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Alaska Oil and Gas Conservation Commission
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From:Joseph Lastufka
To:Guhl, Meredith D (OGC)
Subject:RE: [EXTERNAL] 223-108 PBU NK-24, 223-110 PBU F-40A, 223-127 PBU L-294
Date:Thursday, December 11, 2025 3:15:53 PM
Meredith,
Thank you for checking, all 3 wells are either planned to be re-permitted or scheduled
further out than the expiration date. Please cancel all 3 wells:
PBU NK-24 (PTD #223-108)
PBU F-40A (PTD #223-110)
PBU L-294 (PTD #223-127)
Please let me know if you need anything else. Thanks!
Thanks,
Joe Lastufka
Sr. Drilling Technologist
Hilcorp North Slope, LLC
Office: (907)777-8400, Cell:(907)227-8496
From: Guhl, Meredith D (OGC) <meredith.guhl@alaska.gov>
Sent: Thursday, December 11, 2025 2:34 PM
To: Joseph Lastufka <joseph.lastufka@hilcorp.com>
Subject: [EXTERNAL] 223-108 PBU NK-24, 223-110 PBU F-40A, 223-127 PBU L-294
Hello Joe,
The following three approved permits are nearing their expiration dates. Does Hilcorp plan to
drill any of these three wells, or should they be marked canceled in the AOGCC database?
1. 223-108 PBU NK-24, expires 2/13/2026
2. 223-110 PBU F-40A, expires 1/3/2026
3. 223-127 PBU L-294, expires 1/2/2026
Thanks,
Meredith
Meredith Guhl (she/her)
Petroleum Geology Assistant
Alaska Oil and Gas Conservation Commission
333 W. 7th Ave, Anchorage, AK 99501
meredith.guhl@alaska.gov
Direct: (907) 793-1235
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 confidential and/or privileged information. The unauthorized review, use or disclosure of such
information may violate state or federal law. If you are an unintended recipient of this e-mail, please delete it, without
first saving or forwarding it, and, so that the AOGCC is aware of the mistake in sending it to you, contact Meredith Guhl
at 907-793-1235 or meredith.guhl@alaska.gov.
The information contained in this email message is confidential and may be legally privileged and is intended only for the use of the
individual or entity named above. If you are not an intended recipient or if you have received this message in error, you are hereby
notified that any dissemination, distribution, or copy of this email is strictly prohibited. If you have received this email in error, please
immediately notify us by return email or telephone if the sender's phone number is listed above, then promptly and permanently deletethis message.
While all reasonable care has been taken to avoid the transmission of viruses, it is the responsibility of the recipient to ensure that theonward transmission, opening, or use of this message and any attachments will not adversely affect its systems or data. No responsibilityis accepted by the company in this regard and the recipient should carry out such virus and other checks as it considers appropriate.
Originated: Delivered to:7-Nov-24
Alaska Oil & Gas Conservation Commiss 07Nov24-NR
ATTN: Meredith Guhl
333 W. 7th Ave., Suite 100
600 E 57th Place Anchorage, Alaska 99501-3539
Anchorage, AK 99518
(907) 273-1700 main (907)273-4760 fax
WELL NAME API #
SERVICE ORDER
#FIELD NAME
SERVICE
DESCRIPTION
DELIVERABLE
DESCRIPTION DATA TYPE DATE LOGGED
3S-03 50-103-20458-00-00 203-091 Kuparuk River WL IBC-CBL FINAL FIELD 10-Oct-24
2K-19A 50-103-20118-01-00 211-034 Kuparuk River WL Cutter FINAL FIELD 11-Oct-24
MT7-83 50-103-20891-01-00 224-102 Greater Mooses Tooth WL TTiX-USIT-CBL FINAL FIELD 19-Oct-24
1C-157 50-029-23754-00-00 223-038 Kuparuk River WL IBC-CBL FINAL FIELD 23-Oct-24
CD1-33A 50-103-20357-01-00 222-105 Colville River WL PERF FINAL FIELD 30-Oct-24
MT7-09 50-103-20837-00-00 222-011 Greater Mooses Tooth WL TTiX-Plug&Perf FINAL FIELD 1-Nov-24
Transmittal Receipt
________________________________ X_________________________________
Print Name Signature Date
Please return via courier or sign/scan and email a copy to Schlumberger.
Nraasch@slb.com SLB Auditor -
TRANSMITTAL DATE
TRANSMITTAL #
A Delivery Receipt signature confirms that a package (box, envelope,
etc.) has been received. The package will be handled/delivered per
standard company reception procedures. The package's contents have
not been verified but should be assumed to contain the above noted
media.
# Schlumberger-Private
T39755
T39756
T39757
T39758
T39759
T39760
1C-157 50-029-23754-00-00 223-038 Kuparuk River WL IBC-CBL FINAL FIELD 23-Oct-24
Gavin Gluyas
Digitally signed by Gavin
Gluyas
Date: 2024.11.08 08:38:26
-09'00'
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
Monty M. Myers
Drilling Manager
Hilcorp Alaska, LLC
3800 Centerpoint Drive, Suite 1400
Anchorage, AK, 99503
Re: Prudhoe Bay Field, Sag River Undefined Oil Pool, PBU NK-24
Hilcorp Alaska, LLC
Permit to Drill Number: 223-108
Surface Location: 1384' FSL, 664' FEL, Sec 36, T12N, R15E, UM, AK
Bottomhole Location: 1733' FSL, 1806' FEL, Sec 22, T12N, R16E, UM, AK
Dear Mr. Myers:
Enclosed is the approved application for the permit to drill the above referenced well.
Per Statute AS 31.05.030(d)(2)(B) and Regulation 20 AAC 25.071, composite curves for all well
logs run must be submitted to the AOGCC within 90 days after completion, suspension, or
abandonment of this well, or within 90 days of acquisition of the data, whichever occurs first.
This permit to drill does not exempt you from obtaining additional permits or an approval required
by law from other governmental agencies and does not authorize conducting drilling operations
until all other required permits and approvals have been issued. In addition, the AOGCC reserves
the right to withdraw the permit in the event it was erroneously issued.
Operations must be conducted in accordance with AS 31.05 and Title 20, Chapter 25 of the Alaska
Administrative Code unless the AOGCC specifically authorizes a variance. Failure to comply
with an applicable provision of AS 31.05, Title 20, Chapter 25 of the Alaska Administrative Code,
or an AOGCC order, or the terms and conditions of this permit may result in the revocation or
suspension of the permit.
Sincerely,
Brett W. Huber, Sr.
Chair, Commissioner
DATED this day of February 2024.
Brett W. Huber,
Sr.
Digitally signed by Brett W.
Huber, Sr.
Date: 2024.02.13 17:10:35
-06'00'
13
Stg 1 L-955 sx T-595 sx, Stg 2 L-1002 sx / T-539 sx
Drilling Manager
11/17/23
Monty M
Myers
By Grace Christianson at 11:35 am, Nov 17, 2023
* Weekly diverter function test required if surface hole lasts more than 7 days.
* BOPE test to 4000 psi. Annular to 3500 psi.
* FIT and Casing tests digital data to AOGCC upon completion.
1140
9.875"
DSR-11/20/23
PRUDHOE BAY, SAG RIVER
UNDEFINED OIL POOL
223-108
St
50-029-23773-00-00
MGR18JAN2024 A.Dewhurst 12FEB24
*&:JLC 2/13/2024
Brett W. Huber, Sr.Digitally signed by Brett W. Huber, Sr.
Date: 2024.02.13 17:11:02 -06'00'
02/13/24
02/13/24
Prudhoe Bay East
(PBU) NK-24
Drilling Program
Version 0
11/01/2023
Table of Contents
1.0 Well Summary ........................................................................................................................... 2
2.0 Management of Change Information ........................................................................................ 3
3.0 Tubular Program:...................................................................................................................... 4
4.0 Drill Pipe Information: .............................................................................................................. 4
5.0 Internal Reporting Requirements ............................................................................................. 5
6.0 Planned Wellbore Schematic ..................................................................................................... 6
7.0 Drilling / Completion Summary ................................................................................................ 7
8.0 Mandatory Regulatory Compliance / Notifications .................................................................. 8
9.0 R/U and Preparatory Work ..................................................................................................... 11
10.0 N/U 21-1/4” 2M Diverter System ............................................................................................. 12
11.0 Drill 16” Hole Section .............................................................................................................. 14
12.0 Run 13-3/8” Surface Casing .................................................................................................... 17
13.0 Cement 13-3/8” Surface Casing ............................................................................................... 22
14.0 ND Diverter, NU BOPE, & Test .............................................................................................. 27
15.0 Drill 12-1/4” Intermediate 1 Hole Section ............................................................................... 28
16.0 Run 9-5/8” Intermediate 1 Casing ........................................................................................... 33
17.0 Cement 9-5/8” Intermediate 1 Casing ..................................................................................... 36
18.0 Drill 8-1/2” x 9-7/8” Intermediate 2 Hole Section ................................................................... 39
19.0 Run 7” Intermediate 2 Liner ................................................................................................... 44
20.0 Cement 7” Intermediate 2 Liner ............................................................................................. 47
21.0 Drill 6-1/8” Production Hole Section ....................................................................................... 50
22.0 Run 4-1/2” Production Liner ................................................................................................... 54
23.0 Cement 4-1/2” Production Liner ............................................................................................. 57
24.0 Perforate 4-1/2” Liner ............................................................................................................. 60
25.0 Run Upper Completion/ Post Rig Work ................................................................................. 61
26.0 Parker 273 Rig Diverter Schematic ......................................................................................... 65
27.0 Parker 273 Rig BOP Schematic ............................................................................................... 66
28.0 Wellhead Schematic ................................................................................................................. 67
29.0 Days Vs Depth .......................................................................................................................... 68
30.0 Formation Tops & Information............................................................................................... 69
31.0 Anticipated Drilling Hazards .................................................................................................. 73
32.0 Parker 273 Rig Layout............................................................................................................. 81
33.0 FIT Procedure .......................................................................................................................... 82
34.0 Parker 273 Rig Choke Manifold Schematic ............................................................................ 83
35.0 Casing Design ........................................................................................................................... 84
36.0 12-1/4” Hole Section MASP ..................................................................................................... 85
37.0 8-1/2” x 9-7/8” Hole Section MASP ......................................................................................... 86
Page 2
Prudhoe Bay East
NK-24 Sag Producer
Drilling Procedure
38.0 6-1/8” Hole Section MASP ....................................................................................................... 87
39.0 Spider Plot (NAD 27) (Governmental Sections) ...................................................................... 88
40.0 Surface Plat (As Built) (NAD 27) ............................................................................................. 89
1.0 Well Summary
Well PBU NK-24
Pad Prudhoe Bay NK Pad
Planned Completion Type 4-1/2”production Tubing
Target Reservoir(s) Sag River Sands
Planned Well TD, MD / TVD 26,335’ MD / 9,926’ TVD
PBTD, MD / TVD 26,255’ MD / 9,929’ TVD
Surface Location (Governmental) 1,384' FSL, 664' FEL, Sec 36, T12N, R15E, UM, AK
Surface Location (NAD 27) X= 721,897.30, Y= 5,979,929.04
Top of Productive Horizon
(Governmental)746' FNL, 2,458' FEL, Sec 28, T12N, R16E, UM, AK
TPH Location (NAD 27) X= 735,247.93, Y= 5,988,769.69
BHL (Governmental) 1,733' FSL, 1,806' FEL, Sec 22, T12N, R16E, UM, AK
BHL (NAD 27) X= 741,093.00, Y= 5,991,436.00
AFE Number 231-00061
AFE Drilling Days 50
AFE Completion Days 8
Maximum Anticipated Pressure
(Surface) 3,906 psig
Maximum Anticipated Pressure
(Downhole/Reservoir) 4,912 psig
Work String
5” 19.5# S-135 XT-50
4” 14# S-139 XT-39
Parker 273 KB Elevation above MSL: 19.5 ft + 46.95 ft = 66.45 ft
GL Elevation above MSL: 19.5 ft
BOP Equipment 13-5/8” x 5M Annular, (3) ea 13-5/8” x 5M Rams
Page 3
Prudhoe Bay East
NK-24 Sag Producer
Drilling Procedure
2.0 Management of Change Information
Page 4
Prudhoe Bay East
NK-24 Sag Producer
Drilling Procedure
3.0 Tubular Program:
Hole
Section
OD (in)ID (in)Drift
(in)
Conn OD
(in)
Wt
(#/ft)
Grade Conn Burst
(psi)
Collapse
(psi)
Tension
(k-lbs)
Cond 20” 19.25 - - - X-52 Weld
16” 13-3/8” 12.415 12.259 14.375 68 L-80 BTC 5,020 2,270 1,556
12-1/4” 9-5/8” 8.681 8.525 10.625 47 L-80 DWC-C 6,870 4,760 1,086
8-1/2” 7” 6.276 6.151 7.656 26 L-80 VamTop 7,240 5,410 604
6-1/8” 4-1/2” 3.958 3.833 4.937 12.6 13Cr-80 VamTop 8,430 7,500 288
Tubing 4-1/2” 3.958 3.833 4.937 12.6 13Cr-80 VamTop 8,430 7,500 288
4.0 Drill Pipe Information:
Hole
Section
OD
(in)
ID (in)TJ ID
(in)
TJ OD
(in)
Wt
(#/ft)
Grade Conn M/U
(Min)
M/U
(Max)
Tension
(k-lbs)
Surf, Int,
& Prod
5”4.276”3.500”6.500”19.5 S-135 XT50 44,000 52,800 712klb
4”3.340”2.688” 4.875”14.0 S-135 XT39 17,700 21,200 513klb
All casing will be new, PSL 1 (100% mill inspected, 10% inspection upon delivery).
