stable Fluid 15 8,400 200 200 0:13:20 0:47:03 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1517-7 30# Hybor G-i Pad 37 3,160 75 75 0:02:02 0:33:43 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1517-8 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:31:41 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1517-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 1,400 33 35 1,400 0:00:57 0:23:52 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1517-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 1,750 42 45 3,500 0:01:14 0:22:56 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 3.00 37 2,800 67 76 8,400 0:02:03 0:21:42 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1517-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 3,400 81 95 13,600 0:02:35 0:19:39 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 4.50 37 3,500 83 100 15,750 0:02:43 0:17:04 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1517-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 3,850 92 112 19,250 0:03:03 0:14:21 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1517-15 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 3,800 90 113 20,900 0:03:04 0:11:18 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1517-16 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 4,050 96 122 24,300 0:03:19 0:08:15 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1517-17 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.5000 37 2,800 67 86 18,200 0:02:20 0:04:56 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1517-18 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37 2,100 50 66 14,700 0:01:47 0:02:36 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1517-19 30# Hybor G-i Spacer and Dart Drop 37 1,260 30 30 0:00:49 0:00:49 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1518-1 30# Hybor G-i Pad 37 3,160 75 75 0:02:02 0:33:43 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1518-2 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:31:41 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1518-3 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 1,400 33 35 1,400 0:00:57 0:23:52 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1518-4 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 1,750 42 45 3,500 0:01:14 0:22:56 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1518-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 2,800 67 76 8,400 0:02:03 0:21:42 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1518-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 3,400 81 95 13,600 0:02:35 0:19:39 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1518-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 3,500 83 100 15,750 0:02:43 0:17:04 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1518-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 3,850 92 112 19,250 0:03:03 0:14:21 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1518-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 3,800 90 113 20,900 0:03:04 0:11:18 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1518-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 4,050 96 122 24,300 0:03:19 0:08:15 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 6.50 37 2,800 67 86 18,200 0:02:20 0:04:56 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 7.00 37 2,100 50 66 14,700 0:01:47 0:02:36 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1518-13 30# Hybor G-i Spacer and Dart Drop 37 1,260 30 30 0:00:49 0:00:49 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1519-1 30# Hybor G-i Pad 37 3,160 75 75 0:02:02 0:33:43 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1519-2 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:31:41 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1519-3 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 1,400 33 35 1,400 0:00:57 0:23:52 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1519-4 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 1,750 42 45 3,500 0:01:14 0:22:56 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1519-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 2,800 67 76 8,400 0:02:03 0:21:42 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1519-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 3,400 81 95 13,600 0:02:35 0:19:39 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1519-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 3,500 83 100 15,750 0:02:43 0:17:04 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1519-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 3,850 92 112 19,250 0:03:03 0:14:21 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1519-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 3,800 90 113 20,900 0:03:04 0:11:18 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1519-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 4,050 96 122 24,300 0:03:19 0:08:15 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 6.50 37 2,800 67 86 18,200 0:02:20 0:04:56 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 7.00 37 2,100 50 66 14,700 0:01:47 0:02:36 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1519-13 30# Hybor G-i Spacer and Dart Drop 37 1,260 30 30 0:00:49 0:00:49 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1520-1 30# Hybor G-i Pad 37 3,160 75 75 0:02:02 0:33:43 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1520-2 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:31:41 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1520-3 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 1,400 33 35 1,400 0:00:57 0:23:52 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1520-4 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 1,750 42 45 3,500 0:01:14 0:22:56 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1520-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 2,800 67 76 8,400 0:02:03 0:21:42 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1520-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 3,400 81 95 13,600 0:02:35 0:19:39 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1520-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 3,500 83 100 15,750 0:02:43 0:17:04 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1520-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 3,850 92 112 19,250 0:03:03 0:14:21 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1520-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 3,800 90 113 20,900 0:03:04 0:11:18 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1520-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 4,050 96 122 24,300 0:03:19 0:08:15 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 6.50 37 2,800 67 86 18,200 0:02:20 0:04:56 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 7.00 37 2,100 50 66 14,700 0:01:47 0:02:36 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1520-13 30# Hybor G-i Spacer and Dart Drop 37 1,260 30 30 0:00:49 0:00:49 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1521-1 30# Hybor G-i Pad 37 3,160 75 75 0:02:02 0:33:43 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1521-2 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:31:41 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1521-3 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 1,400 33 35 1,400 0:00:57 0:23:52 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1521-4 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 1,750 42 