Page 5
Prudhoe Bay East
NK-24 Sag Producer
Drilling Procedure
5.0 Internal Reporting Requirements
5.1 Fill out daily drilling report and cost report on WellEz.
x Report covers operations from 6am to 6am
x Click on one of the tabs at the top to save data entered. If you click on one of the tabs to the left
of the data entry area – this will not save the data entered, and will navigate to another data entry.
x Ensure time entry adds up to 24 hours total.
x Try to capture any out of scope work as NPT. This helps later on when we pull end of well
reports.
x Enter the MD and TVD depths EVERY DAY whether you are making hole or not.
5.2 Afternoon Updates
x Submit a short operations update each work day to mmyers@hilcorp.com,
frank.roach@hilcorp.com, nathan.sperry@hilcorp.com, jengel@hilcorp.com and
joseph.lastufka@hilcorp.com
5.3 Intranet Home Page Morning Update
x Submit a short operations update each morning by 7am on the company intranet homepage. On
weekend and holidays, ensure to have this update in before 5am.
5.4 EHS Incident Reporting
x Health and Safety: Notify EHS field coordinator.
x Environmental: Drilling Environmental Coordinator
x Notify Drilling Manager & Drilling Engineer on all incidents
x Submit Hilcorp Incident report to contacts above within 24 hrs
5.5 Casing Tally
x Send final “As-Run” Casing tally to mmyers@hilcorp,com, frank.roach@hilcorp.com,
jengel@hilcorp.com and joseph.lastufka@hilcorp.com
5.6 Casing and Cement report
x Send casing and cement report for each string of casing to mmyers@hilcorp.com,
frank.roach@hilcorp.com, jengel@hilcorp.com and joseph.lastufka@hilcorp.com
5.7 Hilcorp Contact List:
Title Name Work Phone Email
Drilling Manager Monty Myers 907.777.8431 mmyers@hilcorp.com
Drilling Engineer Frank Roach 907.777.8413 frank.roach@hilcorp.com
Drilling Engineer Joe Engel 907.777.8395 jengel@hilcorp.com
Drilling Engineer Nate Sperry 907.777.8450 nathan.sperry@hilcorp.com
Completion Engineer David Bjork 907.564.4672 david.bjork@hilcorp.com
Geologist Christopher Clinkscales 907.777.8316 christopher.clinkscales@hilcorp.com
Reservoir Engineer Tanner Gansert 907.564.5234 tanner.gansert@hilcorp.com
Drilling Env. Coordinator Chris Keil 303.681.8844 chris.keil@hilcorp.com
EHS Manager Laura Green 907.777.8314 lagreen@hilcorp.com
Drilling Tech Joe Lastufka 907.777.8400 Joseph.Lastufka@hilcorp.com
_____________________________________________________________________________________
Created By: FVR 10/20/2023
PROPOSED SCHEMATIC
Niakuk Unit
Well: NK 24
Last Completed: TBD
PTD: TBD
GENERAL WELL INFO
API: TBD
Completed: TBD
CASING DETAIL
Size Type Wt/ Grade/ Conn ID Top Btm BPF
20" Conductor 129.5 / X56 / Weld N/A Surface 110’ N/A
13-3/8” Surface 68 / L-80 / BTC 12.415” Surface 6,868’ 0.1497
9-5/8” Intermediate 47 / L-80 / DWC/C 8.681” Surface 18,188’ 0.0732
7” Liner 26 / L-80 / VT 6.276” 18,038’ 19,701’ 0.0383
4-1/2” Liner 12.6 / 13Cr-80 / VT 3.958” 19,551’ 26,335’ 0.0152
TUBING DETAIL
4-1/2” Tubing 12.6 / 13Cr-80 / VT 3.958” Surface 19,551’ 0.0152
PERFORATION DETAIL
Sands Top (MD) Btm (MD) Top (TVD) Btm (TVD) FT Date Status
TD =26,335’(MD) / TD =9,926’(TVD)
13-3/8”
KB Elev: = 65.85’ / GL Elev: = 19.5’
4-1/2”
5
3
4
6
7
9-5/8”
2
PBTD =26,255’(MD) / PBTD =9,929’(TVD)
7”
4-1/2”
1
OPEN HOLE / CEMENT DETAIL
Driven
16” Stg 1 L – 955 sx / T – 595 sx, Stg 2 L – 1002 sx / T – 539 sx
12-1/4” L – 522 sx / T – 383 sx
8-1/2” 564 sx Class G
6-1/8” 795 sx Class G
JEWELRY DETAIL
No Depth ID Item
1 ~2,300’ 12.415” 13-3/8” ES Cementer
2 ~18,038’ 6.190 9-5/8” x 7” Liner Hanger/LTP
3 ~19,551’ 3.910 7” x 4-1/2” Liner Hanger/LTP
4 ~19,555’ 3.958 WLEG
5 ~19,455’ 3.856” Packer
6 TBD 3.813” GLM (Number and depth TBD)
7 ~2,100’ 3.812” Nipple profile for SSSV
WELL INCLINATION DETAIL
TREE & WELLHEAD
Tree
Wellhead
6.0
Page 7
Prudhoe Bay East
NK-24 Sag Producer
Drilling Procedure
7.0 Drilling / Completion Summary
NK-24 is a 4-string, grassroots producer planned to target the Sag River sands.
The directional plan is 16” surface hole and 13-3/8” surface casing set in the base of the SV5. A 12-1/4”
section will be drilled and 9-5/8” intermediate 1 casing set at base of the CM3. An 8-1/2”x9-7/8”
underreamed section will be drilled and 7” intermediate 2 liner set at TSGR. A 6-1/8” horizontal section will
be drilled with the sump in the Ivishak and TD in the Sag River formation. A 4-1/2” production liner will be
run and cemented in place. Perforating will be performed on the rig, and the well will be completed with 4-
1/2” production tubing.
Parker 273 will be used to drill and complete the wellbore.
Drilling operations are expected to commence approximately December 13, 2023, pending rig schedule.
Surface casing will be run to 6,868’ MD / ~4,083’ TVD and cemented to surface via a 2-stage primary cement
job. Cement returns to surface will confirm TOC at surface. If cement returns to surface are not observed,
necessary remedial action will then be discussed with AOGCC authorities.
All cuttings & mud generated during drilling operations will be hauled to one of two locations:
Primary: Prudhoe G&I on Pad 4
Secondary: the Milne Point “B” pad G&I facility
General sequence of operations:
1. MIRU Innovation Rig to well site
2. N/U & Test 21-1/4” Diverter and 16” diverter line
3. Drill 16” hole to TD of surface hole section. Run and cement 13-3/8” surface casing
4. N/D diverter, N/U wellhead, NU 13-5/8” 5M BOP & Test
5. Drill 12-1/4” to TD of intermediate 1 hole section. Run and cement 9-5/8” intermediate 1 casing
6. Drill 8-1/2”x9-7/8” to TD of intermediate 2 hole section. Run and cement 7” intermediate 2 liner
7. Drill 6-1/8” hole to TD
8. Run and cement 4-1/2” production liner
9. TCP 4-1/2” production liner
10. Run Upper Completion
11. N/D BOP, N/U Tree, RDMO
Reservoir Evaluation Plan:
1. Surface Hole: Remote Ops geologist. LWD: GR + Res
2. Intermediate 1 Hole: Field Ops geologist for casing pick. LWD: GR + Res
3. Intermediate 2 Hole: Field Ops geologist for casing pick. Triple Combo
4. Production Hole: Field Ops geologist. LWD: Triple-Combo (For geo-steering)
March 4th, 2024 from email correspondence -A.Dewhurst
Page 8
Prudhoe Bay East
NK-24 Sag Producer
Drilling Procedure
8.0 Mandatory Regulatory Compliance / Notifications
Regulatory Compliance
Ensure that our drilling and completion operations comply with all applicable AOGCC regulations,
specific regulations are listed below. If additional clarity or guidance is required on how to comply with
a specific regulation, do not hesitate to contact the Anchorage Drilling Team.
x BOPs shall be tested at (2) week intervals during the drilling and completion of PBU NK-24.
Ensure to provide AOGCC 24 hrs notice prior to testing BOPs.
x The initial and subsequent tests of BOP equipment will be to 250/4,000 psi for 5/5 min (annular to
70% rated WP, 3,500 psi on the high test for initial and subsequent tests).Confirm that these test
pressures match those specified on the APD.
x If the BOP is used to shut in on the well in a well control situation or control fluid flow from the
well bore, AOGCC is to be notified and we must test all BOP components utilized for well control
prior to the next trip into the wellbore. This pressure test will be charted same as the 14 day BOP
test.
x All AOGCC regulations within 20 AAC 25.033 “Primary well control for drilling: drilling fluid program
and drilling fluid system”.
x All AOGCC regulations within 20 AAC 25.035 “Secondary well control for primary drilling and
completion: blowout prevention equipment and diverter requirements”.
o Ensure the diverter vent line is at least 75’ away from potential ignition sources
x Ensure AOGCC approved drilling permit is posted on the rig floor and in Co Man office.
x Casing pressure test criteria in 20 AAC 25.030 (e) Casing and Cementing,“A casing pressure test
must be performed if BOPE is to be installed on a casing. The casing must be tested to hold a
minimum surface pressure equal to 50 percent of the casing internal yield pressure. The test
pressure must show stabilizing pressure and may not decline more than 10 percent within 30
minutes. The results of this test and any subsequent tests of the casing must be recorded as required
by 20 AAC 25.070(1)”.
Page 9
Prudhoe Bay East
NK-24 Sag Producer
Drilling Procedure
AOGCC Regulation Variance Requests:
x No variances are requested at this time.
Summary of Parker 273 BOP Equipment & Test Requirements
Hole Section Equipment Test Pressure (psi)
16”x 21-1/4” 2M Annular BOP w/ 16” diverter line Function Test Only
12-1/4”
x 13-5/8” x 5M Annular BOP
x 13-5/8” x Double Gate
o Blind ram in btm cavity
x Mud cross w/ 3-1/8” x 5M side outlets
x 13-5/8” x Single ram
x 3” x 5M Choke Line
x 2” x 5M Kill line
x 3” x 5M Choke manifold
x Standpipe, floor valves, etc
Initial Test: 250/4,000
Annular: 250/3,500
Subsequent Tests:
250/4,000
Annular: 250/3,500
8-1/2”
x 13-5/8” x 5M Annular BOP
x 13-5/8” x Double Gate
o Blind ram in btm cavity
x Mud cross w/ 3-1/8” x 5M side outlets
x 13-5/8” x Single ram
x 3” x 5M Choke Line
x 2” x 5M Kill line
x 3” x 5M Choke manifold
x Standpipe, floor valves, etc
6-1/8”
x 13-5/8” x 5M Annular BOP
x 13-5/8” x Double Gate
o Blind ram in btm cavity
x Mud cross w/ 3-1/8” x 5M side outlets
x 13-5/8” x Single ram
x 3” x 5M Choke Line
x 2” x 5M Kill line
x 3” x 5M Choke manifold
x Standpipe, floor valves, etc
Primary closing unit: Sara Koomey Control Unit, 3,000 psi, 316 gallon accumulator unit.
Primary closing hydraulics is provided by an electrically driven triplex pump. Secondary back-up is an air-driven
pump and emergency pressure is provided by bottled nitrogen.
The remote closing operator panels are located in the doghouse and on accumulator unit.
x 9-7/8"
Page 10
Prudhoe Bay East
NK-24 Sag Producer
Drilling Procedure
Required AOGCC Notifications:
x Well control event (BOPs utilized to shut in the well to control influx of formation fluids).
x 24 hours notice prior to spud.
x 24 hours notice prior to testing BOPs.
x 24 hours notice prior to casing running & cement operations.
x Any other notifications required in APD.
Regulatory Contact Information:
AOGCC
Jim Regg / AOGCC Inspector / (O): 907-793-1236 / Email:jim.regg@alaska.gov
Mel Rixse / Petroleum Engineer / (O): 907-793-1231 / (C): 907-223-3605 / Email:melvin.rixse@alaska.gov
Victoria Loepp / Petroleum Engineer / (O): 907-793-1247 / Email:Victoria.loepp@alaska.gov
Primary Contact for Opportunity to witness:AOGCC.Inspectors@alaska.gov
Test Inspection notification standardization format:http://doa.alaska.gov/ogc/forms/TestWitnessNotif.html
Notification / Emergency Phone: 907-793-1236 (During normal Business Hours)
Notification / Emergency Phone: 907-659-2714 (Outside normal Business Hours)
Page 11
Prudhoe Bay East
NK-24 Sag Producer
Drilling Procedure
9.0 R/U and Preparatory Work
9.1 NK-24 will utilize an existing set 20” conductor on Niakuk Pad. Ensure to review attached
surface plat and make sure rig is over appropriate conductor.
9.2 Ensure PTD and drilling program are posted in the rig office and on the rig floor.
9.3 Install landing ring.
9.4 Insure (2) 4” nipples are installed on opposite sides of the conductor with ball valves on each.
9.5 Level pad and ensure enough room for layout of rig footprint and R/U.
9.6 Rig mat footprint of rig.
9.7 Ensure any necessary wellhead equipment is staged prior to MIRU. A slip-loc starting head
should also be staged in the cellar in the event that surface casing must be set using emergency
slips.
9.8 MIRU Parker 273 Ensure rig is centered over conductor to prevent any wear to BOPE or
wellhead.
9.9 Mix spud mud for 16” surface hole section. Ensure mud temperatures are cool (<80qF).
9.10 Ensure 5-3/4” liners in mud pumps.
x NOV 12-P-160 1,600 HP mud pumps are rated at 5,085 psi, 471 gpm @ 120 spm @ 97%
volumetric efficiency.
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10.0 N/U 21-1/4” 2M Diverter System
10.1 N/U 21-1/4” diverter (Diverter Schematic attached to program).
x N/U 20”, 5M diverter “T”.
x NU Knife gate & 16” diverter line.
x N/U 20” riser to BOP Deck
x Ensure diverter R/U complies with AOGCC reg 20.AAC.25.035(C).
x Diverter line must be 75 ft from nearest ignition source
10.2 Notify AOGCC. Function test diverter.
x Ensure that the knife gate and annular are operated on the same circuit so that knife gate opens
prior to annular closure.
x Ensure that the annular closes in less than 45 seconds (API Standard 64 3rd edition March 2018
section 12.6.2 for packing element ID greater than 20”)
10.3 Ensure to set up a clearly marked “warning zone” is established on each side and ahead of the
vent line tip. “Warning Zone” must include:
x A prohibition on vehicle parking
x A prohibition on ignition sources or running equipment
x A prohibition on staged equipment or materials
x Restriction of traffic to essential foot or vehicle traffic only.
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10.4 Rig & Diverter Orientation:
x May change on location
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11.0 Drill 16” Hole Section
11.1 P/U 16” directional drilling assembly:
x Ensure BHA components have been inspected previously.
x Drift and caliper all components before M/U. Visually verify no debris inside components
that cannot be drifted.
x Ensure TF offset is measured accurately and entered correctly into the MWD software.
x Consider running a UBHO sub for wireline gyro.GWD will be the primary gyro tool.
x Have DD run hydraulics calculations on site to ensure optimum nozzle sizing.
x Drill string will be 5” 19.5# S-135.
x Run a solid float in the surface hole section.
11.2 Begin drilling out from conductor at reduced flow rates to avoid broaching the conductor.
x Consider using a trash bit to clean out conductor to mitigate potential damage from debris in
conductor.
11.3 Drill 16” hole section to section TD in the SV5. Confirm this setting depth with the Geologist
and Drilling Engineer while drilling the well, targeting the shale package in the base of the SV5.
x Monitor the area around the conductor for any signs of broaching. If broaching is observed,
stop drilling (or circulating) immediately notify Drilling Engineer.
x Efforts should be made to minimize dog legs in the surface hole. Keep DLS < 6 deg / 100.
x Hold a safety meeting with rig crews to discuss:
x Conductor broaching ops and mitigation procedures.
x Well control procedures and rig evacuation
x Flow rates, hole cleaning, mud cooling, etc.
x Pump sweeps and maintain mud rheology to ensure effective hole cleaning.
x Keep mud as cool as possible to keep from washing out permafrost.
x Pump at 450-550 gpm while drilling through permafrost. Monitor shakers closely to ensure
shaker screens and return lines can handle the flow rate.
x Once past base permafrost, slowly increase flow rate to a maximum of 650 gpm over several
stands.
x Avoid sliding when drilling across the prognosed base of permafrost, top SV6, and the
EOCU to prevent high dogleg severity.
x Ensure to not out drill hole cleaning capacity, perform clean up cycles or reduce ROP if
packoffs, increase in pump pressure or changes in hookload are seen
x Slow in/out of slips and while tripping to keep swab and surge pressures low
x Ensure shakers are functioning properly. Check for holes in screens on connections.
x Have the flowline jets hooked up and be ready to jet the flowline at the first sign of pea
gravel, clay balling or packing off.
x Adjust MW and viscosity as necessary to maintain hole stability.
x Perform gyro surveys until clean MWD surveys are seen. Take MWD surveys every stand
drilled.
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x In PBE hydrates are not present. However, continue to drill using hydrate mitigation
measures:
x Keep mud temperature as cool as possible, Target 60-70°F
x Dump and dilute as necessary to maintain temp, utilize cold water on the rig as well as
cold premade mud on trucks ready
x Drill through hydrate sands and quickly as possible, do not backream.
x While not expected to be present, monitor returns for hydrates, checking pressurized &
non-pressurized scales
x Take MWD and GWD surveys every stand until magnetic interference cleans up. After
MWD surveys show clean magnetics, only take MWD surveys.
x Surface Hole AC:
x There are no wells with a clearance factor of <1.0
11.4 16” hole mud program summary:
System Type:8.8 – 9.5 ppg Pre-Hydrated Aquagel/freshwater spud mud
Properties:
Section Density PV YP API FL HPHT Drill Solids MBT Hardness
Surface –BPRF 8.8 –9.0 10-20 20-45 NC NA <9 <35 <200
BPRF - TD 9.0 –9.5 10-30 20-45 <10 NA <9 <35 <200
System Formulation: Gel + FW spud mud
Product Quantity
Water 0.967 Bbls
Soda Ash 0.125 ppb
M-I GEL 35.0 ppb
Primary Products
Weight Material M-I WATE
Viscosifiers M-I GEL
Fluid Loss Additives M-I Pac UL (only if needed for fluid loss near TD)
Alkalinity Control Soda Ash
Bit & BHA Balling SCREENKLEEN (only if needed for balling in surface)
Contingency Products
Thinner CF Desco II, TANNATHIN & SAPP
Cement Contamination Sodium Bicarbonate & SAPP
Screen Blinding SCREENKLEEN
Lost Circulation Material NUT PLUG FINE & MEDIUM, M-I-X II FINE & Medium
Foaming/Aeration SCREENKLEEN / DEFOAM EXTRA
x PVT System: PVT will be used throughout the drilling and completion phase. Remote
monitoring stations will be available at the driller’s console, Co Man office, Toolpusher
office, and mud loggers office.
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x Casing Running:Reduce system YP as required for running casing as allowed (do not
jeopardize hole conditions). Run casing carefully to minimize surge and swab pressures.
Reduce the system rheology once the casing is landed to a YP < 20 (check with the
cementers to see what YP value they have targeted).
11.5 At TD; PU 2-3 stands off bottom to avoid washing out the hole at TD, CBU, pump tandem
sweeps and drop viscosity. Drop mud temp as low as possible as well.
11.6 RIH to bottom, proceed to BROOH to HWDP
x Pump at full drill rate (550-650 gpm) and maximize rotation.
x Pull slowly, 5 – 10 ft / minute, adjust as dictated by hole conditions
x Monitor well for any signs of packing off or losses.
x Have the flowline jets hooked up and be ready to jet the flowline at the first sign of clay
balling.
x If flow rates are reduced to combat overloaded shakers/flowline, stop back reaming until
parameters are restored.
11.7 TOOH and LD BHA
11.8 No open hole logging program planned.
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12.0 Run 13-3/8” Surface Casing
12.1 R/U and pull wearbushing.
12.2 R/U Weatherford 13-3/8” casing running equipment (CRT & Tongs)
x Ensure 13-3/8” BTC x XT50, and TXP x XT50 XO on rig floor and M/U to FOSV.
x Use BOL 2000 thread compound. Dope pin end only w/ paint brush.
x R/U of CRT if hole conditions require.
x R/U a fill up tool to fill casing while running if the CRT is not used.
x Ensure all casing has been drifted to 12.25” on the location prior to running.
x Be sure to count the total # of joints on the location before running.
x Keep hole covered while R/U casing tools.
x Record OD’s, ID’s, lengths, S/N’s of all components w/ vendor & model info.
12.3 P/U shoe joint, visually verify no debris inside joint.
12.4 Continue M/U & thread locking 120’ shoe track assembly consisting of:
13-3/8” Float Shoe
1 joint – 13-3/8”, 2 Centralizers 10’ from each end w/ stop rings
1 joint –13-3/8”, 1 Centralizer mid joint w/ stop ring
13-3/8” Float Collar w/ Stage Cementer Bypass Baffle ‘Top Hat’
1 joint –13-3/8”, 1 Centralizer mid joint with stop ring
13-3/8” HES Baffle Adaptor
x Ensure bypass baffle is correctly installed on top of float collar.
x Ensure proper operation of float equipment while picking up.
x Ensure to record S/N’s of all float equipment and stage tool components.
12.5 Float equipment and Stage tool equipment drawings:
This end up.
Bypass Baffle
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12.6 Continue running 13-3/8” surface casing
x Fill casing while running using fill up line on rig floor.
x Use BOL 2000 thread compound. Dope pin end only w/ paint brush.
x Centralization:
x 1 centralizer every joint to ~ 1000’ MD from shoe
x 1 centralizer every 2 joints from ~1,000’ above shoe to ~100’ TVD below base
permafrost (~2,280’ MD)
x Utilize a collar clamp until weight is sufficient to keep slips set properly.
x Break circulation prior to reaching the base of the permafrost if casing run indicates poor
hole conditions.
x Any packing off while running casing should be treated as a major problem. It is preferable
to POH with casing and condition hole than to risk not getting cement returns to surface.
12.7 Install the Halliburton Type H ES-II Stage tool so that it is positioned at least 100’ TVD below
the permafrost (~1,935’ MD prognosed).
x Install centralizers over couplings on 5 joints below and 5 joints above stage tool.
x Do not place tongs on ES cementer, this can cause damage to the tool.
x Ensure tool is pinned with 6 opening shear pins. This will allow the tool to open at 2800 psi.
13-3/8” 68/# L-80 BTC MUT – Make up to Mark 10 jts Take Average
Casing OD Minimum Optimum Maximum
13-3/8” 27,540 ft-lbs Mark 33,660 ft-lbs
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12.8 Continue running 13-3/8” surface casing
x Centralizers: 1 centralizer every 3rd joint to 200’ from surface
x Fill casing while running using fill up line on rig floor.
x Use BOL 2000 thread compound. Dope pin end only w/ paint brush.
x Centralization:
o 1 centralizer every 2 joints to base of conductor
12.9 Watch displacement carefully and avoid surging the hole. Slow down running speed if
necessary.
12.10 Slow in and out of slips.
12.11 P/U landing joint and M/U to casing string. Position the casing shoe +/- 10’ from TD. Strap the
landing joint prior to the casing job and mark the joint at (1) ft intervals to use as a reference
when getting the casing on depth.
12.12 Lower casing to setting depth. Confirm measurements.
12.13 Have slips staged in cellar, along with necessary equipment for the operation.
12.14 Circulate and condition mud through CRT. Reduce YP to < 20 to help ensure success of cement
job. Ensure adequate amounts of cold M/U water are available to achieve this. If possible
reciprocate casing string while conditioning mud.
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13.0 Cement 13-3/8” Surface Casing
13.1 Hold a pre-job safety meeting over the upcoming cement operations. Make room in pits for
volume gained during cement job. Ensure adequate cement displacement volume available as
well. Ensure mud & water can be delivered to the cementing unit at acceptable rates.
x How to handle cement returns at surface. Ensure vac trucks are on standby and ready to
assist.
x Which pumps will be utilized for displacement, and how fluid will be fed to displacement
pump.
x Ensure adequate amounts of water for mix fluid is heated and available in the water tanks.
x Positions and expectations of personnel involved with the cementing operation.
i. Extra hands in the pits to strap during the cement job to identify any losses
x Review test reports and ensure pump times are acceptable.
x Conduct visual inspection of all hard lines and connections used to route slurry to rig floor.
13.2 Document efficiency of all possible displacement pumps prior to cement job.
13.3 Flush through cement pump and treating iron from pump to rig floor to the shakers. This will
help ensure any debris left in the cement pump or treating iron will not be pumped downhole.
13.4 R/U cement line (if not already done so). Company Rep to witness loading of the top and
bottom plugs to ensure done in correct order.
13.5 Fill surface cement lines with water and pressure test.
13.6 Pump remaining 120 bbls 10.5 ppg tuned spacer.
13.7 Drop bottom plug (flexible bypass plug) – HEC rep to witness. Mix and pump cement per below
calculations for the 1st stage, confirm actual cement volumes with cementer after TD is reached.
13.8 Cement volume based on annular volume + 40% open hole excess. Job will consist of lead &
tail, TOC brought to stage tool.
Estimated 1st Stage Total Cement Volume:
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Cement Slurry Design (1st Stage Cement Job):
13.8 Attempt to reciprocate casing during cement pumping if hole conditions allow. Watch
reciprocation PU and SO weights, if the hole gets “sticky”, cease pipe reciprocation and continue
with the cement job.
13.9 After pumping cement, drop top plug (Shutoff plug) and displace cement with spud mud out of
mud pits, spotting water across the HEC stage cementer.
x Ensure volumes pumped and volumes returned are documented and constant communication
between mud pits, HEC Rep and HES Cementers during the entire job.