45 3,500 0:01:14 0:22:56 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1521-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 2,800 67 76 8,400 0:02:03 0:21:42 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1521-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 3,400 81 95 13,600 0:02:35 0:19:39 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 4.50 37 3,500 83 100 15,750 0:02:43 0:17:04 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 5.00 37 3,850 92 112 19,250 0:03:03 0:14:21 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 5.50 37 3,800 90 113 20,900 0:03:04 0:11:18 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 6.00 37 4,050 96 122 24,300 0:03:19 0:08:15 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 6.50 37 2,800 67 86 18,200 0:02:20 0:04:56 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 7.00 37 2,100 50 66 14,700 0:01:47 0:02:36 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1521-13 30# Hybor G-i Spacer and Dart Drop 37 1,260 30 30 0:00:49 0:00:49 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.15Interval 17Moraine@ 10447.39 - 10451.73 ft 138.7 °F"Frac Sleeve 16Interval 18Moraine@ 9925.58 - 9929.92 ft 137.6 °F"Frac Sleeve 17Interval 19Moraine@ 9402.53 - 9406.87 ft 135.7 °F"Frac Sleeve 18Interval 20Moraine@ 8879.86 - 8884.2 ft 133.4 °F"Frac Sleeve 18Interval 21Moraine@ 8358.17 - 8362.51 ft 131.1 °F"Frac Sleeve 20Conoco Phillips - 3S-602Planned Design5 CUSTOMERConoco Phillips FALSEAPIBFD (lb/gal)8.48LAT 70.39430569LEASE3S-602SALES ORDERBHST (°F)140LONG-150.1949722FORMATIONMoraineDATE 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-6TreatmentStage Fluid Stage Proppant Conc Rate Volume Volume Volume Total Time TimeCrosslinker Crosslinker Surfactant Buffer Gel Breaker BreakerBiocideInterval Number Description Description Description(ppg) (bpm) (gal) (bbl) (bbl) (lbs) (hh:mm:ss) (hh:mm:ss)(gpt) (gpt) (gpt) (gpt) (ppt) (ppt) (ppt) (ppt)Liquid AdditivesDry Additives50-103-2090622-1 30# Hybor G-i Pad 37 3,160 75 75 0:02:02 0:39:39 1.00 0.25 1.00 0.50 30.00 2.00 2.00 0.1522-2 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:37:37 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1522-3 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 1,400 33 35 1,400 0:00:57 0:29:48 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1522-4 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 1,750 42 45 3,500 0:01:14 0:28:51 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1522-5 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 2,800 67 76 8,400 0:02:03 0:27:38 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1522-6 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 3,400 81 95 13,600 0:02:35 0:25:35 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1522-7 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 3,500 83 100 15,750 0:02:43 0:23:00 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1522-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 3,850 92 112 19,250 0:03:03 0:20:17 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1522-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 3,800 90 113 20,900 0:03:04 0:17:14 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1522-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 4,050 96 122 24,300 0:03:19 0:14:11 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1522-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37 2,800 67 86 18,200 0:02:20 0:10:52 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1522-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37 2,100 50 66 14,700 0:01:47 0:08:31 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1522-13 30# Linear Flush 37 5,036 120 120 0:03:14 0:06:44 1.00 0.50 30.00 2.00 2.000.1522-14 Freeze Protect Freeze Protect 10 1,470 35 35 0:03:30 0:03:30 0.50 30.0022-15 Shut-In Shut-In23-1 Shut-In Shut-In0:59:02 23-2 Freeze Protect Prime Up Pressure Test 5 1,000 24 24 0:04:46 0:59:02 23-3 Shut-In Shut-In0:54:17 23-4 30# Linear Spacer and Dart Drop 15 1,260 30 30 0:02:00 0:54:17 1.00 0.50 30.00 2.00 2.000.1523-5 30# Hybor G-i Establish Stable Fluid 15 8,400 200 200 0:13:20 0:52:17 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1523-6 30# Hybor G-i Pad 37 3,160 75 75 0:02:02 0:38:57 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1523-7 30# Hybor G-i Conditioning Pad 100M 0.25 37 12,000 286 289 3,000 0:07:49 0:36:55 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1523-8 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 1.00 37 1,400 33 35 1,400 0:00:57 0:29:06 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1523-9 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 2.00 37 1,750 42 45 3,500 0:01:14 0:28:10 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1523-10 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 3.00 37 2,800 67 76 8,400 0:02:03 0:26:56 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1523-11 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.00 37 3,400 81 95 13,600 0:02:35 0:24:53 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1523-12 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 4.50 37 3,500 83 100 15,750 0:02:43 0:22:18 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1523-13 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.00 37 3,850 92 112 19,250 0:03:03 0:19:35 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1523-14 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 5.50 37 3,800 90 113 20,900 0:03:04 0:16:32 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1523-15 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.00 37 4,050 96 122 24,300 0:03:19 0:13:29 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1523-16 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 6.50 37 2,800 67 86 18,200 0:02:20 0:10:10 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1523-17 30# Hybor G-i Proppant Laden Fluid Wanli 16/20 Ceramic 7.00 37 2,100 50 66 14,700 0:01:47 0:07:50 1.00 0.25 1.00 0.50 30.00 2.00 2.000.1523-18 30# Linear Flush 37 4,730 113 113 0:03:03 0:06:03 1.00 0.50 30.00 2.00 2.000.1523-19 Freeze Protect Freeze Protect 10 1,260 30 30 0:03:00 0:03:00 23-20 Shut-In Shut-In1,630,668 38,825 43,275 4,189,000Design Total (gal)Design Total (lbs)CL-28M BC-140X2 Losurf-300D MO-67 WG-36 OPTIFLO-III OPTIFLO-II BE-6-4,120,000(gal) (gal) (gal) (gal) (lbs) (lbs) (lbs) (lbs)75,91869,000Initial Design Material Volume 1,531.7 382.9 1,607.7 804.6 48,273.8 3,215.3 3,215.3 241.1-14,610-Whole Units to be ordered1,531,740-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 0.8 46.6 3.1 3.1 0.2-Min Additive Rate21:53:15 Interval 23Moraine@ 7399.73 - 7404.07 ft 126.8 °FInterval 22Moraine@ 7878.09 - 7882.43 ft 128.9 °F"Frac Sleeve 21Proppant TypeWanli 16/20 Ceramic100M---Fluid Type-30# LinearSeawaterFreeze Protect30# Hybor G-i---Conoco Phillips - 3S-602Planned Design6 Hydraulic Fracturing Fluid Product Component Information Disclosure 2025-03-20 Alaska HARRISON BAY 50-103-20906-00-00 CONOCOPHILLIPS 3S 602 -150.19497221 70.39430569 NAD83 none Oil 5200 1528275.1 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 Calcium Chloride Customer Salt Solution Flow Insurance Copper Patina Energy Tracer Oxygon HES Scavenger Ingredients Water 7732-18-5 95.00%72.26540%13012384 Corundum 1302-74-5 60.00%13.72847%2472000 Mullite 1302-93-8 40.00%9.15231%1648000 Sodium chloride 7647-14-5 5.00%3.80344%684863 Crystalline silica, quartz 14808-60-7 100.00%0.39043%70303 Guar