13.10 Ensure rig pump is used to displace cement. To operate the stage tool hydraulically, the plug
must be bumped.
13.11 Displacement calculation:
= (6,868-120)*.1497
=1,010 bbls
13.12 Monitor returns closely while displacing cement. Adjust pump rate if losses are seen at any
point during the job. Be prepared to pump out fluid from cellar. Have black water available to
contaminate any cement seen at surface.
13.13 If plug is not bumped at calculated strokes, double check volumes and calculations. Over
displace by no more than 50% of shoe track volume, ±4.5 bbls before consulting with Drilling
Engineer.
13.14 If plug is not bumped, consult with Drilling Engineer. Ensure the free fall stage tool opening
plug is available if needed. This is the back-up option to open the stage tool if the plugs are not
bumped.
13.15 Bump the plug with 500 psi over displacement pressure. Bleed off pressure and confirm floats
are holding. If floats do not hold, pressure up string to final circulating pressure and hold until
cement is set. Monitor pressure build up and do not let it exceed 500 psi above final circulating
pressure if pressure must be held, this is to ensure the stage tool is not prematurely opened.
Lead Slurry Tail Slurry
Density 12.0 lb/gal 15.8 lb/gal
Yield 2.35 ft3/sk 1.16 ft3/sk
Mix Water 13.92 gal/sk 4.97 gal/sk
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13.16 Increase pressure to 3,300 psi to open circulating ports in stage collar. Slightly higher pressure
may be necessary if TOC is above the stage tool. CBU and record any spacer or cement returns
to surface and volume pumped to see the returns. Circulate until YP < 20 again in preparation
for the 2nd stage of the cement job.
13.17 Be prepared for cement returns to surface. Dump cement returns in the cellar or open the shaker
bypass line to the cuttings tank. Have black water available and vac trucks ready to assist.
Ensure to flush out any rig components, hard lines and BOP stack that may have come in contact
with the cement.
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Second Stage Surface Cement Job:
13.18 Prepare for the 2
nd stage as necessary. Circulate until first stage reaches sufficient compressive
strength. Try to maintain flow rate through stage tool until 2nd stage is ready. Hold pre-job safety
meeting.
x Past wells have seen pressure increase while circulating through stage tool after reduced
rate
13.19 HEC representative to witness the loading of the ES cementer closing plug in the cementing
head.
13.20 Fill surface lines with water and pressure test.
13.21 Pump remaining 120 bbls 10.5 ppg tuned spacer.
13.22 Mix and pump cmt per below recipe for the 2
nd stage.
13.23 Cement volume based on annular volume + open hole excess (200% for lead and 100% for tail).
Job will consist of lead & tail, TOC brought to surface. However cement will continue to be
pumped until clean spacer is observed at surface.
Estimated 2nd Stage Total Cement Volume:
Cement Slurry Design (2nd stage cement job):
13.24 Continue pumping lead until uncontaminated spacer is seen at surface, then switch to tail.
13.25 After pumping cement, drop ES Cementer closing plug and displace cement with spud mud out
of mud pits.
Lead Slurry Tail Slurry
System Arctic Cem G
Density 11.0 lb/gal 15.8 lb/gal
Yield 2.54 ft3/sk 1.17 ft3/sk
Mixed
Water 12.2 gal/sk 5.08 gal/sk
516
2793
18.3
1140
102
2895
497
110'
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Drilling Procedure
13.26 Displacement calculation:
2055’ x 0.1497 bpf = 308 bbls mud
13.27 Monitor returns closely while displacing cement. Adjust pump rate if necessary. Wellhead side
outlet valve in cellar can be opened to take returns to cellar if required. Be prepared to pump out
fluid from cellar. Have black water available to retard setting of cement.
13.28 Decide ahead of time what will be done with cement returns once they are at surface. We should
circulate approximately 100 - 150 bbls of cement slurry to surface.
13.29 Land closing plug on stage collar and pressure up to 1,000 – 1,500 psi to ensure stage tool closes.
Follow instructions of Halliburton personnel. Bleed off pressure and check to ensure stage tool
has closed. Slips will be set as per plan to allow full annulus for returns during surface cement
job. Set slips.
13.30 Make initial cut on 13-3/8” final joint. L/D cut joint. Make final cut on 13-3/8”. Dress off stump.
Install 13-3/8” wellhead. If transition nipple is welded on, allow to cool as per schedule.
Ensure to report the following on wellez:
x Pre flush type, volume (bbls) & weight (ppg)
x Cement slurry type, lead or tail, volume & weight
x Pump rate while mixing, bpm, note any shutdown during mixing operations with a duration
x Pump rate while displacing, note whether displacement by pump truck or mud pumps, weight & type
of displacing fluid
x Note if casing is reciprocated or rotated during the job
x Calculated volume of displacement, actual displacement volume, whether plug bumped & bump
pressure, do floats hold
x Percent mud returns during job, if intermittent note timing during pumping of job. Final circulating
pressure
x Note if pre flush or cement returns at surface & volume
x Note time cement in place
x Note calculated top of cement
x Add any comments which would describe the success or problems during the cement job
Send final “As-Run” casing tally & casing and cement report to frank.roach@hilcorp.com and
joseph.lastufka@hilcorp.com This will be included with the EOW documentation that goes to the
AOGCC.
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14.0 ND Diverter, NU BOPE, & Test
14.1 ND the diverter T, knife gate, diverter line & NU 13-5/8” 5M casing spool.
14.2 NU 13-5/8” x 5M BOP as follows:
x BOP configuration from top down: 13-5/8” x 5M annular / 13-5/8” x 5M double gate / 13-
5/8” x 5M mud cross / 13-5/8” x 5M single gate
x Double gate ram should be dressed with 2-7/8” x 5-1/2” VBRs or 5” solid body rams in top
cavity,blind ram in bottom cavity.
x Single ram can be dressed with 2-7/8” x 5-1/2” VBRs or 5” solid body rams
x NU bell nipple, install flowline.
x Install (1) manual valve & HCR valve on kill side of mud cross. (Manual valve closest to
mud cross).
x Install (1) manual valve on choke side of mud cross. Install an HRC outside of the manual
valve
14.3 RU MPD RCD and related equipment
14.4 Run 5” BOP test plug
14.5 Test BOP to 250/4,000 psi for 5/5 min. Test annular to 250/3,500 psi for 5/5 min.
x Test with 5” test joint and test VBR’s with 2-7/8” and 5” test joints
x Smallest and largest pipes to be ran
x Confirm test pressures with PTD
x Ensure to monitor side outlet valves and annulus valve pressure gauges to ensure no pressure
is trapped underneath test plug
x Once BOPE test is complete, send a copy of the test report to town engineer and drilling tech
14.6 RD BOP test equipment
14.7 Dump and clean mud pits, send spud mud to G&I pad for injection.
14.8 Mix LSND fluid for production hole. Starting mud weight at either 9.0 ppg or matching mud
weight used to TD surface hole, whichever is heavier.
14.9 Set wearbushing in wellhead.
14.10 If needed, rack back as much 5” DP in derrick as possible to be used while drilling the hole
section.
14.11 Ensure 5-3/4” liners in mud pumps.
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Drilling Procedure
15.0 Drill 12-1/4” Intermediate 1 Hole Section
15.1 MU 12-1/4” cleanout BHA
x Milltooth bit and Motor
15.2 TIH w/ 12-1/4” BHA to stage tool. Note depth TOC tagged on AM report. Drill out stage tool.
15.3 TIH to TOC above the baffle adapter. Note depth TOC tagged on morning report.
15.4 RU and test casing to 3,000 psi / 30 min. Ensure to record volume / pressure (every ¼ bbl) and
plot on LOT/FIT graph. AOGCC reg is 50% of burst = 5,020 / 2 = ~2,510 psi. Document
incremental volume pumped (and subsequent pressure) and volume returned. Ensure rams are
used to test casing as per AOGCC Industry Guidance Bulletin 17-001.
15.5 Drill out shoetrack and 20’ of new formation.
15.6 CBU and condition mud for LOT.
15.7 Conduct LOT. Chart Test. Ensure test is recorded on same chart as casing test. Document
incremental volume pumped (and subsequent pressure) and volume returned. Submit casing test
and LOT digital data to AOGCC.
x 11.8 ppg EMW provides >>25bbls based on 11.0 ppg MW, 10.0 ppg PP (swabbed kick at 11.0
ppg EMW BHP)
15.8 POOH and LD cleanout BHA
15.9 MU 12-1/4” directional BHA
x RSS and Gr/Res
x Ensure BHA components have been inspected previously.
x Drift and caliper all components before MU. Visually verify no debris inside components that
cannot be drifted.
x Ensure MWD is RU and operational.
x Have DD run hydraulics calculations on site to ensure optimum nozzle sizing.
x Drill string will be 5” 19.5# S-135 XT50.
x Run a solid float in this hole section.
x 12-1/4” ghost reamer along 5” DP to split openhole section (~5,650’ behind bit).
0.5 ppg kick intensity above 11.0 ppg mud wt would require 12.4 ppge shoe integrity for ~25 bbl kick tolerance.
- mgr
Email promptly upon completion: melvin.rixse@alaska.gov
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15.10 12-1/4” hole section mud program summary:
System Type:9.0 – 11.0 ppg LSND drilling fluid
Properties:
Interval Density PV YP API FL HPHT Drill Solids MBT Hardness
~6,868’ – ~10,543’
Shoe –UG4
9.0 – 9.4 5 – 20 15 – 30 < 8 N/A <6% <12 <200
~10,543’ – ~15,994’
UG4 –CM3
9.4 – 10.5 5 – 20 15 – 30 < 8 N/A <6% <20 <200
~15,994’ – ~18,188’
CM3 –TD
10.5 – 11.0 5 – 20 15 – 30 < 6 N/A <6% <20 <200
Product Quantity
Water 0.916 bbls/bbl
Soda Ash 0.17 ppb
DUO-VIS 1.0 –1.5 ppb (as needed)
DUAL-FLO/ FLO-TROL 3.0 ppb
SCREENKLEEN 0.25% v/v
M-I Wate 55 ppb (as needed for wt.)
Busan 1060 2.1 gals/100 bbls
Sodium Metabisulfite 0.25 ppb (added at rig only)
Primary Products
Viscosifiers DUO-VIS/ XCD
Fluid Loss Additives FLO-TROL/ DUAL-FLO
Bit & BHA Balling SCREENKLEEN (only if needed for balling/Ugnu/WS)
Bridging Agent SAFE-CARB 20 & 40
Alkalinity Control Soda Ash
Inhibition Potassium Chloride
Lubricants LUBE 776 & LOTORQ
Corrosion Control Sodium Metabisulfite (added at rig only)
Bacteria Control Busan 1060
Contingency Products
Cement Contamination Sodium Bicarbonate & SAPP
Weight Material MI-WATE
Foaming/Aeration SCREENKLEEN, DEFOAM EXTRA
Lost Circulation Material NUT PLUG FINE & MEDIUM, SAFE-CARB 40, 250 & 750
x Density: Weighting material to be used for the hole section will be Barite. Additional
barite will be on location to weight up the active system (1) ppg above highest anticipated
MW.
x Solids Concentration: It is imperative that the solids concentration be kept low while
drilling the production hole section. Keep the shaker screen size optimized and fluid
running to near the end of the shakers. It is okay if the shakers run slightly wet to ensure
we are running the finest screens possible.
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x Rheology: Keep viscosifier additions to an absolute minimum (DUO-VIS / XCD). Do
not pump high vis sweeps, instead use tandem sweeps. Ensure 6 rpm is > 8.5 (hole
diameter) for sufficient hole cleaning
x Dump and dilute as necessary to keep drilled solids to an absolute minimum.
x MD Totco PVT will be used throughout the drilling and completion phase. Remote
monitoring stations will be available at the driller’s console, Co Man office, &
Toolpusher office.
15.11 TIH with 12-1/4” directional assembly to bottom.
15.12 Displace wellbore to LSND for upcoming hole section. Initial mud weight is either 9.0 ppg or the
mud weight used to TD surface section, whichever is higher.
15.13 Obtain initial ECD benchmark readings prior to drilling ahead.
15.14 Drill 12-1/4” hole section from 13-3/8” shoe to ~ 10,350’ MD (~200’ MD above UG4) per
Geologist and Drilling Engineer Utilizing the following parameters:
x Flow Rate: 900-975 GPM
x RPM: Maximize RPM when rotating Take the first couple stands to understand BHA
tendency. Maintenance slides may be necessary to keep sail angle
x Ensure shaker screens are set up to handle this flowrate. Ensure shakers are running slightly
wet to maximize solids removal efficiency. Check for holes in screens on every connection.
x Keep pipe movement with pumps off to slow speeds, to keep surge and swab pressures low
x Take MWD surveys every stand, can be taken more frequently if deemed necessary, ex:
concretion deflection
x Monitor Torque and Drag with pumps on every 5 stands
x Monitor ECD, pump pressure & hookload trends for hole cleaning indication. Attempt to
limit drilling ECD to 1.0 ppg over calculated cleanhole ECD.
x Good drilling and tripping practices are vital for avoidance of differential sticking. Make
every effort to keep the drill string moving whenever possible and avoid stopping with the
BHA across any sands for any extended period of time.
x Limit maximum instantaneous ROP to < 200 FPH. The SV sands will drill faster than this,
but good hole cleaning practices now reduces time needed to cleanup prior to running casing.
x Target ROP is as fast as we can clean the hole without having to backream connections
x 12-1/4” Interval A/C:
x There are no wells with a CF < 1.0
15.15 Toward the end of the above interval, begin to weight up to 9.4 ppg. Ensure mud is a consistent
9.4 ppg ~200’ before entering the UG4.
x Overpressure is not expected in the UG4 through UG1.