gum 9000-30-0 100.00%0.26809%48274 Water 7732-18-5 100.00%0.12634%22750 Calcium Chloride 10043-52-4 100.00%0.05554%10000 Borate salts Proprietary 60.00%0.05403%9728 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 Water 7732-18-5 100.00%0.04721%8500 Ethanol 64-17-5 60.00%0.04070%7328 Ammonium persulfate 7727-54-0 100.00%0.03571%6430 Monoethanolamine borate 26038-87-9 100.00%0.02161%3892 Oxyalkylated nonyl phenolic resin Proprietary 30.00%0.02035%3664 Halliburton Denise Tuck Denise.Tuck @Halliburton. com 281-871-6226 Heavy aromatic petroleum naphtha 64742-94-5 30.00%0.02035%3664 Ammonium acetate 631-61-8 100.00%0.01531%2757 Sodium hydroxide 1310-73-2 30.00%0.01420%2558 Oxylated phenolic resin Proprietary 30.00%0.01071%1929 Halliburton Denise Tuck Denise.Tuck @Halliburton. com 281-871-6226 Oxyalkylated phenolic resin Proprietary 10.00%0.00678%1222 Halliburton Denise Tuck Denise.Tuck @Halliburton. com 281-871-6226 Ethylene glycol 107-21-1 30.00%0.00648%1168 Acetic acid 64-19-7 30.00%0.00459%828 Inorganic mineral 1317-65-3 5.00%0.00450%811 Potassium chloride 7447-40-7 5.00%0.00450%811 EDTA/Copper chelate Proprietary 30.00%0.00417%751 Halliburton Denise Tuck Denise.Tuck @Halliburton. com 281-871-6226 Naphthalene 91-20-3 5.00%0.00339%611 Poly(oxy-1,2-ethanediyl), alpha-(4- nonylphenyl)-omega-hydroxy-, branched 127087-87-0 5.00%0.00339%611 Flow Insurance Copper Proprietary 100.00%0.00245%442 Patina Energy Product Stewardship test@patinae nergy.com 7205324886 2-Bromo-2-nitro-1,3-propanediol 52-51-7 100.00%0.00134%241 Polymer Proprietary 1.00%0.00090%163 Halliburton Denise Tuck Denise.Tuck @Halliburton. com 281-871-6226 Gluteraldehyde 111-30-8 1.00%0.00090%163 Calcium magnesium carbonate 16389-88-1 1.00%0.00090%163 Inorganic mineral Proprietary 1.00%0.00090%163 Halliburton Denise Tuck Denise.Tuck @Halliburton. com 281-871-6226 Ammonium chloride 12125-02-9 5.00%0.00069%126 1,2,4 Trimethylbenzene 95-63-6 1.00%0.00068%123 Sodium chloride 7647-14-5 1.00%0.00047%86 C.I. pigment Orange 5 3468-63-1 1.00%0.00018%33 Ammonia 7664-41-7 1.00%0.00014%26 Sodium bisulfate 7681-38-1 0.10%0.00009%17 Methanesulfonic acid, 1-hydroxy-, sodium salt 870-72-4 0.10%0.00009%17 2,7-Naphthalenedisulfonic acid, 3- hydroxy-4-[(4-sulfor-1- naphthalenyl) azo] -, trisodium salt 915-67-3 0.10%0.00002%4 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 Magnesium nitrate 10377-60-3 0.01%0.00001%2 2-Methyl-4-isothiazolin-3-one 2682-20-4 0.01%0.00001%2 Erythorbate Proprietary CONFIDENTIAL 0.00000%0 HES * 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 directed 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: 20 AAC 25.283 Hydraulic Fracturing Application – Checklist KRU 3S-602 (PTD No. 225-003; Sundry No. 325-163) Paragraph Sub-Paragraph Section Complete? AOGCC Page 1 March , 2025 (a) Application for Sundry Approval (a)(1) Affidavit Provided with application. SFD 3/25/2025 (a)(2) Plat Provided with application. SFD 3/25/2025 (a)(2)(A) Well location Provided with application. Well lies in Sections 18, 7, and 6 of T12N, R8E, UM and Section 36 of T13N, R7E, UM. SFD 3/25/2025 (a)(2)(B) Each water well within ½ mile None: According to the Water Estate map available through DNR’s Alaska Mapper application (accessed online ), there are no wells are used for drinking water purposes are known to lie within ½ mile of the surface location of KRU 3S-602. There are no subsurface water rights or temporary subsurface water rights within 4 miles of the surface location of KRU 3S-602. SFD 3/25/2025 (a)(2)(C) Identify all well types within ½ mile Provided with application. SFD 3/25/2025 (a)(3) Freshwater aquifers: geological name; measured and true vertical depth None. This well lies within the Kuparuk River Unit boundary of 1984 that forms the basis for the aquifer exemption granted by Title 40 CFR 147.102(b)(3) according to a recent opinion by the EPA, which states in part: "In short, EPA finds that the boundary of Alaska’s aquifer exemption at 40 C.F.R. 147.102(b)(3) was determined on May 11, 1984. After a program is approved or promulgated, additions to aquifer exemptions, including boundary expansions to aquifers or parts thereof, submitted as part of a UIC program cannot change unless EPA approves those additions in accordance with EPA’s UIC program regulations (See 40 C.F.R. 144.7(b)(1) and (3)).” (Reference: Email from Evan Osborne, US EPA Region 10, to Steve Davies, AOGCC, dated December 2, 2024.) SFD 3/25/2025 (a)(4) Baseline water sampling plan None required. SFD 3/25/2025 20 AAC 25.283 Hydraulic Fracturing Application – Checklist KRU 3S-602 (PTD No. 225-003; Sundry No. 325-163) Paragraph Sub-Paragraph Section Complete? AOGCC Page 2 March , 2025 (a)(5) Casing and cementing information Provided with application. Proposed schematic attached, as built not generated to date. CDW 03/26/2025 (a)(6) Casing and cementing operation assessment 10-3/4” surface casing was cemented to plan with cement returned to surface. 7-5/8” casing cemented to plan with CBL evaluated by CPAI as TOC 4500 ft MD, SLB SonicScope evaluation results in TOC of 5181 ft MD with weaker zones of poorer cement in 6200 ft and 6800 ft depths. AOGCC cement evaluation expert reviewed the data and concurs wth the 5181 ft MD conservative TOC estimate. 4.5” production liner from 6973 ft has liner top and packer seals within 7-5/8” casing cemented interval. CDW 03/26/2025 (a)(6)(A) Casing cemented below lowermost freshwater aquifer and conforms to 20 AAC 25.030 Only exempt freshwater aquifers are present. (See Section (a)(3), above.) SFD 3/25/2025 (a)(6)( B) Each hydrocarbon zone is isolated Yes: Surface casing was set at 2,930’ MD (-2,458’ TVDSS) and cemented with 160 barrels of cement returns at surface. For KRU 3S-602, 7-5/8” intermediate casing was set at 7,129’ MD, -5,112’ TVDSS. Top of good-quality cement interpreted from the CBL is about 5,200’ MD (-4,032’ TVDSS). The Coyote interval spans from ~5,220’ to about 6,000’ MD (about -4,038’ to -4,597’ TVDSS), and the top of the Moraine reservoir lies at 7,1118’ MD (-5,109’ TVDSS). So, cement isolates each hydrocarbon zone. SFD 3/26/2025 CDW 03/26/2025 20 AAC 25.283 Hydraulic Fracturing Application – Checklist KRU 3S-602 (PTD No. 225-003; Sundry No. 325-163) Paragraph Sub-Paragraph Section Complete? AOGCC Page 3 March , 2025 (a)(7) Pressure test: information and pressure-test plans for casing and tubing installed in well Provided with application. 3850 psi MITIA 3/23/2025, 4200 psi MITT 3/23/2025. CDW 03/26/2025 (a)(8) Pressure ratings and schematics: wellbore, wellhead, BOPE, treating head Provided with application. 10K psi Frac Tree max. frac. Pressure 7050 psi. Pump knock out 7550 and GORV 8050 psi., tree test 10000 psi, lines test 9500 psi. CDW 03/26/2025 (a)(9)(A) Fracturing and confining zones: lithologic description for each zone (a)(9)(B) Geological name of each zone (a)(9)(C) and (a)(9)(D) Measured and true vertical depths (a)(9)(E) Fracture pressure for each zone Upper confining zones: 720’ true-vertical thickness (TVT) of mudstone and siltstone assigned to the Torok formation, which has a top at 6,000’ MD (-4,599’ TVDSS). Fracture gradient is expected to range from about 0.82 psi/ft (15.8 ppg EMW). Fracturing Zone: The top of the Moraine reservoir is at 7,118’ MD (-5,111 TVDSS) and it consists of an interval of thinly interbedded sandstone, siltstone, and silty shale that averages 210’ TVT in this area. Fracture gradient expected to range from about 0.65 to 0.70 psi/ft (12.5 to 13.5 ppg EMW). Lower confining zones: Lower Torok, HRZ and Kalubik shale with an aggregate TVT of about 500’. The top of the lower confining zones is estimated to lie from -5,250’ to -5,300’ TVDSS. Fracture gradient expected to range from about 0.78 to 0.94 psi/ft (15.0 to 18.0 ppg EMW). SFD 3/25/2025 (a)(10) Location, orientation, report on mechanical condition of each well that may transect the confining zones and sufficient information to determine wells will not interfere with containment of hydraulic fracturing fluid within ½ mile of the proposed wellbore trajectory It is highly unlikely that any of the wells or wellbores within a ½-mile radius will interfere with hydraulic fracturing fluids from this operation because of cement isolation and / or separation distance. There are seven wells/sidetracks within ½ mile of KRU 3S-602 that penetrate the confining intervals. CPAI has provided cementing information and zonal isolation/containment reviews. CDW 03/26/2025 20 AAC 25.283 Hydraulic Fracturing Application – Checklist KRU 3S-602 (PTD No. 225-003; Sundry No. 325-163) Paragraph Sub-Paragraph Section Complete? AOGCC Page 4 March , 2025 The operator has identified seven wells within the AOR for S-602. They are, in order of increasing distance from the Moraine reservoir open to 3S-602: KRU 3S-06 (203-057) Plugged and Abandoned Well located about 870’ from 3S-602 at Moraine reservoir level: The uppermost 80% of the Coyote interval is NOT covered by cement, but at this location it is not judged to be a significant hydrocarbon zone. The lowest 20% of the interval is covered by cement that formed the kick-off plug for the immediately redrilled well 3S-06A. The Moraine interval is isolated from the overlying Coyote and from the underlying Kuparuk sands by open-hole cement plugs, but it is also NOT covered by cement. On open-hole cement plug covers and isolates the Kuparuk sands. Given the expected maximum half-length of the induced fractures is about 410’, and that they will develop parallel to the horizontal section of this wellbore, it is highly unlikely that this well will interfere with fracturing fluids due to separation distance. KRU 3S-06A (203-088) Plugged and Abandoned Service Well located about 950’ from 3S-602 at Moraine reservoir level: Cement isolates the Moraine and Kuparuk intervals. A perf, wash, and cement-squeeze operation was successfully conducted across the uppermost 50’ of the Coyote interval and 100’ of the overlying confining interval so the Coyote interval is isolated from the overlying section. As above, separation distance will prevent this well from interfering with fracturing fluid containment. KRU 3S-606 (223-111) Active Service Well located about 1,050’ from 3S-602 at Moraine reservoir level: The Coyote is completely covered with good-quality cement bond. Moraine and Coyote are isolated by intermediate casing cement. As SFD 3/25/2025 20 AAC 25.283 Hydraulic Fracturing Application – Checklist KRU 3S-602 (PTD No. 225-003; Sundry No. 325-163) Paragraph Sub-Paragraph Section Complete? AOGCC Page 5 March , 2025 above, separation distance will prevent this well from interfering with fracturing fluid containment. KRU 3S-15 (202-254) Plugged and Abandoned Development Well located about 1,500’ from 3S-602 at Moraine level: Quality of cement across Moraine is unknown. Coyote may not be covered by cement. Kup C appears poorly cemented. Separation distance from 3S-602 at top of Moraine is about 1,500', so it is highly unlikely that this well will interfere with hydraulic fracturing fluids. KRU 3S-14 (202-221) Plugged and Abandoned Service Well located about 2,000’ from 3S-602 at Moraine level: Perf, wash, and cementing operations were conducted to cover the uppermost 50’ of Coyote and the lowermost 100’ of overlying, confining interval. The Moraine interval appears to be uncemented. The Kuparuk sands are cemented. KRU 3S-624 (PTD 223-104) Active Development Well located about 2,100’ from 3S-602 at Moraine level: Intermediate casing cement isolates the Coyote interval. The intermediate casing was set just above the reservoir in this horizontal Moraine producer, so it also isolates that interval. KRU 3S-617 (PTD 223-085 Active Service Well located about ½ mile from 3S-602 at Moraine level: Good-quality intermediate casing cement isolates Moraine and Coyote. SFD 3/25/2025 (a)(11) Faults and fractures, Sufficient information to determine no interference with containment of the hydraulic fracturing fluid within ½ mile of the proposed wellbore trajectory None. The operator has not identified any faults or fracture zones through seismic or well data within a ½-mile radius of KRU 3S-602. It is unlikely that any faults will interfere with containment of the injected fracturing fluids; however, if there are indications that a fracture has intersected a fault or natural-fracture interval during frac operations, the operator will go to flush and terminate the stage immediately. SFD 3/25/2025 20 AAC 25.283 Hydraulic Fracturing Application – Checklist KRU 3S-602 (PTD No. 225-003; Sundry No. 325-163) Paragraph Sub-Paragraph Section Complete? AOGCC Page 6 March , 2025 (a)(12) Proposed program for fracturing operation Provided with application. CDW 03/26/2025 (a)(12)(A) Estimated volume Provided with application. 43K bbl total dirty vol. 4.189M lb total proppant CDW 03/26/2025 (a)(12)(B) Additives: names, purposes, concentrations Provided with application. CDW 03/26/2025 (a)(12)(C) Chemical name and CAS number of each Provided with application. Halliburton and Patina Energy disclosures provided. CDW 03/26/2025 (a)(12)(D) Inert substances, weight or volume of each Provided with application. CDW 03/26/2025 (a)(12)(E) Maximum treating pressure with supporting info to determine appropriateness for program Simulation shows max surface pressure 7050 psi. Max. 7050 psi allowable treating pressure. Max pressure is 7550 psi to 8050 psi to Pump shutdown. With 3500 psi back pressure IA (IA popoff set 3600 psi), max tubing differential should be 3550 psi. CDW 03/26/2025 (a)(12)(F) Fractures – height, length, MD and TVD to top, description of fracturing model Provided with application. The anticipated half-lengths of the induced fractures range from 250’ to 410’ according to the Operator’s computer simulation. Computer simulation indicates the anticipated height of the induced fractures will be about 230’ (shallowest estimated TVD of about 4,859’ and deepest estimated TVD of about 4,975’), so induced fractures may penetrate into, but not through, the overlying confining layer that is about 500’ thick in this area. SFD 3/25/2025 (a)(13) Proposed program for post-fracturing well cleanup and fluid recovery Well cleanout and flowback procedure provided with application. No disposal identified. 3S road access to waste disposal sites. CDW 03/26/2025 (b)Testing of casing or intermediate casing Tested >110% of max anticipated pressure 3500 psi back pressure, tested to 3850 psi, popoff set as 3600 psi CDW 03/26/2025 20 AAC 25.283 Hydraulic Fracturing Application – Checklist KRU 3S-602 (PTD No. 225-003; Sundry No. 325-163) Paragraph Sub-Paragraph Section Complete? AOGCC Page 7 March , 2025 (c) Fracturing string (c)(1) Packer >100’ below TOC of production or intermediate casing 4.5” tubing will be anchored with a retrievable packer set at approx. 