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Drilling Procedure
15.16 Drill 12-1/4” hole section from ~10,350’ MD to ~ 15,800’ MD (~200’ MD above CM3) per
Geologist and Drilling Engineer Utilizing the following parameters:
x Flow Rate: 800-950 GPM
x RPM: Maximize RPM when rotating
x Limit WOB to 20k max to maintain bit stability when encountering hard stringers in the
UG4-UG1
x Keep pipe movement with pumps off to slow speeds, to keep surge and swab pressures low
x Take MWD surveys every stand, can be taken more frequently if deemed necessary, ex:
concretion deflection
x Monitor Torque and Drag with pumps on every 5 stands
x Monitor ECD, pump pressure & hookload trends for hole cleaning indication. Attempt to
limit drilling ECD to 1.0 ppg over calculated cleanhole ECD.
x Good drilling and tripping practices are vital for avoidance of differential sticking. Make
every effort to keep the drill string moving whenever possible and avoid stopping with the
BHA across any sands for any extended period of time.
x Limit maximum instantaneous ROP to < 200 FPH. Good hole cleaning practices now
reduces time needed to cleanup prior to running casing.
x Target ROP is as fast as we can clean the hole without having to backream connections
x 12-1/4” Interval A/C:
x There are no wells with a CF < 1.0
15.17 Toward the end of the above interval, begin to weight up from 9.4 ppg to 10.5 ppg. Ensure mud
is a consistent 10.5 ppg ~200’ before entering the CM3.
x If using a spike fluid to weight up, ensure the fluid is heated to avoid shocking the formation
and inducing losses/breathing
15.18 Drill 12-1/4” hole section from ~15,800’ MD to section TD (projected at ~18,188’ MD) per
Geologist and Drilling Engineer Utilizing the following parameters:
x Flow Rate: 800 – 950 GPM
x RPM: Maximize RPM when rotating
x Keep pipe movement with pumps off to slow speeds, to keep surge and swab pressures low
x Take MWD surveys every stand, can be taken more frequently if deemed necessary, ex:
concretion deflection
x Monitor Torque and Drag with pumps on every 5 stands
x Monitor ECD, pump pressure & hookload trends for hole cleaning indication
x 12-1/4” Interval A/C:
x There are no wells with a CF < 1.0
15.19 Intermediate 1 Casing Pick for NK-24:
x TD for the Intermediate 1 interval is toward the base of the CM3.
x Ensure drop to 40° inc is completed before calling TD.
15.20 At TD, CBU at least 3 times at max gpm and RPM. Pump tandem sweeps if needed
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Drilling Procedure
x Monitor BU for increase in cuttings, cuttings in high sail angle hole sections come back in
waves and not a consistent stream, circulate more if necessary
x Obtain BHCT from MWD tools and provide to Halliburton cementers.
15.21 Short trip to the previous trip point
x Pull slow in and out of the slips to avoid swabbing.
x If tight hole is encountered, RIH 2-3 stands and CBU. If tight spot is at the same depth,
begin backreaming.
x If backreaming operations are commenced, continue backreaming to the shoe
x Monitor pressure, ECD, torque, and return flow to indicate potential packing off.
x If backreaming is initiated, utilize MPD to close on connections while BROOH.
x CBU minimum two times at trip point.
15.22 RIH to TD on elevators and circulate hole clean.
15.23 POOH and LD BHA.
15.24 Set test plug and change out upper rams to 9-5/8” fixed-bore rams. Test with 9-5/8” test joint to
250/4,000 psi for 5/5 minutes.
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Drilling Procedure
16.0 Run 9-5/8” Intermediate 1 Casing
16.1 Well control preparedness: In the event of an influx of formation fluids while running the
intermediate casing, the following well control response procedure will be followed:
x P/U & M/U the 5” safety joint (with 9-5/8” crossover installed on bottom, TIW valve in open
position on top, 5” handling joint above TIW). This joint shall be fully M/U and available
prior to running the first joint of 9-5/8” casing.
x Slack off and with 5” DP across the BOP, shut in ram or annular on 5” DP. Close TIW.
x Proceed with well kill operations.
16.2 R/U 9-5/8” casing running equipment.
x Ensure 9-5/8” 47# DWC/C x XT50 crossover is on rig floor and M/U to FOSV.
x Ensure all casing has been drifted on the deck prior to running.
x Be sure to count the total # of joints on the deck before running.
x Keep hole covered while R/U casing tools.
x Record OD’s, ID’s, lengths, S/N’s of all components w/ vendor & model info.
16.3 Run 9-5/8” intermediate casing
x Use BOL 2000 or equivalent thread compound. Dope pin end only w/ paint brush. Wipe off
excess.
x Centralization:
x 1 centralizer every joint to ~ 2000’ MD from surface casing shoe
x 1 centralizer every 2 joints from ~2,000’ above shoe to 1 jt below 13-3/8” surface casing
shoe (~6,900’ MD)
x Utilize a collar clamp until weight is sufficient to keep slips set properly.
x If liner length exceeds surface casing length, ensure centralizers are placed 1/jt for each joint
outside of the surface shoe.
x Obtain up and down weights of the casing before entering open hole. Record rotating torque
at 10 and 20 rpm
x See data sheets on the next page for MU torque for the 9-5/8” casing connection.
12.15 Continue M/U & thread locking 80’ shoe track assembly consisting of:
9-5/8” Float Shoe
1 joint – 9-5/8”, 2 Centralizers 10’ from each end w/ stop rings
1 joint –9-5/8”, 1 Centralizer mid joint w/ stop ring
9-5/8” Float Collar
1 joint – 9-5/8”, 1 Centralizer free floating
9-5/8” 47/# L-80 DWC/C Make-up Torque
Casing OD Minimum Optimum Maximum
9-5/8” 40,000 ft-lbs 45,000 ft-lbs 50,000 ft-lbs
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Drilling Procedure
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16.4 Watch displacement carefully and avoid surging the hole. Slow down running speed if
necessary.
16.5 Slow in and out of slips.
16.6 RIH with 9-5/8” intermediate casing to 13-3/8” shoe at ~ 6,868’ MD. CBU and establish PU,
SO, and rotating weights prior to exiting shoe.
16.7 Continue to RIH with 9-5/8” intermediate casing using the following circulation strategy (Note:
Take special care when staging pumps up and down to avoid packing off and breaking down
formation):
x 13-3/8” shoe to TD: Every 5th joint, staging up to planned cementing rate. Circulate for 5
minutes.
x If pickup/slackoff weights are deviating from trend, circulate consecutive joints down to
achieve a bottoms-up.
16.8 P/U hanger and landing joint and M/U to casing string. Casing shoe +/- 5’ from TD.
16.9 Break circulation at 1 bpm to avoid breaking down formation. Slowly stage up to full circulating
rate (planned cementing rates). Allow circulating pressures to stabilize before increasing
circulating rate to the next stage. Circulate 2 BU or more if needed to condition hole for
cementing. Reduce YP to < 18 to help ensure success of cement job. Do not start the YP drop
until casing is on bottom and cementers are ready.
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Drilling Procedure
17.0 Cement 9-5/8” Intermediate 1 Casing
17.1 Hold a pre-job safety meeting over the upcoming cement operations. Make room in pits for
volume gained during cement job. Ensure adequate cement displacement volume available as
well. Ensure mud & water can be delivered to the cementing unit at acceptable rates.
x How to handle cement returns at surface. Ensure vac trucks are on standby and ready to
assist.
x Which pumps will be utilized for displacement, and how fluid will be fed to displacement
pump.
x Ensure adequate amounts of water for mix fluid is heated and available in the water tanks.
x Positions and expectations of personnel involved with the cementing operation.
i. Extra hands in the pits to strap during the cement job to identify any losses
x Review test reports and ensure pump times are acceptable.
x Conduct visual inspection of all hard lines and connections used to route slurry to rig floor.
17.2 Document efficiency of all possible displacement pumps prior to cement job.
17.3 Flush through cement pump and treating iron from pump to rig floor to the shakers. This will
help ensure any debris left in the cement pump or treating iron will not be pumped downhole.
17.4 R/U cement line (if not already done so). Company Rep to witness loading of the top and
bottom plugs to ensure done in correct order.
17.5 Fill surface cement lines with water and pressure test.
17.6 Pump remaining 120 bbls 12.5 ppg tuned spacer.
17.7 Drop bottom plug – HEC rep to witness. Mix and pump cement per below calculations for the
1st stage, confirm actual cement volumes with cementer after TD is reached.
17.8 Cement volume based on annular volume + 40% open hole excess. Job will consist of lead &
tail, TOC brought to above TWS.
Estimated Total Cement Volume:
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Drilling Procedure
Cement Slurry Design:
17.9 Attempt to reciprocate casing during cement pumping if hole conditions allow. Watch
reciprocation PU and SO weights, if the hole gets “sticky”, cease pipe reciprocation and continue
with the cement job.
17.10 After pumping cement, drop top plug and displace with the rig pumps and LSND mud out of
mud pits.
x Ensure volumes pumped and volumes returned are documented and constant communication
between mud pits, HEC Rep and HES Cementers during the entire job.
17.11 Displacement calculation:
= (18,188-80)*.0732
= 1326 bbls
17.12 Monitor returns closely while displacing cement. Adjust pump rate if losses or packing off are
seen at any point during the job.
17.13 If plug is not bumped at calculated strokes, double check volumes and calculations. Over
displace by no more than 50% of shoe track volume, ±3.0 bbls before consulting with Drilling
Engineer.
17.14 Bump the plug with 500 psi over displacement pressure. Bleed off pressure and confirm floats
are holding. If floats do not hold, pressure up string to final circulating pressure and hold until
cement is set.
17.15 Set packoff and test per wellhead tech.
17.16 Change upper rams from 9-5/8” casing rams to 2-7/8” x 5” VBRs and test to 250/4,000 psi for
5/5 minutes with 5” test joint.
17.17 Freeze protect 13-3/8” x 9-5/8” casing annulus to ~2,200’ MD with dead crude or diesel after
cement tests indicate cement has reached 500 psi compressive strength. Note: Injection after
packoff set & tested not required as there’s ~8,100’ between planned TOC and the casing shoe.
x Initiate injection down with drilling mud. Pump 1-2 bbls down the annulus (after reaching
breakdown pressure) to ensure an open annulus in preparation for the freeze protect job.
Lead Slurry Tail Slurry
Density 13.0 lb/gal 15.3 lb/gal
Yield 1.84 ft3/sk 1.23 ft3/sk
Mix Water 10.13 gal/sk 5.57 gal/sk
Injection immediately after plug bump not necessary due to distance
between planned TOC and surface casing shoe. - mgr per Franck Roach email 01-DEC-23
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Drilling Procedure
x Freeze protect with 131 bbls of dead crude/diesel
x Ensure total injection volume injected down the annulus (including mud used to keep
annulus open) doesn’t exceed 110% of the 13-3/8” x 9-5/8” annular volume.
Ensure to report the following on wellez:
x Pre flush type, volume (bbls) & weight (ppg)
x Cement slurry type, lead or tail, volume & weight
x Pump rate while mixing, bpm, note any shutdown during mixing operations with a duration
x Pump rate while displacing, note whether displacement by pump truck or mud pumps, weight & type
of displacing fluid
x Note if casing is reciprocated or rotated during the job
x Calculated volume of displacement , actual displacement volume, whether plug bumped & bump
pressure, do floats hold
x Percent mud returns during job, if intermittent note timing during pumping of job. Final circulating
pressure
x Note if pre flush or cement returns at surface & volume
x Note time cement in place
x Note calculated top of cement
x Add any comments which would describe the success or problems during the cement job
Send final “As-Run” casing tally & casing and cement report to jengel@hilcorp.com and
joseph.lastufka@hilcorp.com This will be included with the EOW documentation that goes to the
AOGCC.
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Drilling Procedure
18.0 Drill 8-1/2” x 9-7/8” Intermediate 2 Hole Section
21.1 MU 8-1/2” x 9-7/8” directional BHA
x RSS and Triple Combo
x Ensure BHA components have been inspected previously.
x Drift and caliper all components before MU. Visually verify no debris inside components that
cannot be drifted.
x Ensure MWD is RU and operational.
x Have DD run hydraulics calculations on site to ensure optimum nozzle sizing. Hydraulics
calculations and recommended TFA is attached below.
x Halliburton underreamer will be utilized above the MWD to allow for 9-7/8” hole
x Drill string will be 5” 19.5# S-135 XT50.
x Run a solid float in the intermediate 2 hole section.
21.2 TIH w/ 8-1/2” x 9-7/8” BHA to float collar. Note depth TOC tagged on AM report. Drill out
shoe track to 10’ above float shoe.