6973 ft MD with sliding sleeves planned for 7400 ft MD to 18671 ft MD. TOC in 7-5/8” casing at 4500 to 5181 ft MD with shoe at 7129 ft MD. SonicScope evaluations shows good cement at area of interest so no cement concerns. CDW 03/26/2025 (c)(2) Tested >110% of max anticipated pressure differential Tubing test of 4200 psi. Max pressure differential is estimated as 3550 psi (7050 with 3500 psi backpressure) so test of 4200 psi satisfies 110% CDW 03/26/2025 (d) Pressure relief valve Line pressure <= test pressure, remotely controlled shut-in device 9500 psi line pressure test, pump knock out 7550 psi with max. global kickout 8050 psi. IA PRV set as 3600 psi. CDW 03/26/2025 (e) Confinement Frac fluids confined to approved formations Provided with application. CDW 03/26/2025 (f) Surface casing pressures Monitored with gauge and pressure relief device IA PRV set at 3600 psi. Surface annulus open. Frac pressures continuously monitored. CDW 03/26/2025 (g) Annulus pressure monitoring & notification 500 psi criteria During hydraulic fracturing operations, all annulus pressures must be continuously monitored and recorded. If at any time during hydraulic fracturing operations the annulus pressure increases more than 500 psig above those anticipated increases caused by pressure or thermal transfer, the operator shall: CDW 03/26/2025 (g)(1) Notify AOGCC within 24 hours (g)(2) Corrective action or surveillance (g)(3) Sundry to AOGCC (h) Sundry Report (i) Reporting (i)(1) FracFocus Reporting (i)(2) AOGCC Reporting: printed & electronic 20 AAC 25.283 Hydraulic Fracturing Application – Checklist KRU 3S-602 (PTD No. 225-003; Sundry No. 325-163) Paragraph Sub-Paragraph Section Complete? AOGCC Page 8 March , 2025 (j) Post-frac water sampling plan Not required (see Section (a)(3), above). SFD 3/25/2025 (k) Confidential information Clearly marked and specific facts supporting nondisclosure Non-confidential well. SFD 3/25/2025 (l) Variances requested Modifications of deadlines, requests for variances or waivers No plan for post fracture water well analysis. Commission may require this depending on performance of the fracturing operation. 1 From:Nozaki, Manabu <Manabu.Nozaki@conocophillips.com> Sent:Thursday, March 27, 2025 4:28 PM To:AOGCC Permitting (CED sponsored); Loepp, Victoria T (OGC); Davies, Stephen F (OGC); Dewhurst, Andrew D (OGC) Cc:Dodson, Kate; Conklin, Amy A; Lee, David L; Zwarich, Nola R; Hobbs, Greg S; Nozaki, Manabu Subject:RE: [EXTERNAL]RE: 3S-602 Frac Sundry Application Follow Up Flag:Follow up Flag Status:Flagged Hi AOGCC Team, We have a change on the 3S-602 frac sundry. Now we plan to pump the 46 ResMetrics chemical tracers (23 oil tracers and 23 water tracers).. ResMetrics will send you the chemical disclosure document directly to AOGCC. Regards, Manabu From: AOGCC Permitting (CED sponsored) <aogcc.permitting@alaska.gov> Sent: Tuesday, March 25, 2025 8:20 AM To: Nozaki, Manabu <Manabu.Nozaki@conocophillips.com>; Loepp, Victoria T (OGC) <victoria.loepp@alaska.gov>; Davies, Stephen F (OGC) <steve.davies@alaska.gov>; Dewhurst, Andrew D (OGC) <andrew.dewhurst@alaska.gov> Cc: Dodson, Kate <Kate.Dodson@conocophillips.com>; Conklin, Amy A <Amy.A.Conklin@conocophillips.com>; Lee, David L <David.L.Lee@conocophillips.com> Subject: [EXTERNAL]RE: 3S-602 Frac Sundry 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. Hello, This application has been received for processing. Thank you, Grace 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 2 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: Nozaki, Manabu <Manabu.Nozaki@conocophillips.com > Sent: Monday, March 24, 2025 5:00 PM To: AOGCC Permitting (CED sponsored) <aogcc.permitting@alaska.gov>; Loepp, Victoria T (OGC) <victoria.loepp@alaska.gov>; Davies, Stephen F (OGC) <steve.davies@alaska.gov>; Dewhurst, Andrew D (OGC) <andrew.dewhurst@alaska.gov> Cc: Dodson, Kate <Kate.Dodson@conocophillips.com>; Conklin, Amy A <Amy.A.Conklin@conocophillips.com >; Lee, David L <David.L.Lee@conocophillips.com >; Nozaki, Manabu <Manabu.Nozaki@conocophillips.com> Subject: 3S-602 Frac Sundry Application AOGCC Team, We would like to submit the frac sundry application for the 3S-602. Patina Energy will send you their chemical disclosure for the chemical tracer separately. We would like to start the frac operation on April 7th. If you have any questions, please let us know. Best Regards, Manabu Nozaki | Completions Engineer, Alaska Wells | ConocoPhillips O: +1-907-265-6519 | M: +1-907-917-9567 | ATO-1578, Anchorage, AK, USA Email: Manabu.Nozaki@ConocoPhillips.com 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. 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 ConocoPhillips Alaska Inc. P.O. Box 100360 Anchorage, Alaska, 99510 Re: Kuparuk River Field, Torok Oil Pool, KRU 3S-602 ConocoPhillips Alaska Inc. Permit to Drill Number: 225-003 Surface Location: 2464 FNL, 837 FEL, S18, T12N, R8E, UM Bottomhole Location: 2596 FSL, 1210 FWL, S36, T12N, R8E, 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 AOGCCreserves 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 AOGCCspecifically 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 AOGCCorder, 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 day of )HEUXDU\, 2025. Jessie L. Chmielowski Digitally signed by Jessie L. Chmielowski Date: 2025.02.11 14:41:41 -09'00' 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: 18,985 TVD: 5205 4a. Location of Well (Governmental Section): 7. Property Designation: Surface: Top of Productive Horizon: 8. DNR Approval Number: 13. Approximate Spud Date: Total Depth:9. Acres in Property:14. Distance to Nearest Property: 4b. Location of Well (State Base Plane Coordinates - NAD 27): 10. KB Elevation above MSL (ft): 67.2 15. Distance to Nearest Well Open Surface: x- 476422 y- 5993951 Zone- 4 27.7 to Same Pool: 934' to 3S-606 16. Deviated wells: Kickoff depth: 300 feet 17. Maximum Potential Pressures in psig (see 20 AAC 25.035) Maximum Hole Angle: 92 degrees Downhole: Surface: Hole Casing Weight Grade Coupling Length MD TVD MD TVD 42" 20" 94# H40 Welded 80 40 40 120 120 13-1/2" 10-3/4" 45.5# L80 H563 2857 40 40 2857 2488 9-7/8" 7-5/8" 29.7# L80 H563 6405 40 40 6405 4929 9-7/8" 7-5/8" 33.7# P110S H563 800 6405 4929 7205 5203 6-1/2" 4-1/2" 12.6# P110-S H563 11955 7030 5156 18985 5205 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: Chris Brillon Contact Email:trevor.kelley@cop.com Wells Engineering Manager Contact Phone: 281-513-6789 Date: Permit to Drill API Number: Permit Approval Number:Date: Conditions of approval : 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 2436 P.O. Box 100360 Anchorage, Alaska, 99510-0360 2464 FNL, 837 FEL, S18 T12N R8E, UM ADL380107, ADL380106, ADL393883 STATE OF ALASKA ALASKA OIL AND GAS CONSERVATION COMMISSION PERMIT TO DRILL 20 AAC 25.005 ConocoPhillips Alaska Inc.59-52-180 KRU 3S-602 1743 FSL, 2602 FWL, S7 T12N R8E, UM 932060000, 932059000, 368561000 2596 FSL, 1210 FWL, S36 T13N R7E, UM 2448, 2437, 5760 GL / BF Elevation above MSL (ft): 18.Casing Program: Specifications Top - Setting Depth - Bottom Cement Quantity, c.f. or sacks (including stage data) Total Depth MD (ft): Total Depth TVD (ft): Plugs (measured): Effect. Depth MD (ft): Effect. Depth TVD (ft): Casing Length Size Cement Volume MD Intermediate Surface Conductor/Structural Perforation Depth MD (ft): Perforation Depth TVD (ft): Liner Production If checked, well may not be used to explore for, test, or produce coalbed methane, gas hydrates, or gas contained in shales: 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: Trevor