21.3 RU and test casing to 4,000 psi / 30 min. Ensure to record volume / pressure (every ¼ bbl) and
plot on FIT graph. Document incremental volume pumped (and subsequent pressure) and
volume returned. Ensure rams are used to test casing as per AOGCC Industry Guidance Bulletin
17-001.
21.4 Intermediate 2 hole section will use the same mud used to TD Intermediate 1 hole section.
21.5 Drill out remaining shoe track and 20’ of new formation.
21.6 CBU and condition mud for FIT.
21.7 Conduct FIT to 12.9 ppg EMW. Chart Test. Ensure test is recorded on same chart as casing test.
Document incremental volume pumped (and subsequent pressure) and volume returned. Submit
casing test and FIT digital data to AOGCC.
x 12.9 ppg FIT provides >>25bbls based on 12.0 ppg MW, 10.50 ppg EMW PP (swabbed kick at
12.0 ppg EMW BHP)
21.8 8-1/2” x 9-7/8” hole section mud program summary:
System Type:10.5 – 12.0 ppg LSND drilling fluid
Email: melvin.rixse@alaska.gov
Notify AOGCC if FIT <12.9 ppg
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Drilling Procedure
Properties:
Interval Density PV YP API FL HPHT Drill Solids MBT Hardness
~18,188’ – ~18,845’
Shoe –CM1
10.5 – 10.8 5 – 20 15 – 30 < 6 N/A <6% <20 <200
~18,845’ – TD
CM1 –TD
10.8 – 12.0 5 – 20 15 – 30 < 6 <10 <6% <20 <200
Product Quantity
Water 0.916 bbls/bbl
Soda Ash 0.17 ppb
DUO-VIS 1.0 –1.5 ppb (as needed)
DUAL-FLO/ FLO-TROL 3.0 ppb
SCREENKLEEN 0.25% v/v
M-I Wate 55 ppb (as needed for wt.)
Busan 1060 2.1 gals/100 bbls
Sodium Metabisulfite 0.25 ppb (added at rig only)
Primary Products
Viscosifiers DUO-VIS/ XCD
Fluid Loss Additives FLO-TROL/ DUAL-FLO
Bit & BHA Balling SCREENKLEEN (only if needed for balling/Ugnu/WS)
Bridging Agent SAFE-CARB 20 & 40
Alkalinity Control Soda Ash
Inhibition Potassium Chloride
Lubricants LUBE 776 & LOTORQ
Corrosion Control Sodium Metabisulfite (added at rig only)
Bacteria Control Busan 1060
Contingency Products
Cement Contamination Sodium Bicarbonate & SAPP
Weight Material M-I Wate
Foaming/Aeration SCREENKLEEN, DEFOAM EXTRA
Lost Circulation Material NUT PLUG FINE & MEDIUM, SAFE-CARB 40, 250 & 750
x Density: Weighting material to be used for the hole section will be barite. Additional
barite will be on location to weight up the active system (1) ppg above highest anticipated
MW.
x Solids Concentration: It is imperative that the solids concentration be kept low while
drilling the production hole section. Keep the shaker screen size optimized and fluid
running to near the end of the shakers. It is okay if the shakers run slightly wet to ensure
we are running the finest screens possible.
x Rheology: Keep viscosifier additions to an absolute minimum (DUO-VIS / XCD). Data
suggests excessive viscosifier concentrations can decrease return permeability. Do not
pump high vis sweeps, instead use tandem sweeps. Ensure 6 rpm is > 8.5 (hole diameter)
for sufficient hole cleaning
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Drilling Procedure
x Run the centrifuge as needed while drilling the production hole, this will help with solids
removal.
x Dump and dilute as necessary to keep drilled solids to an absolute minimum.
x MD Totco PVT will be used throughout the drilling and completion phase. Remote
monitoring stations will be available at the driller’s console, Co Man office, &
Toolpusher office.
21.9 Install MPD RCD
21.10 Begin drilling 8-1/2” hole section, on-bottom staging technique:
x Tag bottom and begin drilling with 100 - 120 rpms at bit. Allow WOB to stabilize at 5-8K.
x Slowly begin bringing up rpms, monitoring stick slip and BHA vibrations
x If BHA begins to show excessive vibrations / whirl / stick slip, it may be necessary to PU
off bottom and restart on bottom staging technique. If stick slip continues, consider adding
0.5% lubes
21.11 Once ~300’ outside of the 9-5/8” shoe, pick up off bottom and activate underreamer per
Halliburton procedure. Verify reamer blades are unlocked.
21.12 Drill 8-1/2” x 9-7/8” hole section to ~18,650’ MD (~200’ above CM1) per geologist and Drilling
Engineer utilizing the following parameters:
x Flow Rate: 500-550 GPM, target min. AV’s 200 ft/min, 385 GPM
x RPM: 120+
x Keep pipe movement with pumps off to slow speeds, to keep surge and swab pressures low
x Take MWD surveys every stand, can be taken more frequently if deemed necessary, ex:
concretion deflection
x Monitor Torque and Drag with pumps on every 5 stands
x Monitor ECD, pump pressure & hookload trends for hole cleaning indication
x Good drilling and tripping practices are vital for avoidance of differential sticking. Make
every effort to keep the drill string moving whenever possible and avoid stopping with the
BHA across the sand for any extended period of time.
x Limit maximum instantaneous ROP to < 200 FPH. This is to minimize cutter damage if
encountering concretions or the Tuffs section in the Colville.
x Do not initiate backreaming while the underreamer is unlocked. Backreaming can damage
the reamer cutting blocks or possibly back off the pilot BHA.
x Prior to picking up off bottom for a connection, ensure WOB has drilled off (hookload and
torque returning to free rotating values) and RPM gradutally slowed to zero. This is to
mitigate the risk of backing off the pilot BHA.
x Target ROP is as fast as we can clean the hole without having to backream connections
x MPD will be utilized to hold ECD and monitor any pressure build up on connections.
x 8-1/2” x 9-7/8” Hole Section A/C:
X 9-7/8" -mgr
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Drilling Procedure
x There are no wells with a CF < 1.0
21.13 Toward the end of the above interval, begin to weight up from 10.5 ppg to 10.8 ppg. Ensure mud
is a consistent 10.8 ppg ~200’ before entering the CM1.
x If using a spike fluid to weight up, ensure the fluid is heated to avoid shocking the formation
and inducing losses/breathing
21.14 Drill 8-1/2” hole section from ~18,650’ to section TD per Geologist and Drilling Engineer.
x Flow Rate: 500-550 GPM, target min. AV’s 200 ft/min, 385 GPM
x RPM: 120+
x Keep pipe movement with pumps off to slow speeds, to keep surge and swab pressures low
x Take MWD surveys every stand, can be taken more frequently if deemed necessary, ex:
concretion deflection
x Monitor Torque and Drag with pumps on every 5 stands
x Monitor ECD, pump pressure & hookload trends for hole cleaning indication
x Good drilling and tripping practices are vital for avoidance of differential sticking. Make
every effort to keep the drill string moving whenever possible and avoid stopping with the
BHA across the sand for any extended period of time.
x Limit maximum instantaneous ROP to < 200 FPH. This is to minimize cutter damage if
encountering concretions or the Tuffs section in the Colville.
x Do not initiate backreaming while the underreamer is unlocked. Backreaming can damage
the reamer cutting blocks or possibly back off the pilot BHA.
x Prior to picking up off bottom for a connection, ensure WOB has drilled off (hookload and
torque returning to free rotating values) and RPM gradutally slowed to zero. This is to
mitigate the risk of backing off the pilot BHA.
x Target ROP is as fast as we can clean the hole without having to backream connections
x MPD will be utilized to hold ECD and monitor any pressure build up on connections.
x 8-1/2” x 9-7/8” Hole Section A/C:
x There are no wells with a CF < 1.0
21.15 TD will be in the SGR formation and confirmed via samples. Do not lock the underreamer
blades until SGR samples are verified. Follow Halliburton parameters for rotating while
circulating up samples with the blades unlocked.
21.16 Once samples are verified and the underreamer blades are locked closed, CBU at drilling rate
and max rotation. Pump sweeps if needed
x Monitor BU for increase in cuttings
21.17 Perform wiper trip to the 9-5/8” casing shoe
x Pulling speed 5 – 10 min/stand (slip to slip time, not including connections), adjust as
dictated by hole conditions
x If pulling tight, trip back to TD and begin backreaming operations.
x If backreaming operations are commenced, continue backreaming to the shoe
X 9-7/8" -mgr
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Drilling Procedure
21.18 CBU minimum two times at 9-5/8” shoe and clean casing with high vis sweeps.
21.19 If trip to 9-5/8” shoe is clean, continue to POOH and LD BHA for upcoming liner run.
21.20 If trip to the shoe is troublesome, run back to TD and CBU 2x or until well cleans up, whichever
comes later.
21.21 POOH and LD BHA. Rabbit DP that will be used to run liner.
Only LWD open hole logs are planned for the hole section (GR + Res). There will not be any
additional logging runs conducted.
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Drilling Procedure
19.0 Run 7” Intermediate 2 Liner
22.1 Well control preparedness: In the event of an influx of formation fluids while running the
injection liner, the following well control response procedure will be followed:
x P/U & M/U the 5” safety joint (with 7” crossover installed on bottom, TIW valve in open
position on top, 5” handling joint above TIW). This joint shall be fully M/U and available
prior to running the first joint of 7” liner.
x Slack off and with 5” DP across the BOP, shut in ram or annular on 5” DP. Close TIW.
x Proceed with well kill operations.
22.2 Change upper VBRs to 7” casing rams and test to 250 psi low, 4,000 psi high for 5/5 minutes
using 7” test joint.
22.3 R/U 7” liner running equipment.
x Ensure 7” 26# VT x XT50 crossover is on rig floor and M/U to FOSV.
x Ensure all casing has been drifted on the deck prior to running.
x Be sure to count the total # of joints on the deck before running.
x Keep hole covered while R/U casing tools.
x Record OD’s, ID’s, lengths, S/N’s of all components w/ vendor & model info.
22.4 Run 7” injection liner
x Use Vam approved thread compound. Dope pin end only w/ paint brush. Wipe off excess.
x Utilize a collar clamp until weight is sufficient to keep slips set properly.
x Use lift nubbins and stabbing guides for the liner run.
x If liner length exceeds surface casing length, ensure centralizers are placed 1/jt for each joint
outside of the surface shoe.
x Obtain up and down weights of the liner before entering open hole.
x See data sheet on the next page for MU torque for the 7” liner connections.
x Run 1 centralizer per joint.
7” 26/# L-80 VT – Make up Torque
Casing OD Minimum Optimum Maximum
7” 7,470 ft-lbs 8,300 ft-lbs 9,130 ft-lbs
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22.5 Ensure hanger/pkr will not be set in a 9-5/8” connection.
x AOGCC regulations require a minimum 100’ overlap between the inner and outer strings as
per 20 AAC 25.030(d)(6). Plan is to place liner hanger with ~150’ overlap. Do not place
liner hanger/packer across 9-5/8” connection.
22.6 Before picking up Baker SLZXP liner hanger / packer assy, count the # of joints on the pipe deck
to make sure it coincides with the pipe tally.
22.6 M/U Baker SLZXP liner top packer to 7” liner. Circulate 2 liner volumes to clear string and
allow for PAL mix to set
22.7 Note: PU, SO, ROT and torque of liner. Run liner in the hole one stand and pump through liner
hanger to ensure a clear flow path exists.
22.8 RIH with liner no faster than 30 ft/min – Watch displacement carefully and avoid surging the
hole. Slow down running speed if necessary.
x Ensure 5” DP has been drifted
x Fill drill pipe on the fly. Monitor FL and if filling is required due to losses/surging.
22.9 Slow in and out of slips. Ensure accurate slack off data is gathered during RIH. Record shoe
depth + SO depth every stand. Record torque value if it becomes necessary to rotate the string to
bottom.
22.10 Obtain up and down weights of the liner before entering open hole. Record rotating torque at 10,
& 20 RPM. If torque approaches make-up torque of liner, discontinue rotation.
22.11 Tag bottom and PU to position float shoe ~2’ off bottom.
22.12 Break circulation. Begin circulating at ~0.5 – 1 BPM and monitor pump pressures. Do not
exceed 1,600 psi while circulating for risk of prematurely setting liner hanger. Note all losses.
Confirm all pressures with Baker.
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Drilling Procedure
20.0 Cement 7” Intermediate 2 Liner
23.1 Hold a pre-job safety meeting over the upcoming cement operations. Make room in pits for
volume gained during cement job. Ensure adequate cement displacement volume available as
well. Ensure mud & water can be delivered to the cementing unit at acceptable rates.
x How to handle cement returns at surface. Ensure vac trucks are on standby and ready to
assist.
x Which pumps will be utilized for displacement, and how fluid will be fed to displacement
pump.
x Ensure adequate amounts of water for mix fluid is heated and available in the water tanks.
x Positions and expectations of personnel involved with the cementing operation.
i. Extra hands in the pits to strap during the cement job to identify any losses
x Review test reports and ensure pump times are acceptable.
x Conduct visual inspection of all hard lines and connections used to route slurry to rig floor.
23.2 Document efficiency of all possible displacement pumps prior to cement job.
23.3 Flush through cement pump and treating iron from pump to rig floor to the shakers. This will
help ensure any debris left in the cement pump or treating iron will not be pumped downhole.