Kelley Commission Use Only See cover letter for other requirements. Kuparuk River Field Torok Oil Pool 2/28/2025 2598' to ADL025528 387 sx of 14.0 ppg Ext. Class G + 137 sx of 15.3 ppg Class G Cement to surface with 10 yds slurry 932 sx of 11.0 ppg DeepCRETE + 272 sx of 15.8 ppg Class G 1915 Stratigraphic Test No Mud log req'd: Yes No No Directional svy req'd: Yes No hh Seabed ReportDrilling Fluid Program 20 AAC 25.050 requirements BOP SketchDrhilling Program Time v. Depth Plot Shallow Hazard Analysis Single Well Gas Hydrates No Inclination-only svy req'd: Yes No Exploratory - Oil Development - Gas Service - Supply Multiple Zone Geothermal No No &ŽƌŵϭϬͲϰϬϭZĞǀŝƐĞĚϯͬϮϬϮϭ This permit is valid for 24 months from the date of approval per 20 AAC 25.005(g) -DQ By Grace Christianson at 10:37 am, Jan 17, 2025 Diverter variance request granted per 20 AAC 20.035(h)(2) Initial BOP test to 5000 psig; subsequent BOP test to 3500 psig Annular preventer test to 2500 psig 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 BOPE testing on a 21-day interval is approved with the attached conditions DSR-1/22/25 X A.Dewhurst 27JAN25 50-103-20906-00-00 VTL 2/11/2025 225-003 ($8 2/11/2025 2/11/2025Jessie L. Chmielowski Digitally signed by Jessie L. Chmielowski Date: 2025.02.11 14:41:53 -09'00' RBDMS JSB 021325 <Zhϯ^ͲϲϬϮ 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. 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dŚĞϲͲϭͬϮΗƉƌŽĚƵĐƚŝŽŶŝŶƚĞƌǀĂůǁŝůůďĞĚƌŝůůĞĚŚŽƌŝnjŽŶƚĂůůLJĂŶĚ ŐĞŽͲƐƚĞĞƌĞĚǁŝƚŚŝŶƚŚĞDŽƌĂŝŶĞĨŽƌŵĂƚŝŽŶ͘dŚĞǁĞůůǁŝůůďĞ ĐŽŵƉůĞƚĞĚĂƐĂŶƵŶĐĞŵĞŶƚĞĚ͕ĨƌĂĐƚƵƌĞƐƚŝŵƵůĂƚĞĚWƌŽĚƵĐĞƌǁŝƚŚϰͲϭͬϮΗůŝŶĞƌ͕ĨƌĂĐƐůĞĞǀĞƐĂŶĚƐǁĞůůƉĂĐŬĞƌƐ͘dŚĞƵƉƉĞƌ ĐŽŵƉůĞƚŝŽŶǁŝůůŝŶĐůƵĚĞĂƉƌŽĚƵĐƚŝŽŶƉĂĐŬĞƌǁŝƚŚ'>D͛ƐĂŶĚĂĚŽ ǁŶŚŽůĞŐĂƵŐĞƚŝĞĚďĂĐŬƚŽƐƵƌĨĂĐĞ͘ /ƚŝƐƌĞƋƵĞƐƚĞĚƚŚĂƚĂǀĂƌŝĂŶĐĞŽĨƚŚĞĚŝǀĞƌƚĞƌƌĞƋƵŝƌĞŵĞŶƚƵŶĚĞƌϮϬϮϱ͘Ϭϯϱ;ŚͿ;ϮͿŝƐŐƌĂŶƚĞĚ͘dŚĞƌĞŚĂƐďĞĞŶŵƵůƚŝƉůĞ ǁĞůůƐĚƌŝůůĞĚŽŶƉĂĚǁŚŝĐŚŚĂǀĞŶŽƚĞŶĐŽƵŶƚĞƌĞĚĂŶLJƐŚĂůůŽǁŐĂƐŽƌŚĂĚĂŶLJŝƐƐƵĞƐƌĞůĂƚĞĚƚŽŚLJĚƌĂƚĞƐ͘ ǀĂƌŝĂŶĐĞŝƐĂůƐŽƌĞƋƵĞƐƚĞĚĨŽƌĂKW ƚĞƐƚŝŶƚĞƌǀĂůŽĨϮϭĚĂLJƐĨŽƌƚŚŝƐƉƌŽũĞĐƚ͘ŽLJŽŶϮϱƐƵƉƉŽƌƚĞĚƚŚĞW/KW ďĞƚǁĞĞŶ ǁĞůůŵĂŝŶƚĞŶĂŶĐĞƉƌŽŐƌĂŵƚŚƌŽƵŐŚKs/ĂŶĚŚĂƐŵĂŝŶƚĂŝŶĞĚϳϯйĨŝƌƐƚƚŝŵĞƉĂƐƐƌĂƚĞĂůŽŶŐǁŝƚŚĂϵϵйĞĨĨĞĐƚŝǀĞŶĞƐƐĨŽƌĂůů ĐŽŵƉŽŶĞŶƚƐƚĞƐƚĞĚŝŶϮϬϮϰƚŽĚĂƚĞ͘dŚĞǀĂƌŝĂŶĐĞĂůůŽǁƐĞĨĨĞĐƚŝǀĞĚƌŝůůŝŶŐĂŶĚĐŽŵƉůĞƚŝŽŶŽĨƚŚĞůŽŶŐůĂƚĞƌĂůŽĨƚŚŝƐǁĞůů͘ WůĞĂƐĞĨŝŶĚĂƚƚĂĐŚĞĚƚŚĞŝŶĨŽƌŵĂƚŝŽŶƌĞƋƵŝƌĞĚďLJϮϬϮϱ͘ϬϬϱ;ĂͿĂŶĚ;ĐͿĨŽƌLJŽƵƌƌĞǀŝĞǁ͘WĞƌƚŝŶĞŶƚŝŶĨŽƌŵĂƚŝŽŶ ĂƚƚĂĐŚĞĚƚŽƚŚŝƐĂƉƉůŝĐĂƚŝŽŶŝŶĐůƵĚĞƐƚŚĞĨŽůůŽǁŝŶŐ͗ 1.&ŽƌŵϭϬͲϰϬϭƉƉůŝĐĂƚŝŽŶĨŽƌWĞƌŵŝƚƚŽƌŝůůƉĞƌϮϬϮϱ͘ϬϬϱ;ĂͿ 2.WƌŽƉŽƐĞĚĚƌŝůůŝŶŐƉƌŽŐƌĂŵ 3.WƌŽƉŽƐĞĚĚƌŝůůŝŶŐĨůƵŝĚƐƉƌŽŐƌĂŵƐƵŵŵĂƌLJ 4.WƌŽƉŽƐĞĚĐŽŵƉůĞƚŝŽŶĚŝĂŐƌĂŵ 5.WƌĞƐƐƵƌĞŝŶĨŽƌŵĂƚŝŽŶĂƐƌĞƋƵŝƌĞĚďLJϮϬϮϱ͘ϬϬϱ;ĐͿ;ϰͿ;ĂͲĐͿ 6.ŝƌĞĐƚŝŽŶĂůĚƌŝůůŝŶŐͬĐŽůůŝƐŝŽŶĂǀŽŝĚĂŶĐĞŝŶĨŽƌŵĂƚŝŽŶĂƐƌĞƋƵŝ ƌĞĚďLJϮϬϮϱ͘ϬϱϬ;ďͿ /ŶĨŽƌŵĂƚŝŽŶƉĞƌƚŝŶĞŶƚƚŽƚŚĞĂƉƉůŝĐĂƚŝŽŶƚŚĂƚŝƐƉƌĞƐĞŶƚůLJŽŶĨŝůĞĂƚƚŚĞK'͗ 1.ŝĂŐƌĂŵƐŽĨƚŚĞKWĞƋƵŝƉŵĞŶƚ͕ĚŝǀĞƌƚĞƌĞƋƵŝƉŵĞŶƚĂŶĚĐŚŽŬĞŵĂŶŝĨŽůĚůĂLJŽƵƚĂƐƌĞƋƵŝƌĞĚďLJϮϬ Ϯϱ͘Ϭϯϱ;ĂͿĂŶĚ;ďͿ͘ 2.ĚĞƐĐƌŝƉƚŝŽŶŽĨƚŚĞĚƌŝůůŝŶŐĨůƵŝĚƐŚĂŶĚůŝŶŐƐLJƐƚĞŵ͘ 3.ŝĂŐƌĂŵŽĨƌŝƐĞƌƐĞƚƵƉ͘ /ĨLJŽƵŚĂǀĞĂŶLJƋƵĞƐƚŝŽŶƐŽƌƌĞƋƵŝƌĞĨƵƌƚŚĞƌŝŶĨŽƌŵĂƚŝŽŶ͕ƉůĞĂƐĞĐŽŶƚĂĐƚdƌĞǀŽƌ<ĞůůĞLJĂƚϮϴϭͲϱϭϯͲϲϳϴϵ ;ƚƌĞǀŽƌ͘ŬĞůůĞLJΛĐŽƉ͘ĐŽŵͿŽƌŚƌŝƐƌŝůůŽŶĂƚϵϬϳͲϮϲϱͲϲϭϮϬ͘ ^ŝŶĐĞƌĞůLJ͕ĐĐ͗ ϯ^ͲϲϬϮtĞůů&ŝůĞͬ:ĞŶŶĂdĂLJůŽƌ dKϭϴϬϰ tŝůů ĂƌŚĂƌƚ dKϭϱϱϮ dƌĞǀŽƌ<ĞůůĞLJŚƌŝƐƌŝůůŽŶ dKϭϱϰϴ ƌŝůůŝŶŐ ŶŐŝŶĞĞƌ ǀĂƌŝĂŶĐĞŽĨƚŚĞĚŝǀĞƌƚĞƌƌĞƋƵŝƌĞŵĞŶƚ ϯ^ͲϲϬϮK'ϭϬͲϰϬϭW ϭͬϭϰͬϮϬϮϱ ϯ^ͲϲϬϮK'ϭϬͲϰϬϭWϭͮϭϮ ϯ^ͲϲϬϮtĞůůWůĂŶ ƉƉůŝĐĂƚŝŽŶĨŽƌWĞƌŵŝƚƚŽƌŝůů dĂďůĞŽĨŽŶƚĞŶƚƐ 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ϭϱ͘WƌŽƉŽƐĞĚŽŵƉůĞƚŝŽŶ^ĐŚĞŵĂƚŝĐ͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘͘ϭϮ ϯ^ͲϲϬϮK'ϭϬͲϰϬϭW ϭͬϭϰͬϮϬϮϱ ϯ^ͲϲϬϮK'ϭϬͲϰϬϭWϮͮϭϮ ϭ͘ tĞůůEĂŵĞ ZĞƋƵŝƌĞŵĞŶƚƐŽĨϮϬϮϱ͘ϬϬϱ;ĨͿ dŚĞǁĞůůĨŽƌǁŚŝĐŚƚŚŝƐĂƉƉůŝĐĂƚŝŽŶŝƐƐƵďŵŝƚƚĞĚǁŝůůďĞĚĞƐŝŐŶ ĂƚĞĚĂƐϯ^ͲϲϬϮ Ϯ͘ >ŽĐĂƚŝŽŶ^ƵŵŵĂƌLJ ZĞƋƵŝƌĞŵĞŶƚƐŽĨϮϬϮϱ͘ϬϬϱ;ĐͿ;ϮͿ >ŽĐĂƚŝŽŶĂƚ^ƵƌĨĂĐĞϮϰϲϰ&E>͕ϴϯϳ& >͕^ϭϴdϭϮEZϴ ͕hD EϮϳ EŽƌƚŚŝŶŐ͗ϱϵϵϯϵϱϬ͘ϱϱ ĂƐƚŝŶŐ͗ϰϳϲϰϮϮ͘Ϯϰ Z< ůĞǀĂƚŝŽŶϯϵ͘ϱ͛D^> WĂĚ ůĞǀĂƚŝŽŶϮϳ͘ϳ͛D^> dŽƉŽĨWƌŽĚƵĐƚŝǀĞ,ŽƌŝnjŽŶ;,ĞĞůͿϭϳϲϮ&^>͕ϮϭϵϮ& >͕^ϳdϭϮEZϴ ͕hD EϮϳ EŽƌƚŚŝŶŐ͗ϱϵϵϴϭϴϬ͘ϵϵ ĂƐƚŝŶŐ͗ϰϳϱϬϲϱ͘ϴϮ DĞĂƐƵƌĞĚĞƉƚŚ͕Z<͗ϳϮϬϱ͚D dƌƵĞsĞƌƚŝĐĂůĞƉƚŚ͕Z<͗ϱϮϬϯ͚ds dƌƵĞsĞƌƚŝĐĂůĞƉƚŚ͕^^͗ϱϭϯϲ͚dsƐƐ dŽƚĂůĞƉƚŚ;dŽĞͿϮϱϵϲ&^>͕ϭϮϭϬ&t>͕^ϯϲdϭϯEZϳ ͕hD EϮϳ EŽƌƚŚŝŶŐ͗ϰϳϮϭϰϬ͘Ϯϱ ĂƐƚŝŶŐ͗ϲϬϬϵϱϴϰ͘Ϭϯ DĞĂƐƵƌĞĚĞƉƚŚ͕Z<͗ϭϴϵϴϱ͚D dƌƵĞsĞƌƚŝĐĂůĞƉƚŚ͕Z<͗ϱϮϬϱ͚ds dƌƵĞsĞƌƚŝĐĂůĞƉƚŚ͕^^͗ϱϭϯϴ͚dsƐƐ WĂĚ>ĂLJŽƵƚ ϯ^ͲϲϬϮK'ϭϬͲϰϬϭW ϭͬϭϰͬϮϬϮϱ ϯ^ͲϲϬϮK'ϭϬͲϰϬϭWϯͮϭϮ tĞůůWůĂƚ ϯ^ͲϲϬϮK'ϭϬͲϰϬϭWϰͮϭϮ ϯ^ͲϲϬϮK'ϭϬͲϰϬϭW ϭͬϭϰͬϮϬϮϱ ϯ͘ WƌŽƉŽƐĞĚƌŝůůŝŶŐWƌŽŐƌĂŵ ZĞƋƵŝƌĞŵĞŶƚƐŽĨϮϬϮϱ͘ϬϬϱ;ĐͿ;ϭϯͿ ϭ͘ 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ŚĂŶŐĞƵƉƉĞƌϳͲϱͬϴΗƐŽůŝĚďŽĚLJƌĂŵƐƚŽϮͲϳͬϴ͟džϱ͟sZ͛Ɛ͘dĞ ƐƚKW ƚŽϮϱϬͬϯ͕ϱϬϬƉƐŝ͘;ϮϰͲϰϴŚƌ͘ ƌĞŐƵůĂƚŽƌLJŶŽƚŝĐĞͿ͘ ϭϰ͘ WŝĐŬƵƉĂŶĚZ/,ǁŝƚŚϲͲϭͬϮ͟ĚƌŝůůŝŶŐĂƐƐĞŵďůLJ͘>ŽŐƚŽƉŽĨĐĞŵĞŶƚǁŝƚŚƐŽŶŝĐƚŽŽůŝŶƌĞĐŽƌĚĞĚŵŽĚĞ͘ ϭϱ͘ ŚĂƌƚĐĂƐŝŶŐƉƌĞƐƐƵƌĞƚĞƐƚƚŽϯ͕ϱϬϬƉƐŝĨŽƌϯϬŵŝŶƵƚĞƐŝĨŶŽƚƚĞƐƚĞĚŽŶƉůƵŐďƵŵƉ͘ ϭϲ͘ ƌŝůůŽƵƚƐŚŽĞƚƌĂĐŬĂŶĚϮϬĨĞĞƚŽĨŶĞǁĨŽƌŵĂƚŝŽŶ͘WĞƌĨŽƌŵ&/d͘DŝŶŝŵƵŵĂĐĐĞƉƚĂďůĞůĞĂŬͲŽĨĨĨŽƌĚƌŝůůŝŶŐ ĂŚĞĂĚŝƐϭϭƉƉŐ Dt͘ ϭϳ͘ ƌŝůůϲͲϭͬϮΗŚŽƌŝnjŽŶƚĂůŚŽůĞƚŽƐĞĐƚŝŽŶd;>tWƌŽŐƌĂŵ͗'ZͬZ ^ͬĞŶͬEĞƵͬ^ŽŶŝĐͿ͘ ϭϴ͘ ŝƌĐƵůĂƚĞƚŚĞŚŽůĞĐůĞĂŶĂŶĚWKK,͘ ϭϵ͘ ZƵŶϰͲϭͬϮ͟ůŝŶĞƌƚŽdĂŶĚƐĞƚůŝŶĞƌŚĂŶŐĞƌ ϮϬ͘ ^ĞƚƉĂĐŬĞƌ͘ŚĂƌƚĐĂƐŝŶŐƉƌĞƐƐƵƌĞƚĞƐƚϯ͕ϱϬϬƉƐŝ͘WKK,>W͘ Ϯϭ͘ ZƵŶϰͲϭͬϮ͟ƵƉƉĞƌĐŽŵƉůĞƚŝŽŶǁŝƚŚŐůĂƐƐƉůƵŐ͕ƉƌŽĚƵĐƚŝŽŶƉĂĐŬ Ğƌ͕ĐŚĞŵŝĐĂůŝŶũĞĐƚŝŽŶŵĂŶĚƌĞůǁŝƚŚĐĂƉ ƐƚƌŝŶŐ͕ĚŽǁŶŚŽůĞŐĂƵŐĞ͕ĂŶĚŐĂƐůŝĨƚŵĂŶĚƌĞůƐ͘^ƉĂĐĞŽƵƚĂŶĚůĂŶĚƚƵďŝŶŐŚĂŶŐĞƌǁŝƚŚƉƌĞͲŝŶƐƚĂůůĞĚĂŶĚ ƉƌĞͲƚĞƐƚĞĚWs͘ ϮϮ͘ WƌĞƐƐƵƌĞƚĞƐƚŚĂŶŐĞƌƐĞĂůƐƚŽϯ͕ϴϱϬƉƐŝ͘ Ϯϯ͘ WƌĞƐƐƵƌĞƚĞƐƚĂŐĂŝŶƐƚƚŚĞŐůĂƐƐƉůƵŐƚŽƐĞƚƉƌŽĚƵĐƚŝŽŶƉĂĐŬĞƌ͕ƚĞƐƚƚƵďŝŶŐƚŽϯ͕ϴϱϬƉƐŝ͕ĐŚĂƌƚƚĞƐƚ͘ Ϯϰ͘ ůĞĞĚƚƵďŝŶŐƉƌĞƐƐƵƌĞƚŽϮϮϬϬƉƐŝĂŶĚƚĞƐƚ/ƚŽϯ͕ϴϱϬƉƐŝ͕ĐŚĂƌƚƚĞƐƚ͘ Ϯϱ͘ /ŶƐƚĂůů,WͲWsĂŶĚƚĞƐƚƚŽϮϱϬϬƉƐŝ͘ ϯ^ͲϲϬϮK'ϭϬͲϰϬϭW ϭͬϭϰͬϮϬϮϱ ϯ^ͲϲϬϮK'ϭϬͲϰϬϭWϱͮϭϮ Ϯϲ͘ EŝƉƉůĞĚŽǁŶKW͘ Ϯϳ͘ /ŶƐƚĂůůƚƵďŝŶŐŚĞĂĚĂĚĂƉƚĞƌĂƐƐĞŵďůLJ͘EͬhƚƌĞĞĂŶĚƚĞƐƚƚŽϱϬϬϬƉƐŝͬϭϬŵŝŶƵƚĞƐ͘ Ϯϴ͘ &ƌĞĞnjĞƉƌŽƚĞĐƚĚŽǁŶƚƵďŝŶŐĂŶĚĂŶŶƵůƵƐ͘ Ϯϵ͘ ^ĞĐƵƌĞǁĞůů͘ZŝŐĚŽǁŶĂŶĚŵŽǀĞŽƵƚ͘ ϰ͘ KWĂŶĚŝǀĞƌƚĞƌ/ŶĨŽƌŵĂƚŝŽŶ ZĞƋƵŝƌĞŵĞŶƚƐŽĨϮϬϮϱ͘ϬϬϱ;ĐͿ;ϯΘϳͿ WůĞĂƐĞƌĞĨĞƌĞŶĐĞKWĂŶĚĚŝǀĞƌƚĞƌƐĐŚĞŵĂƚŝĐƐŽŶĨŝůĞĨŽƌŽLJŽŶϮϱ ŽLJŽŶϮϱǁŝůůƵƐĞĂKW ƐƚĂĐŬĞƋƵŝƉƉĞĚǁŝƚŚĂŶĂŶŶƵůĂƌƉƌĞǀĞŶƚĞƌ͕ĨŝdžĞĚ͕ϳͲϱͬϴΗƐŽůŝĚďŽĚLJƌĂŵƐ͕ ďůŝŶĚͬƐŚĞĂƌƌĂŵƐĂŶĚǀĂƌŝĂďůĞďŽƌĞƌĂŵƐǁŚŝůĞĚƌŝůůŝŶŐĂŶĚƌƵŶŶŝŶŐĐĂƐŝŶŐŝŶƚŚĞŝŶƚĞƌŵĞĚŝĂƚĞƐĞĐƚŝŽŶŽĨ ϯ^ͲϲϬϮ͘ ϯ^ͲϲϬϮŚĂƐĂD^WŽĨϭϴϮϭƉƐŝŝŶƚŚĞŝŶƚĞƌŵĞĚŝĂƚĞŚŽůĞƐĞĐƚŝŽŶƵƐŝŶŐƚŚĞŵĞƚŚŽĚŽůŽŐLJƉƌĞƐĞŶƚĞĚŝŶ ƐĞĐƚŝŽŶϱD^WĐĂůĐƵůĂƚŝŽŶƐ͘tŝƚŚĂD^WůĞƐƐƚŚĂŶϯϬϬϬƉƐŝŽŶ ŽĐŽWŚŝůůŝƉƐĐůĂƐƐŝĨŝĞƐƚŚĞŽƉĞƌĂƚŝŽŶĂƐĂ ůĂƐƐϮ͘ WĞƌϮϬϮϱ͘Ϭϯϱ͘Ğ͘ϭ͗͘ &ŽƌĂŶŽƉĞƌĂƚŝŽŶǁŝƚŚĂŵĂdžŝŵƵŵƉŽƚĞŶƚŝĂůƐƵƌĨĂĐĞƉƌĞƐƐƵƌĞŽĨϯ͕ϬϬϬƉƐŝŽƌůĞƐƐ͕KW ŵƵƐƚŚĂǀĞĂƚůĞĂƐƚ ƚŚƌĞĞƉƌĞǀĞŶƚĞƌƐ͕ŝŶĐůƵĚŝŶŐ͗ ŝ͘ KŶĞĞƋƵŝƉƉĞĚǁŝƚŚƉŝƉĞƌĂŵƐƚŚĂƚĨŝƚƚŚĞƐŝnjĞŽĨĚƌŝůůƉŝƉĞ͕ƚƵ ďŝŶŐŽƌĐĂƐŝŶŐďĞŐŝŶƵƐĞĚ͕ĞdžĐĞƉƚƚŚĂƚƉŝƉĞƌĂŵƐ ŶĞĞĚŶŽƚďĞƐŝnjĞĚƚŽďŽƚƚŽŵͲŚŽůĞĂƐƐĞŵďůŝĞƐĂŶĚĚƌŝůůĐŽůůĂƌƐ͘ ŝŝ͘ KŶĞǁŝƚŚďůŝŶĚƌĂŵƐ ŝŝŝ͘ KŶĞĂŶŶƵůĂƌƚLJƉĞ /ŶƚĞƌŵĞĚŝĂƚĞƌŝůůŝŶŐͬĂƐŝŶŐ x ŶŶƵůĂƌWƌĞǀĞŶƚĞƌ;ŝŝŝͿ x ϳͲϱͬϴΗ&ŝdžĞĚZĂŵƐ x ůŝŶĚͬ^ŚĞĂƌZĂŵƐ;ŝŝͿ x sZ͛Ɛ;ŝͿ WƌŽĚƵĐƚŝŽŶ͗ x ŶŶƵůĂƌWƌĞǀĞŶƚĞƌ;ŝŝŝͿ x sZ͛Ɛ;ŝͿ x ůŝŶĚͬ^ŚĞĂƌZĂŵƐ;ŝŝͿ x sZ͛Ɛ;ŝͿ ϯ^ͲϲϬϮK'ϭϬͲϰϬϭW ϭͬϭϰͬϮϬϮϱ ϯ^ͲϲϬϮK'ϭϬͲϰϬϭWϲͮϭϮ /ƚŝƐƌĞƋƵĞƐƚĞĚƚŚĂƚĂǀĂƌŝĂŶĐĞŽĨƚŚĞĚŝǀĞƌƚĞƌƌĞƋƵŝƌĞŵĞŶƚƵŶĚĞƌϮϬϮϱ͘Ϭϯϱ;ŚͿ;ϮͿŝƐŐƌĂŶƚĞĚ͘ƚϯ^͕ ƚŚĞƌĞŚĂƐŶŽƚďĞĞŶƐŝŐŶŝĨŝĐĂŶƚŝŶĚŝĐĂƚŝŽŶŽĨƐŚĂůůŽǁŐĂƐŽƌŐĂƐŚLJĚƌĂƚĞƐƚŚƌŽƵŐŚƚŚĞƐƵƌĨĂĐĞŚŽůĞŝŶƚĞƌǀĂů͘ dŚĞƌĞĂƌĞϳƉƌĞǀŝŽƵƐůLJĚƌŝůůĞĚǁĞůůƐ;ϯ^Ͳϭϰ͕ϯ^ͲϲϬϲ͕ϯ^ͲϲϭϬ͕ϯ^Ͳϲϭϭ͕ϯ^ͲϲϭϮ͕ϯ^Ͳϲϭϳ͕ϯ^ͲϲϮϰͿǁŝƚŚŝŶϱϬϬ͛ŽĨ ƚŚĞƉƌŽƉŽƐĞĚϯ^ͲϲϬϮƐƵƌĨĂĐĞƐŚŽĞůŽĐĂƚŝŽŶ͘EŽŶĞŽĨƚŚĞƐĞǁĞůůƐĞŶĐŽƵŶƚĞƌĞĚĂŶLJƐŝŐŶŝĨŝĐĂŶƚŝŶĚŝĐĂƚŝŽŶŽĨ ƐŚĂůůŽǁŐĂƐŽƌŐĂƐŚLJĚƌĂƚĞƐ͘ ϱ͘ D^WĂůĐƵůĂƚŝŽŶƐ ZĞƋƵŝƌĞŵĞŶƚƐŽĨϮϬϮϱ͘ϬϬϱ;ĐͿ;ϰͿ ;ͿŵĂdžŝŵƵŵĚŽǁŶŚŽůĞƉƌĞƐƐƵƌĞĂŶĚŵĂdžŝŵƵŵƉŽƚĞŶƚŝĂůƐƵƌĨĂĐĞƉƌĞƐƐƵƌĞ͖ DĂdžŝŵƵŵWŽƚĞŶƚŝĂů^ƵƌĨĂĐĞWƌĞƐƐƵƌĞ;DW^WͿŝƐĚĞƚĞƌŵŝŶĞĚĂƐƚŚĞůĞƐƐĞƌŽĨ͗ DĞƚŚŽĚϭ͗ƐƵƌĨĂĐĞƉƌĞƐƐƵƌĞĂƚďƌĞĂŬĚŽǁŶŽĨƚŚĞĨŽƌŵĂƚŝŽŶĐĂƐŝŶŐƐĞĂƚǁŝƚŚĂŐĂƐŐƌĂĚŝĞŶƚƚŽƚŚĞƐƵƌĨĂĐĞ DĞƚŚŽĚϮ͗ĨŽƌŵĂƚŝŽŶƉŽƌĞƉƌĞƐƐƵƌĞĂƚƚŚĞŶĞdžƚĐĂƐŝŶŐƉŽŝŶƚůĞƐƐĂŐĂƐŐƌĂĚŝĞŶƚƚŽƚŚĞƐƵƌĨĂĐĞ DĞƚŚŽĚϭDĞƚŚŽĚϮ ܯܲܵܲ ൌ ሾሺܨܩൈ ͲǤͲͷʹሻ െ ܩܽݏܩݎܽ݀݅݁݊ݐሿ ൈ ܸܶܦ ܯܲܵܲ ൌ ܨܲܲ െ ሺܩܽݏܩݎܽ݀݅݁݊ݐሻ ൈ ܸܶܦ tŚĞƌĞ͗ &'ʹ&ƌĂĐƚƵƌĞŐƌĂĚŝĞŶƚĂƚƚŚĞĐĂƐŝŶŐƐĞĂƚŝŶůďͬŐĂů Ϭ͘ϬϱϮʹŽŶǀĞƌƐŝŽŶĨƌŽŵůďͬŐĂůƚŽƉƐŝͬĨƚ 'ĂƐ'ƌĂĚŝĞŶƚʹϬ͘ϭƉƐŝͬĨƚ dsʹdƌƵĞsĞƌƚŝĐĂůĞƉƚŚŽĨĐĂƐŝŶŐƐĞĂƚŝŶĨƚZ< tŚĞƌĞ͗ &WWʹ&ŽƌŵĂƚŝŽŶWŽƌĞWƌĞƐƐƵƌĞĂƚƚŚĞŶĞdžƚĐĂƐŝŶŐƉŽŝŶƚ 'ĂƐ'ƌĂĚŝĞŶƚʹϬ͘ϭƉƐŝͬĨƚ dŚĞĨŽůůŽǁŝŶŐƉƌĞƐĞŶƚƐĚĂƚĂƵƐĞĚĨŽƌĐĂůĐƵůĂƚŝŽŶŽĨDĂdžŝŵƵŵWŽƚĞŶƚŝĂů^ƵƌĨĂĐĞWƌĞƐƐƵƌĞ;DW^WͿǁŚŝůĞ ĚƌŝůůŝŶŐ͗ ^ĞĐƚŝŽŶ,ŽůĞ^ŝnjĞ WƌĞǀŝŽƵƐ^'^ĞĐƚŝŽŶdDW^W ƉƐŝ DW^WDW^W ^ŝnjĞDds&' ƉƉŐ WŽƌĞWƌĞƐƐƵƌĞ ƉƉŐͮƉƐŝDdsWŽƌĞWƌĞƐƐƵƌĞ ƉƉŐͮƉƐŝ DĞƚŚŽĚϭ ƉƐŝ DĞƚŚŽĚϮ ƉƐŝ ^hZ&ϭϯͲϭͬϮΗ ϮϬΗ ϭϮϬ ϭϮϬ ϵ ϴ͘ϯ ϱϮ Ϯϴϱϳ Ϯϰϴϴ ϵ ϭ͕ϭϲϰ ϰϰϰϰϵϭϱ /EdϭϵͲϳͬϴΗ ϭϬͲϯͬϰΗ Ϯϴϱϳ Ϯϰϴϴ ϭϲ ϵ ϭ͕ϭϲϰ ϳϮϬϱ ϱϮϬϯ ϵ Ϯ͕ϰϯϱ ϭ͕ϴϮϭϭ͕ϴϮϭϭ͕ϵϭϱ WZKϲͲϭͬϮΗ ϳͲϱͬϴΗ ϳϮϬϱ ϱϮϬϯ ϭϮ͘ϱ ϵ Ϯ͕ϰϯϱ ϭϴϵϴϱ ϱϮϬϱ ϵ Ϯ͕ϰϯϲ ϭ͕ϵϭϲ Ϯ͕ϴϲϮϭ͕ϵϭϲ ΎDĂdžŝŵƵŵƉŽƚĞŶƚŝĂůƉŽƌĞƉƌĞƐƐƵƌĞŝŶƚŚĞ^ƵƐŝƚŶĂ^ĂŶĚŝĨƉƌĞƐĞŶƚ ;ͿĚĂƚĂŽŶƉŽƚĞŶƚŝĂůŐĂƐnjŽŶĞƐ͖ dŚĞƉůĂŶŶĞĚǁĞůůďŽƌĞŝƐĞdžƉĞĐƚĞĚƚŽĞŶƚĞƌƚŚĞŐĂƐĐĂƉĂŶĚƚŚĞĂƌĞĂŝƐĞdžƉĞĐƚĞĚƚŽďĞŶŽƌŵĂůůLJƉƌĞƐƐƵƌĞĚ ;ϴ͘ϲͲϵ͘ϬƉƉŐͿ͘ ;ͿĚĂƚĂĐŽŶĐĞƌŶŝŶŐƉŽƚĞŶƚŝĂůĐĂƵƐĞƐŽĨŚŽůĞƉƌŽďůĞŵƐƐƵĐŚĂƐĂďŶŽƌŵĂůůLJŐĞŽͲƉƌĞƐƐƵƌĞĚƐƚƌĂƚĂ͕ůŽƐƚ ĐŝƌĐƵůĂƚŝŽŶnjŽŶĞƐ͕ĂŶĚnjŽŶĞƐƚŚĂƚŚĂǀĞĂƉƌŽƉĞŶƐŝƚLJĨŽƌĚŝĨĨĞƌĞŶƚŝĂůƐƚŝĐŬŝŶŐ͖ WůĞĂƐĞƐĞĞƌŝůůŝŶŐ,ĂnjĂƌĚƐ^ƵŵŵĂƌLJ Recommend granting variance. -A.Dewhurst 27JAN25 ϯ^ͲϲϬϮK'ϭϬͲϰϬϭW ϭͬϭϰͬϮϬϮϱ ϯ^ͲϲϬϮK'ϭϬͲϰϬϭWϳͮϭϮ ϲ͘ WƌŽĐĞĚƵƌĞĨŽƌŽŶĚƵĐƚŝŶŐ&ŽƌŵĂƚŝŽŶ/ŶƚĞŐƌŝƚLJdĞƐƚƐ ZĞƋƵŝƌĞŵĞŶƚƐŽĨϮϬϮϱ͘ϬϬϱ;ĐͿ;ϱͿ ƌŝůůŽƵƚĐĂƐŝŶŐƐŚŽĞĂŶĚƉĞƌĨŽƌŵ>KdƚĞƐƚŽƌ&/dŝŶĂĐĐŽƌĚĂŶĐĞ ǁŝƚŚƚŚĞ>Kdͬ&/dƉƌŽĐĞĚƵƌĞƚŚĂƚ ŽŶŽĐŽWŚŝůůŝƉƐůĂƐŬĂŚĂƐŽŶĨŝůĞǁŝƚŚƚŚĞŽŵŵŝƐƐŝŽŶ͘ ϳ͘ ĂƐŝŶŐĂŶĚĞŵĞŶƚŝŶŐWƌŽŐƌĂŵ ZĞƋƵŝƌĞŵĞŶƚƐŽĨϮϬϮϱ͘ϬϬϱ;ĐͿ;ϲͿ ĂƐŝŶŐĂŶĚĞŵĞŶƚŝŶŐWƌŽŐƌĂŵ K ;ŝŶͿ ,ŽůĞ^ŝnjĞ ;ŝŶͿ tĞŝŐŚƚ ;ůďͬĨƚͿ'ƌĂĚĞŽŶŶ͘ĞŵĞŶƚWƌŽŐƌĂŵ ϮϬ ϰϮ ϵϰ ,ϰϬ tĞůĚĞĚ ĞŵĞŶƚĞĚƚŽƐƵƌĨĂĐĞǁŝƚŚ ϭϬLJĚƐƐůƵƌƌLJ ϭϬͲϯͬϰΗ ϭϯͲϭͬϮΗ ϰϱ͘ϱη >ϴϬ ,ϱϲϯ ĞŵĞŶƚƚŽ^ƵƌĨĂĐĞ ϳͲϱͬϴΗ ϵͲϳͬϴΗ Ϯϵ͘ϳη ϯϯ͘ϳη >ϴϬ WϭϭϬ^,ϱϲϯϮϱϬ͛dsŽƌϱϬϬ͛D͕ǁŚŝĐŚĞǀĞƌŝƐŐƌĞĂƚĞƌ͕ĂďŽǀĞ ŚŝŐŚĞƐƚƐŝŐŶŝĨŝĐĂŶƚŚLJĚƌŽĐĂƌďŽŶďĞĂƌŝŶŐnjŽŶĞ ϰͲϭͬϮΗ ϲͲϭͬϮΗ ϭϮ͘ϲη WϭϭϬͲ^ ,ϱϲϯ hŶĐĞŵĞŶƚĞĚ>ŝŶĞƌǁŝƚŚĨƌĂĐƐůĞĞǀĞƐĂŶĚƐǁĞůůƉĂĐŬĞƌƐ ϭϬͲϯͬϰΗ^ƵƌĨĂĐĞĂƐŝŶŐƌƵŶƚŽϮϴϱϳΖDͬϮϰϴϴΖdsĞŵĞŶƚWůĂŶ͗ ĞŵĞŶƚĨƌŽŵϮϴϱϳ͛DƚŽϮϯϱϳ͛;ϱϬϬ͛ŽĨƚĂŝůͿǁŝƚŚĞĞƉZ d нĚĚƐΛϭϱ͘ϴƉƉŐ͕ĂŶĚĨƌŽŵϮϯϱϳΖƚŽ ƐƵƌĨĂĐĞǁŝƚŚϭϭ͘ϬƉƉŐĞĞƉZ d 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,LJĚƌŽŐĞŶ^ƵůĨŝĚĞŐĂƐ>Žǁ ,Ϯ^ĚƌŝůůƐ͕ĚĞƚĞĐƚŝŽŶƐLJƐƚĞŵƐ͕ĂůĂƌŵƐ͕ƐƚĂŶĚĂƌĚǁĞůůĐŽŶƚƌŽůƉƌĂĐƚŝĐĞƐ͕ŵƵĚƐĐĂǀĞŶŐĞƌƐ dŽďĞƉŽƐƚĞĚŝŶZŝŐ&ůŽŽƌŽŐŚŽƵƐĞWƌŝŽƌƚŽ^ƉƵĚ ϯ^ͲϲϬϮK'ϭϬͲϰϬϭW ϭͬϭϰͬϮϬϮϱ ϯ^ͲϲϬϮK'ϭϬͲϰϬϭWϭϭͮϭϮ tĞůůWƌŽdžŝŵŝƚLJZŝƐŬƐ͗ ϯ^ǁŝůůďĞĂŵƵůƚŝͲǁĞůůƉĂĚ͘ŝƌĞĐƚŝŽŶĂůĚƌŝůůŝŶŐͬĐŽůůŝƐŝŽŶĂ ǀŽŝĚĂŶĐĞŝŶĨŽƌŵĂƚŝŽŶĂƐƌĞƋƵŝƌĞĚďLJK'ϮϬ Ϯϱ͘ϬϱϬ;ďͿŝƐƉƌŽǀŝĚĞĚŝŶƚŚĞĨŽůůŽǁŝŶŐĂƚƚĂĐŚŵĞŶƚƐ͘ ƌŝůůŝŶŐƌĞĂZŝƐŬƐ͗ x ZĞƐĞƌǀŽŝƌWƌĞƐƐƵƌĞ͗ hŶůŝŬĞůLJƚŽĞŶĐŽƵŶƚĞƌĂŶLJĂďŶŽƌŵĂůƉƌĞƐƐƵƌĞŚŽǁĞǀĞƌ͕ƚŚĞƌŝŐǁŝůůďĞƉƌĞƉĂƌĞĚƚŽǁĞŝŐŚƚƵƉŝĨ ƌĞƋƵŝƌĞĚ͘ tĞĂŬƐĂŶĚƐƚƌŝŶŐĞƌƐĐŽƵůĚďĞƉƌĞƐĞŶƚŝŶƚŚĞŽǀĞƌďƵƌĚĞŶ͘>DŵĂƚĞƌŝĂůǁŝůůďĞĂǀĂŝůĂďůĞƚŽƐĞĂůŝŶ ůŽƐƐĞƐŝŶƚŚĞŝŶƚĞƌŵĞĚŝĂƚĞƐĞĐƚŝŽŶ͘ x >ŽƐƚŝƌĐƵůĂƚŝŽŶ͗ ^ƚĂŶĚĂƌĚ>DŵĂƚĞƌŝĂůĂŶĚǁĞůůďŽƌĞƐƚƌĞŶŐƚŚĞŶŝŶŐƉŝůůƐĂƌĞĞdžƉĞĐƚĞĚƚŽďĞĞĨĨĞĐƚŝǀĞŝŶĚĞĂůŝŶŐ ǁŝƚŚůŽƐƚĐŝƌĐƵůĂƚŝŽŶŝĨŶĞĞĚĞĚ͘ x ^ǁĂďďĞĚ<ŝĐŬƐ 'ŽŽĚĚƌŝůůŝŶŐƉƌĂĐƚŝĐĞƐǁŝůůďĞƐƚƌĞƐƐĞĚƚŽŵŝŶŝŵŝnjĞƚŚĞƉŽƚĞŶƚŝĂůŽĨƚĂŬŝŶŐƐǁĂďďĞĚŬŝĐŬƐ͘ ϯ^ͲϲϬϮK'ϭϬͲϰϬϭW ϭͬϭϰͬϮϬϮϱ ϯ^ͲϲϬϮK'ϭϬͲϰϬϭWϭϮͮϭϮ ϭϱ͘ WƌŽƉŽƐĞĚŽŵƉůĞƚŝŽŶ^ĐŚĞŵĂƚŝĐ 40 300 300 500 500 750 750 1000 1000 1250 1250 1500 1500 2000 2000 3000 3000 5000 5000 7000 7000 10000 10000 15000 15000 20000 3S-602 wp06.1 Plan Summary 3S-602 wp06.1 3S-705 (I12) wp09 3S-734 (P04) wp03 3S-714 wp08 3S-723 wp04 3S-07 3S-14 3S-03 3S-701A 3S-701 3S-718 3S-739 (I11) wp03 3S-613 3S-606 3S-611 3S-611PB1 3S-704 3S-730 (P10) wp04 3S-703 (P12) wp04 3S-612 3S-610 3S-16 3S-08 3S-08B 3S-08A 3S-08CL1 3S-08CL1PB1 3S-09 3S-10 3S-732 (I10) wp04 3S-06A 3S-06 3S-15 3S-08C 3T-605PH wp03 0 4 Dogleg Severity0 3000 6000 9000 12000 15000 18000 Measured Depth 10-3/4" Surface Casing 7-5/8" Intermediate Casing 4-1/2" Production Casing 50 50 100 100 0 90 180 270 30 210 60 240 120 300 150 330 Travelling Cylinder Azimuth (TFO+AZI) [°] vs Travelling Cylinder Separation [100 usft/in] 3S-705 (I12) wp09 3S-07 3S-14 3S-03 3S-701A 3S-701 3S-606 3S-704 3S-730 (P10) wp04 3S-703 (P12) wp04 3S-09 3S-10 3S-732 (I10) wp04 3S-06A 3S-06 0 4500 True Vertical Depth0 3000 6000 9000 12000 15000 18000 21000 Vertical Section at 344.50° 10-3/4" Surface Casing 7-5/8" Intermediate Casing 4-1/2" Production Casing 0 28 55 Centre to Centre Separation0 2750 5500 8250 11000 13750 16500 19250 Measured Depth Equivalent Magnetic Distance DDI 6.924 SURVEY PROGRAM Date: 2024-11-18T00:00:00 Validated: Yes Version: Depth From Depth To Survey/Plan Tool 39.50 1300.00 3S-602 wp06.1 (3S-602)r.5 SDI_URSA1 1300.00 2857.61 3S-602 wp06.1 (3S-602) MWD+IFR2+SAG+MS 2857.61 7205.45 3S-602 wp06.1 (3S-602)MWD+IFR2+SAG+MS 7205.45 18985.00 3S-602 wp06.1 (3S-602)MWD+IFR2+SAG+MS Surface Location North / 5993593.54 East / 1616454.32 Ground / 27.70 CASING DETAILS TVD MD Name 2488.20 2857.61 10-3/4" Surface Casing 5203.20 7205.45 7-5/8" Intermediate Casing 5204.75 18985.00 4-1/2" Production Casing Mag Model & Date:BGGM2024 01-Feb-25 Magnetic North is 13.88° East of True North (Magnetic Declination) Mag Dip & Field Strength:80.61° 57184.07nT SECTION DETAILS Sec MD Inc Azi TVD +N/-S +E/-W Dleg TFace VSect Annotation 1 39.50 0.00 0.00 39.50 107.46 -33.10 0.00 0.00 0.00 2 300.00 0.00 0.00 300.00 107.46 -33.10 0.00 0.00 0.00 Start Build 1.00 3 400.00 1.00 340.00 399.99 108.28 -33.40 1.00 340.00 0.87 Start Build 2.00 4 500.00 3.00 340.00 499.93 111.55 -34.59 2.00 0.00 4.35 Start Build 2.50 5 1557.32 29.43 340.00 1506.20 386.57 -134.69 2.50 0.00 296.11 Start 114.82 hold at 1557.32 MD 6 1672.14 29.43 340.00 1606.20 439.59 -153.99 0.00 0.00 352.36 Start DLS 2.50 TFO -3.32 7 2358.12 46.56 338.65 2144.77 832.88 -303.41 2.50 -3.32 771.28 Start 2644.49 hold at 2358.12 MD 8 5002.61 46.56 338.65 3963.00 2621.39 -1002.42 0.00 0.00 2681.56 Start DLS 2.00 TFO 91.98 9 5342.29 46.71 348.00 4196.50 2857.46 -1073.10 2.00 91.98 2927.92 Start DLS 3.50 TFO 168.98 10 5447.31 43.11 349.03 4270.87 2930.09 -1087.88 3.50 168.98 3001.87 Start 547.68 hold at 5447.31 MD 11 5994.98 43.11 349.03 4670.72 3297.51 -1159.12 0.00 0.00 3374.96 Start DLS 3.75 TFO -5.73 12 6808.24 73.50 346.00 5093.10 3964.42 -1309.91 3.75 -5.73 4057.91 Start 100.00 hold at 6808.24 MD 13 6908.24 73.50 346.00 5121.50 4057.46 -1333.10 0.00 0.00 4153.76 Start 200.00 hold at 6908.24 MD 14 7108.24 73.50 346.00 5178.30 4243.52 -1379.49 0.00 0.00 4345.46 Start DLS 3.75 TFO -24.50 15 7327.38 81.00 342.56 5226.64 4449.06 -1437.45 3.75 -24.50 4559.01 Start 13.75 hold at 7327.38 MD 16 7341.13 81.00 342.56 5228.79 4462.02 -1441.51 0.00 0.00 4572.58 Start DLS 3.75 TFO 31.37 17 7465.76 85.00 345.00 5243.98 4580.77 -1476.05 3.75 31.37 4696.24 Start 150.00 hold at 7465.76 MD 18 7615.76 85.00 345.00 5257.05 4725.10 -1514.72 0.00 0.00 4845.66 Start 20.00 hold at 7615.76 MD 19 7635.76 85.00 345.00 5258.79 4744.35 -1519.88 0.00 0.00 4865.59 Start DLS 1.00 TFO 3.64 20 8227.33 90.90 345.37 5279.93 5315.64 -1670.95 1.00 3.64 5456.47 Start 3826.42 hold at 8227.33 MD 21 12053.75 90.90 345.37 5219.57 9017.62 -2636.99 0.00 0.00 9281.97 Start DLS 1.00 TFO 20.98 22 12074.76 91.10 345.45 5219.20 9037.95 -2642.28 1.00 20.98 9302.97 Start DLS 1.00 TFO 12.68 23 12124.09 91.58 345.56 5218.05 9085.69 -2654.62 1.00 12.68 9352.28 Start 1070.38 hold at 12124.09 MD 24 13194.46 91.58 345.56 5188.51 10121.85 -2921.47 0.00 0.00 10422.06 Start DLS 1.00 TFO 179.83 25 13252.59 91.00 345.56 5187.20 10178.12 -2935.96 1.00 179.83 10480.16 Start DLS 1.00 TFO 179.96 26 13338.95 90.14 345.56 5186.34 10261.75 -2957.49 1.00 179.96 10566.51 Start 2998.74 hold at 13338.95 MD 27 16337.69 90.14 345.56 5179.22 13165.76 -3705.24 0.00 0.00 13564.72 Start DLS 1.00 TFO -179.75 28 16351.32 90.00 345.56 5179.20 13178.96 -3708.64 1.00 -179.75 13578.35 Start DLS 1.00 TFO 179.69 29 16514.03 88.37 345.57 5181.51 13336.51 -3749.20 1.00 179.69 13741.01 Start 1105.20 hold at 16514.03 MD 30 17619.23 88.37 345.57 5212.89 14406.41 -4024.53 0.00 0.00 14845.57 Start DLS 1.00 TFO -1.01 