23.4 R/U cement line (if not already done so). Company Rep to witness loading of the top and
bottom plugs to ensure done in correct order.
23.5 Fill surface cement lines with water and pressure test.
23.6 Pump remaining 60 bbls 12.5 ppg tuned spacer.
23.7 Cement volume based on annular volume + 40% open hole excess. Job will consist of tail slurry,
TOC brought to top of liner.
Estimated Total Cement Volume:
Cement Slurry Design:
Tail Slurry
Density 15.8 lb/gal
Yield 1.16 ft3/sk
Mix Water 4.98 gal/sk
23.0
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Drilling Procedure
23.8 Drop drillpipe dart and displace with drilling mud. If hole conditions allow – continue rotating
and reciprocating liner throughout displacement. This will ensure a high quality cement job with
100% coverage around the pipe.
23.9 Displace cement at max rate of 7 bbl/min. Reduce pump rate to 2-3 bpm prior to latching DP
dart into liner wiper plug. Note plug departure from liner hanger running tool and resume
pumping at full displacement rate. Displacement volume can be re-zeroed at this point.
23.10 If elevated displacement pressures are encountered, position liner at setting depth and cease
reciprocation. Monitor returns & pressure closely while circulating. Notify Drilling Foreman
immediately of any changes.
23.11 Bump the plug and pressure up to up as required by Baker procedure to set the liner hanger
(ensure pressure is above nominal setting pressure, but below pusher tool activation pressure).
Hold pressure for 3-5 minutes.
23.12 Slack off 20K lbs on the SLZXP liner hanger/packer to ensure the HRDE setting tool is in
compression for release from the SLZXP liner hanger/packer. Continue pressuring up 4,500 psi
to release the HRDE running tool Slack off total liner weight plus 30k to confirm hanger is set.
23.13 Bleed DP pressure to 0 psi and check floats. Pick up to expose rotating dog sub and set down
50K without pulling sleeve packoff. Pick back up without pulling sleeve packoff, begin rotating
at 10-20 RPM and set down 50K again.
23.14 PU to neutral weight, close BOP and test annulus to 1,500 psi for 5 minutes to confirm liner top
packer is set.
23.15 Bleed off pressure and open BOPE. Pickup to verify that the HRD setting tool has released. If
packer did not test, repeat setting process in 20.13. If running tool cannot be hydraulically
released, apply LH torque to mechanically release the setting.
23.16 Pressure up drill pipe to 500 psi and pick up to remove the RS packoff bushing from the RS
nipple. Bump up pressure as req’d to maintain 500 psi DP pressure while moving pipe until the
pressure drops rapidly, indicating pack-off is above the sealing area (ensure that 500 psi will be
enough to overcome hydrostatic differential at liner top)
23.17 Immediately with the loss of pressure and before DP reaches zero, initiate circulation while
picking up to position the bottom of the stinger inside the tieback sleeve. Increase pump rate to
wellbore clean up rate until the sleeve area is thoroughly cleaned.
23.18 Pick up to the high-rate circulation point above the tieback extension, mark the pipe for
reciprocation, do not re-tag the liner top, and circulate the well clean. While cement returns will
be challenging to observe, watch for them and record the estimated volume. Rotate & circulate
to clear cmt from DP.
Nominal Capacity of 5" S-135 19.5 #/ft ~.01733 bpf -mgr
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23.19 RD cementers and flush equipment. POOH, LDDP and running tool. Verify the liner top packer
received the required setting force by inspecting the rotating dog sub.
23.20 Change upper rams from 7” fixed to 2-7/8” x 5” VBRs and test with 4” and 5” test joints to 250
psi low / 4,000 psi high for 5/5 minutes. If not completed in the previous BOP test, test the lower
VBRs with 4” and 5” test joints to the same criteria.
23.21 Pressure test casing and liner to 250 psi low / 4,000 psi high for 30 minutes. Do not test until
cement has reached minimum 1,000 psi compressive strength.
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21.0 Drill 6-1/8” Production Hole Section
21.1 MU 6-1/8” directional BHA
x RSS and Triple Combo
x Ensure BHA components have been inspected previously.
x Drift and caliper all components before MU. Visually verify no debris inside components that
cannot be drifted.
x Ensure MWD is RU and operational.
x Have DD run hydraulics calculations on site to ensure optimum nozzle sizing. Hydraulics
calculations and recommended TFA is attached below.
x Drill string will be a tapered string 5” 19.5# S-135 XT50 and 4” 14.0# S-135 XT39.
x Run a solid float in the production hole section.
21.2 TIH w/ 6-1/8” BHA to float collar. Note depth TOC tagged on AM report. Drill out shoe track
to 10’ above float shoe.
21.3 RU and test casing/liner envelope to 4,000 psi / 30 min. Ensure to record volume / pressure
(every ¼ bbl) and plot on FIT graph. Document incremental volume pumped (and subsequent
pressure) and volume returned. Ensure rams are used to test casing as per AOGCC Industry
Guidance Bulletin 17-001.
21.4 Displace well to 9.7 ppg solids-free drilling fluid.
21.5 Drill out remaining shoe track and 20’ of new formation.
21.6 CBU and condition mud for FIT.
21.7 Conduct FIT to 10.9 ppg EMW. Chart Test. Ensure test is recorded on same chart as casing test.
Document incremental volume pumped (and subsequent pressure) and volume returned. Submit
casing test and FIT digital data to AOGCC.
x 10.9 ppg FIT provides >>25bbls based on 10.4 ppg MW, 9.40 ppg EMW PP (swabbed kick at
10.4 ppg EMW BHP)
21.8 6-1/8” hole section mud program summary:
System Type:9.6 – 10.4 ppg PowerPro drilling fluid
Properties:
Interval Density PV YP API FL HPHT Drill Solids MBT Hardness
Production 9.6-10.4 5 –20 15 –25 <10 NA <8 <10.0 <200
FIT and Casing Test digital data to: melvin.rixse@alaska.gov
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Product Quantity
Water 0.916 bbls/bbl
Soda Ash 0.17 ppb
POWERVIS 0.75 –1.25 ppb (as needed)
DUAL-FLO/ FLO-TROL 4.0 ppb
SCREENKLEEN 0.125% v/v
KLC 21.8 ppb (6% by wt.)
SAFE-CARB 20 22 ppb
SAFE-CARB 40 22 ppb
Salt 14.4 ppb (as needed for density)
LUBE 776 1.0% v/v
LOTORQ 1.0% v/v
Busan 1060 2.1 gals/100 bbls
Sodium Metabisulfite 0.25 ppb (added at rig only)
Primary Products
Viscosifiers POWERVIS
Fluid Loss Additives FLO-TROL/ DUAL-FLO
Bridging Agent SAFE-CARB 20 & 40
Alkalinity Control Soda Ash
Inhibition Potassium Chloride
Lubricants LUBE 776 & LOTORQ
Corrosion Control Sodium Metabisulfite (added at rig only)
Bacteria Control Busan 1060
Bridging/Density SAFE-CARB 20 & 40, Salt
Contingency Products
Cement Contamination Sodium Bicarbonate & SAPP
Weight Material SAFE-CARB 20 & 40, Salt
Foaming/Aeration SCREENKLEEN, DEFOAM EXTRA
Lost Circulation Material NUT PLUG FINE & MEDIUM, SAFE-CARB 40, 250 & 750
x Density: Primary weighting material to be used for the hole section will be sodium
chloride. Additional NaCl will be on location to weight up the active system (1) ppg
above highest anticipated MW.
x Solids Concentration: It is imperative that the solids concentration be kept low while
drilling the production hole section. Keep the shaker screen size optimized and fluid
running to near the end of the shakers. It is okay if the shakers run slightly wet to ensure
we are running the finest screens possible.
x Rheology: Keep viscosifier additions to a minimum (FLO-VIS). Utilize high vis sweeps
and tandem sweeps as necessary for hole cleaning. Ensure 6 rpm is > 8.5 (hole diameter)
for sufficient hole cleaning
x Run the centrifuge as needed while drilling the production hole, this will help with solids
removal.
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x Dump and dilute as necessary to keep drilled solids to an absolute minimum.
x MD Totco PVT will be used throughout the drilling and completion phase. Remote
monitoring stations will be available at the driller’s console, Co Man office, &
Toolpusher office.
21.9 Install MPD RCD
21.10 Begin drilling 6-1/8” hole section, on-bottom staging technique:
x Tag bottom and begin drilling with 100 - 120 rpms at bit. Allow WOB to stabilize at 5-8K.
x Slowly begin bringing up rpms, monitoring stick slip and BHA vibrations
x If BHA begins to show excessive vibrations / whirl / stick slip, it may be necessary to PU
off bottom and restart on bottom staging technique. If stick slip continues, consider adding
0.5% lubes
21.11 Drill 6-1/8” hole section to section TD per Geologist and Drilling Engineer.
x Flow Rate: 250-350 GPM, target min. AV’s in the open hole section: 200 ft/min, 175 GPM
x RPM: 120+
x Ensure shaker screens are set up to handle this flowrate. Ensure shakers are running slightly
wet to maximize solids removal efficiency. Check for holes in screens on every connection.
x Keep pipe movement with pumps off to slow speeds, to keep surge and swab pressures low
x Take MWD surveys every stand, can be taken more frequently if deemed necessary, ex:
concretion deflection
x Monitor Torque and Drag with pumps on every 5 stands
x Monitor ECD, pump pressure & hookload trends for hole cleaning indication
x Good drilling and tripping practices are vital for avoidance of differential sticking. Make
every effort to keep the drill string moving whenever possible and avoid stopping with the
BHA across the sand for any extended period of time.
x Reservoir plan is to drill down into the Ivishak sands before turning up and landing back in
the Sag River sands for the horizontal.
x There are 3 potential fault crossings (~20,700’MD, ~21,000’MD, and ~21,850’MD) in the
production interval.
x After the sump and landing back in the Sag, additional lubes will likely be required.
x After making a connection, it may be necessary to start rotation prior to bringing on the
pumps. This is to help break the static gels in the mud and minimize the ECD.
x Limit maximum instantaneous ROP to < 200 FPH. The sands will drill faster than this, but
when concretions are hit when drilling this fast, cutter damage can occur.
x Target ROP is as fast as we can clean the hole without having to backream connections
x MPD will be utilized to hold ECD and monitor pressure build up on connections.
x 6-1/8” Hole Section A/C:
x There are no wells with a CF < 1.0
21.12 At TD, CBU at drilling rate and max rotation. Pump sweeps if needed
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x Monitor BU for increase in cuttings
21.13 Perform wiper trip to the 7” liner top.
x Pulling speed 5 – 10 min/stand (slip to slip time, not including connections), adjust as
dictated by hole conditions
x If pulling tight, trip back to TD and begin backreaming operations.
x If backreaming operations are commenced, continue backreaming to the shoe
21.14 CBU minimum two times at the 7” liner top at maximum rate and clean casing with high vis
sweeps.
21.15 Trip back to TD and CBU 2x or until well cleans up, whichever comes later.
21.16 POOH and LD BHA. Rabbit DP that will be used to run liner.
Only LWD open hole logs are planned for the hole section (GR + Res). There will not be any
additional logging runs conducted.
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22.0 Run 4-1/2” Production Liner
22.1 Well control preparedness: In the event of an influx of formation fluids while running the
injection liner, the following well control response procedure will be followed:
x P/U & M/U the 5” safety joint (with 7” crossover installed on bottom, TIW valve in open
position on top, 5” handling joint above TIW). This joint shall be fully M/U and available
prior to running the first joint of 7” liner.
x Slack off and with 5” DP across the BOP, shut in ram or annular on 5” DP. Close TIW.
x Proceed with well kill operations.
22.2 Upper VBRs to cover the 4-1/2” liner, 5” x 4” drillpipe used in this operation.
22.3 R/U 4-1/2” liner running equipment.
x Ensure 4-1/2” 12.6# VT x XT50 crossover is on rig floor and M/U to FOSV.
x Ensure all casing has been drifted on the deck prior to running.
x Be sure to count the total # of joints on the deck before running.
x Keep hole covered while R/U casing tools.
x Record OD’s, ID’s, lengths, S/N’s of all components w/ vendor & model info.
22.4 Run 4-1/2” production liner
x Use Vam approved thread compound. Dope pin end only w/ paint brush. Wipe off excess.
x Utilize a collar clamp until weight is sufficient to keep slips set properly.
x Use lift nubbins and stabbing guides for the liner run.
x If liner length exceeds surface casing length, ensure centralizers are placed 1/jt for each joint
outside of the surface shoe.
x Obtain up and down weights of the liner before entering open hole.
x See data sheet on the next page for MU torque for the 4-1/2” liner connections.
x Run 2 centralizers per joint. One centralizer free floating with stop rings at 4’ and 10’ above
pin. Second centralizer locked down 10’ below box. Centralize no higher than 50’ below 7”
shoe.
4-1/2” 12.6/# 13Cr-80 VT – Make up Torque
Casing OD Minimum Optimum Maximum
4-1/2” 4,000 ft-lbs 4,440 ft-lbs 4,880 ft-lbs
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22.5 Ensure hanger/pkr will not be set in a 7” connection.
x AOGCC regulations require a minimum 100’ overlap between the inner and outer strings as
per 20 AAC 25.030(d)(6). Plan is to place liner hanger with ~150’ overlap. Do not place
liner hanger/packer across 9-5/8” connection.