31 17781.96 90.00 345.54 5215.20 14563.97 -4065.11 1.00 -1.01 15008.25 Start DLS 1.00 TFO -5.26 32 17819.46 90.37 345.51 5215.08 14600.28 -4074.49 1.00 -5.26 15045.74 Start 987.88 hold at 17819.46 MD 33 18807.34 90.37 345.51 5208.64 15556.70 -4321.74 0.00 0.00 16033.45 Start DLS 1.00 TFO 5.94 34 18850.22 90.80 345.55 5208.20 15598.22 -4332.45 1.00 5.94 16076.33 Start DLS 1.00 TFO 2.38 35 18970.33 92.00 345.60 5205.27 15714.50 -4362.36 1.00 2.38 16196.37 Start 14.67 hold at 18970.33 MD 36 18985.00 92.00 345.60 5204.75 15728.70 -4366.01 0.00 0.00 16211.03 TD at 18985.00 FORMATION TOP DETAILS TVDPath Formation 1373.20 Top Ugnu C 1642.20 Top Ugnu B 1717.20 Base Permafrost 1756.20 Top Ugnu A 2025.20 Top West Sak 2438.20 Base West Sak 2613.20 C-80 3429.20 C-50 3905.20 C-35 4109.20 Top Coyote (Top Nanushuk), K3 4645.20 Base Coyote (Base Nanushuk) 5198.20 Top Torok Oil Pool (Top Moraine) Plan: 27.7+39.5 @ 67.20usft (Doyon 25) Project: Kuparuk River Unit_2 Site: Kuparuk 3S Pad Well: 3S-602 Wellbore: 3S-602 Design: 3S-602 wp06.1 0 6000 12000 18000 South(-)/North(+) (3000 usft/in)-12000 -6000 0 6000 12000 West(-)/East(+) (3000 usft/in) 3S-602 [Northland] T3 081224 3S-602 [Northland] T5 081224 3S-602 [Northland] T6 081224 3S-602 [Northland] T4 081224 3S-602 TD 1320 ft 3S-602 T1 1320 ft 3S-602 [Northland] T2 081224 3S-602 [Northland] T1 032123 3S -7 05 (I 1 2) w p 09 3 S -7 3 4 (P 0 4 ) w p 0 3 3 S-7 14 wp08 3 S -723 wp0 4 3 S- 0 7 3 S -1 4 3 S- 0 3 3 S -7 0 1 A 3 S -7 0 1 3 S -718 3S-739 (I11 ) w p03 3 S -6 1 3 3 S -6 0 6 3 S -6 11 3S-611PB13 S -7 04 3S -730 (P 1 0) w p0 4 3S -7 03 (P12 ) wp 0 4 3 S -6 1 2 3 S -6 1 0 3 S - 1 6 3S-083S-08B3S-08A3S-08CL13S-08CL1PB13 S -0 9 3S- 10 3S-732 (I10) w p04 3S-06A 3S-0 6 3 S -153 S- 0 8 C3 T -6 0 2 w p 0 5 v 5 3T-605PH wp03 3 T -6 0 5 (S T ) w p 0 9 3 T -6 0 6 w p 0 8 3 T -6 0 4 w p 0 5 v 5 3 T -6 0 1 w p 0 5 v 5 10-3/4" Surface Casing 7-5/8" Intermediate Casing 4-1/2" Production Casing 5 0 0100 015002000 2 5 0 0 3 0 0 0 3 5 0 0 4 0 0 04500 5 0 0 0 5 2 0 5 3S-602 wp06.1 Plan View with offset wells Project: Kuparuk River Unit_2 Site: Kuparuk 3S Pad Well: 3S-602 Wellbore: 3S-602 Design: 3S-602 wp06.1 0 6000 12000 18000 South(-)/North(+) (3000 usft/in)-12000 -6000 0 6000 12000 West(-)/East(+) (3000 usft/in) 3S-602 [Northland] T3 081224 3S-602 [Northland] T5 081224 3S-602 [Northland] T6 081224 3S-602 [Northland] T4 081224 3S-602 TD 1320 ft 3S-602 T1 1320 ft 3S-602 [Northland] T2 081224 3S-602 [Northland] T1 032123 10-3/4" Surface Casing 7-5/8" Intermediate Casing 4-1/2" Production Casing 5 0 0100 015002000 2 5 0 0 3 0 0 0 3 5 0 0 4 0 0 04500 5 0 0 0 5 2 0 5 3S-602 wp06.1 Plan View 0 3000 6000True Vertical Depth (1500 usft/in)0 4000 8000 12000 16000 Vertical Section at 344.50° (2000 usft/in) 10-3/4" Surface Casing 7-5/8" Intermediate Casing 4-1/2" Production Casing 1 0 0 0 2 0 0 0 30004000500060007000800090001000011000120001300014000150001600017000180003S-602 wp06.1 Start Build 1.00 Start Build 2.00 Start Build 2.50 Start 114.82 hold at 1557.32 MD Start DLS 2.50 TFO -3.32 Start 2644.49 hold at 2358.12 MD Start DLS 2.00 TFO 91.98 Start DLS 3.50 TFO 168.98 Start 547.68 hold at 5447.31 MD Start DLS 3.75 TFO -5.73 Start 100.00 hold at 6808.24 MD Start 200.00 hold at 6908.24 MD Start DLS 3.75 TFO -24.50 Start 13.75 hold at 7327.38 MD Start DLS 3.75 TFO 31.37 Start 150.00 hold at 7465.76 MD Start 20.00 hold at 7615.76 MD Start DLS 1.00 TFO 3.64 Start 3826.42 hold at 8227.33 MD Start DLS 1.00 TFO 20.98 Start DLS 1.00 TFO 12.68 Start 1070.38 hold at 12124.09 MD Start DLS 1.00 TFO 179.83 Start DLS 1.00 TFO 179.96 Start 2998.74 hold at 13338.95 MD Start DLS 1.00 TFO -179.75 Start DLS 1.00 TFO 179.69 Start 1105.20 hold at 16514.03 MD Start DLS 1.00 TFO -1.01 Start DLS 1.00 TFO -5.26 Start 987.88 hold at 17819.46 MD Start DLS 1.00 TFO 5.94 Start DLS 1.00 TFO 2.38 Start 14.67 hold at 18970.33 MD TD at 18985.00 Section View Project: Kuparuk River Unit_2 Site: Kuparuk 3S Pad Well: 3S-602 Wellbore: 3S-602 Design: 3S-602 wp06.1 ! 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A> A> A @ . -- ( *> .> . 4% +% @ .% 4 ( *> .%B> .%B 4 @ .% 4 ( *> % ( .*> .% ( .* 4$ @ . 9 - (*> .> . 4A @ .? 9 ( *> .?> .? 4% +% @ .2 9 - (*> .2> .2 4% +% @ 8 1 7 1 5 ) - + - , 2$A> C ? 7- +0 ' "2AD /- 2%D ; " 3'' ) + 3'' ) ' ) + !"!#$"% & !" ' () / - +0 > : ' > 1 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 nogreater 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. KRU 3S-602 225-003 KUPARUK RIVER TOROK OIL WELL PERMIT CHECKLIST Company ConocoPhillips Alaska, Inc. Well Name:KUPARUK RIV UNIT 3S-602 Initial Class/Type DEV / PEND GeoArea 890 Unit 11160 On/Off Shore On Program DEVField & Pool Well bore seg Annular DisposalPTD#:2250030 KUPARUK RIVER, TOROK OIL - 490169 NA1Permit fee attached Yes ADL380107, ADL380106, and ADL3938832Lease number appropriate Yes3Unique well name and number Yes KUPARUK RIVER, TOROK OIL - 490169 - governed by 725A4Well located in a defined pool Yes5Well located proper distance from drilling unit boundary NA6Well located proper distance from other wells Yes7Sufficient acreage available in drilling unit Yes8If deviated, is wellbore plat included Yes9Operator only affected party Yes10Operator has appropriate bond in force Yes11Permit can be issued without conservation order Yes12Permit can be issued without administrative approval Yes13Can permit be approved before 15-day wait NA14Well located within area and strata authorized by Injection Order # (put IO# in comments) (For NA15All wells within 1/4 mile area of review identified (For service well only) NA16Pre-produced injector: duration of pre-production less than 3 months (For service well only) NA17Nonconven. gas conforms to AS31.05.030(j.1.A),(j.2.A-D) Yes 80' conductor18Conductor string provided Yes SC set at 2488' MD19Surface casing protects all known USDWs Yes 103% excess20CMT vol adequate to circulate on conductor & surf csg No21CMT vol adequate to tie-in long string to surf csg No22CMT will cover all known productive horizons Yes23Casing designs adequate for C, T, B & permafrost Yes24Adequate tankage or reserve pit NA25If a re-drill, has a 10-403 for abandonment been approved Yes26Adequate wellbore separation proposed Yes Diverter variance granted per 20 AAC 20-035(h)(2)27 If diverter required, does it meet regulations Yes Max reservoir pressure is 2436 psig(9.0 ppg EMW); will drill w/ 9.0-9.5 ppg EMW28Drilling fluid program schematic & equip list adequate Yes29BOPEs, do they meet regulation Yes MPSP is 1915 psig; will test bOPs initially to 5000 psig and subsuquently to 3500 psig30BOPE press rating appropriate; test to (put psig in comments) Yes31Choke manifold complies w/API RP-53 (May 84) Yes32Work will occur without operation shutdown Yes33Is presence of H2S gas probable NA34Mechanical condition of wells within AOR verified (For service well only) No Measures required. 267 units recorded at 3S-615 (2024)35 Permit can be issued w/o hydrogen sulfide measures Yes Reservoir pore pressure anticipated to be 9 ppg EMW. May vary due to offset production and injection.36 Data presented on potential overpressure zones NA37Seismic analysis of shallow gas zones NA38Seabed condition survey (if off-shore) NA39Contact name/phone for weekly progress reports [exploratory only] Appr ADD Date 1/27/2025 Appr VTL Date 2/3/2025 Appr ADD Date 1/27/2025 Administration Engineering Geology Geologic Commissioner:Date:Engineering Commissioner:Date Public Commissioner Date *&:JLC 2/11/2025