22.6 Before picking up Baker SLZXP liner hanger / packer assy, count the # of joints on the pipe deck
to make sure it coincides with the pipe tally.
22.7 M/U Baker SLZXP liner top packer to 4-1/2” liner. Circulate 2 liner volumes to clear string and
allow for PAL mix to set
22.8 Note: PU, SO, ROT and torque of liner. Run liner in the hole one stand and pump through liner
hanger to ensure a clear flow path exists.
22.9 RIH with liner no faster than 30 ft/min – Watch displacement carefully and avoid surging the
hole. Slow down running speed if necessary.
x Ensure all 4” and 5” DP for the liner run has been drifted
x Fill drill pipe on the fly. Monitor FL and if filling is required due to losses/surging.
22.10 Slow in and out of slips. Ensure accurate slack off data is gathered during RIH. Record shoe
depth + SO depth every stand. Record torque value if it becomes necessary to rotate the string to
bottom.
22.11 Obtain up and down weights of the liner before entering open hole. Record rotating torque at 10,
& 20 RPM. If torque approaches make-up torque of liner, discontinue rotation.
22.12 Tag bottom and PU to position float shoe ~2’ off bottom.
22.13 Break circulation. Begin circulating at ~0.5 – 1 BPM and monitor pump pressures. Do not
exceed 1,600 psi while circulating for risk of prematurely setting liner hanger. Note all losses.
Confirm all pressures with Baker.
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23.0 Cement 4-1/2” Production Liner
23.1 Hold a pre-job safety meeting over the upcoming cement operations. Make room in pits for
volume gained during cement job. Ensure adequate cement displacement volume available as
well. Ensure mud & water can be delivered to the cementing unit at acceptable rates.
x How to handle cement returns at surface. Ensure vac trucks are on standby and ready to
assist.
x Which pumps will be utilized for displacement, and how fluid will be fed to displacement
pump.
x Ensure adequate amounts of water for mix fluid is heated and available in the water tanks.
x Positions and expectations of personnel involved with the cementing operation.
i. Extra hands in the pits to strap during the cement job to identify any losses
x Review test reports and ensure pump times are acceptable.
x Conduct visual inspection of all hard lines and connections used to route slurry to rig floor.
23.2 Document efficiency of all possible displacement pumps prior to cement job.
23.3 Flush through cement pump and treating iron from pump to rig floor to the shakers. This will
help ensure any debris left in the cement pump or treating iron will not be pumped downhole.
23.4 R/U cement line (if not already done so). Company Rep to witness loading of the top and
bottom plugs to ensure done in correct order.
23.5 Fill surface cement lines with water and pressure test.
23.6 Pump remaining 60 bbls 12.5 ppg tuned spacer.
23.7 Cement volume based on annular volume + 40% open hole excess. Job will consist of tail slurry,
TOC brought to top of liner.
Estimated Total Cement Volume:
Cement Slurry Design:
Tail Slurry
Density 15.8 lb/gal
Yield 1.16 ft3/sk
Mix Water 4.98 gal/sk
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23.8 Drop drillpipe dart and displace with perf pill before swapping to drilling mud. If hole conditions
allow – continue rotating and reciprocating liner throughout displacement. This will ensure a
high quality cement job with 100% coverage around the pipe.
23.9 Displace cement at max rate of 7 bbl/min. Reduce pump rate to 2-3 bpm prior to latching DP
dart into liner wiper plug. Note plug departure from liner hanger running tool and resume
pumping at full displacement rate. Displacement volume can be re-zeroed at this point.
23.10 If elevated displacement pressures are encountered, position casing at setting depth and cease
reciprocation. Monitor returns & pressure closely while circulating. Notify Drilling Foreman
immediately of any changes.
23.11 Bump the plug and pressure up to up as required by Baker procedure to set the liner hanger
(ensure pressure is above nominal setting pressure, but below pusher tool activation pressure).
Hold pressure for 3-5 minutes.
23.12 Slack off 20K lbs on the SLZXP liner hanger/packer to ensure the HRDE setting tool is in
compression for release from the SLZXP liner hanger/packer. Continue pressuring up 4,500 psi
to release the HRDE running tool Slack off total liner weight plus 30k to confirm hanger is set.
23.13 Bleed DP pressure to 0 psi and check floats. Pick up to expose rotating dog sub and set down
50K without pulling sleeve packoff. Pick back up without pulling sleeve packoff, begin rotating
at 10-20 RPM and set down 50K again.
23.14 PU to neutral weight, close BOP and test annulus to 1,500 psi for 5 minutes to confirm liner top
packer is set.
23.15 Bleed off pressure and open BOPE. Pickup to verify that the HRD setting tool has released. If
packer did not test, repeat setting process in 20.13. If running tool cannot be hydraulically
released, apply LH torque to mechanically release the setting.
23.16 Pressure up drill pipe to 500 psi and pick up to remove the RS packoff bushing from the RS
nipple. Bump up pressure as req’d to maintain 500 psi DP pressure while moving pipe until the
pressure drops rapidly, indicating pack-off is above the sealing area (ensure that 500 psi will be
enough to overcome hydrostatic differential at liner top)
23.17 Immediately with the loss of pressure and before DP reaches zero, initiate circulation while
picking up to position the bottom of the stinger inside the tieback sleeve. Increase pump rate to
wellbore clean up rate until the sleeve area is thoroughly cleaned.
23.18 Pick up to the high-rate circulation point above the tieback extension, mark the pipe for
reciprocation, do not re-tag the liner top, and circulate the well clean. While cement returns will
be challenging to observe, watch for them and record the estimated volume. Rotate & circulate
to clear cmt from DP.
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23.19 RD cementers and flush equipment. POOH, LDDP and running tool. Verify the liner top packer
received the required setting force by inspecting the rotating dog sub.
23.20 Pressure test casing and liner to 250 psi low / 4,000 psi high for 30 minutes. Do not test until
cement has reached minimum 1,000 psi compressive strength.
Note: Once running tool is LD, swap to the completion AFE.
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24.0 Perforate 4-1/2” Liner
24.1 If not completed in the previous BOPE test, test annular, upper and lower VBRs with 2-7/8” test
joint to 250psi low 4,000psi high for 5/5 minutes.
24.2 RU to run 2-7/8” perforating assembly per vendor procedure.
x Initial plan is ~4,000’ of 2-7/8” PowerJet Omega (or equivalent) perforation guns will be
needed.
x Exact perforated intervals to be determined by as-drilled logs data. Depths to be determined
and confirmed by Geo/OE/DE.
x Include a contingency hydraulic ball-drop disconnect in assembly
x Limit personnel on rig floor to those required to make up DPC guns.
24.3 RIH with the perforating assembly. Stop to take PU/SO weights at the top of the 7” and 4-1/2”
liners.
24.4 Space out DPC assembly by tagging the landing collar and spacing out on the upstroke.
24.5 Perforate the well per vendor procedure
x An electronic firing head will be used. Review and follow vendor procedures for arming and
firing the DPC guns.
24.6 Immediately after confirming guns have fired, POOH while keeping the hole full to get guns
above the top shot.
x This is to minimize sticking issues from possible sanding
x Flow check well and establish loss rate prior to POOH
24.7 POOH, keeping the hole filled with KWF.
x Record loss rate
x Flow check at the 4-1/2” liner top, 7” liner top, and before pulling BHA through the BOPE
24.8 POOH and LD perf gun assembly. Verify all shots have fired.
x Hydraulic tongs may be used with no backup tongs to spin out guns during rig down to
minimize trapped pressure issues.
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25.0 Run Upper Completion/ Post Rig Work
24.9 RU to run 4-1/2” 12.6#, 13Cr-80 Vam Top tubing.
x Ensure wear bushing is pulled.
x Ensure 4-1/2”, 12.6#, Vam Top x 5” XT50 crossover is on rig floor and M/U to FOSV.
x Ensure all tubing has been drifted in the pipe shed prior to running.
x Be sure to count the total # of joints in the pipe shed before running.
x Keep hole covered while RU casing tools.
x Record OD’s, ID’s, lengths, SN’s of all components with vendor & model info.
x Monitor displacement from wellbore while RIH.
24.10 PU, MU and RH with the following 4-1/2” completion jewelry (tally to be provided by
Operations Engineer):
x Torque Turn All Connections
x Tubing Jewelry to include (top to bottom):
x 1x SSSV
x 6x GLMs (size and final number to be determined by OE)
x 1x ‘X’ Nipple
x 1x Production Packer
x 1x ‘X’ Nipple
x 1x ‘XN’ Nipple with RHC profile installed
x 1x WLEG
x Tubing is 4-1/2”, 12.6#, 13Cr-80, Vam Top
4-1/2” 12.6/# 13Cr-80 Vam Top – Make up Torque
Casing OD Minimum Optimum Maximum
4-1/2” 4,000 ft-lbs 4,440 ft-lbs 4,880 ft-lbs
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24.11 Space out the completion to land such that the 4-1/2” WLEG is inserted half-way into the PBR
on the 4-1/2” production liner. Record PU and SO weights prior to picking up tubing hanger.
24.12 MU the tubing hanger and land same. Run in the lock-down screws and torque to spec.
24.13 Reverse circulate heated kill-weight brine. Circulate surface-to-surface at a maximum of 4 BPM
with brine and inhibited brine as follows:
x Clean brine within the tubing from WLEG to surface
x Inhibited brine on the annular side from the shear valve depth to the WLEG
x Clean brine on the annular side from surface down to the shear valve.
x At the end of the above displacement, reverse circulate an additional 5 bbls clean brine
x With the 5 bbls over displacement complete, spot the fluids back in place by pumping 5 bbls
clean brine down the tubing. This is to clean the RHC-M plug face before dropping the ball
& rod.
24.14 Drop the ball & rod to the RHC-M (roller stem is required due to the sail angle of the well).
24.15 Once ball & rod has landed, pressure up and set the packer.
24.16 Pressure test the tubing to 250 psi low, 4,000 psi high for 30 minutes.
24.17 Slowly bleed tubing pressure to 2,000 psi (confirm shear valve pressure) and test the IA to 250
psi low, 4,000 psi high for 30 minutes.
24.18 Hold pressure on the IA and bleed off the tubing pressure to shear the GLM valve. Confirm 2-
way communication through the shear valve.
24.19 Install and pressure test TWC from above.
24.20 ND BOPE. NU the tubing head adapter and tree.
24.21 PT the tubing hanger void to 500/5,000 psi. PT the tree to 250/5,000 psi.
24.22 RU lubricator and pull TWC.
24.23 Freeze protect the wellbore.
x Rig up to pump heated diesel down the IA, taking returns up the tubing up the tubing.
Reverse 155 bbls heated diesel into the IA. Do not exceed 3bpm while circulating.
x Shut in the IA.
x Line up to U-tube from the IA to the tubing.
x U-tube the diesel and freeze protect the tubing and IA to ~2,200’ MD.
24.24 After u-tube is complete, RU lubricator and install BPV.
24.25 Prepare to hand over well to production. Ensure necessary forms filled out and well handed over
with valve alignment as per operations personnel.
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24.26 RDMO Parker 273
i. POST RIG WELL WORK (sundry to follow)
1. Slickline/Fullbore
a. Pull BPV.
b. Change out GLV per GL ENGR
c. Pull B&R and RHC
2. Well Tie-In
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26.0 Parker 273 Rig Diverter Schematic
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27.0 Parker 273 Rig BOP Schematic
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28.0 Wellhead Schematic
See corrected wellhead schematic at end of PTD
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29.0 Days Vs Depth
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30.0 Formation Tops & Information
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31.0 Anticipated Drilling Hazards
16” Hole Section:
Lost Circulation
Ensure adequate amounts of LCM are available. Monitor fluid volumes to detect any early signs of lost
circulation. For minor seepage losses, consider adding small amounts of calcium carbonate.
Gas Hydrates/Free Gas
Gas hydrates have NOT been seen on NK Pad, nor the closest Drillsites (DS-L5 and DS-L3).
Hole Cleaning:
Maintain rheology of mud system. Sweep hole with high viscosity sweeps as necessary. Optimize
solids control equipment to maintain density, sand content, and reduce the waste stream. Monitor
ECD’s to determine if additional circulation time is necessary. In a highly deviated wellbore, pipe
rotation is critical for effective hole cleaning. Rotate at maximum RPM’s when CBU, and keep pipe
moving to avoid washing out a particular section of the hole. Ensure to clean the hole with rotation after
slide intervals. Do not out drill our ability to clean the hole.
Anti-Collison:
There are no known wells with a clearance factory <1.0. Take directional surveys every stand, take
additional surveys if necessary. Continuously monitor proximity to offset wellbores and record any
close approaches on AM report.
Well Specific A/C:
x There are no wells with a clearance factor of <1.0
Wellbore stability (Faults):
Washouts in the permafrost can be severe if the string is left circulating across it for extended periods of
time. Keep mud as cool as possible by taking on cold water and diluting often. High TOH and RIH
speeds can aggravate fragile shale/coal formations due to the pressure variations between surge and
swab. Bring the pumps on slowly after connections. Monitor conductor for any signs of broaching.
Maintain mud parameters and increase MW to combat running sands and gravel formations.
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H2S:
DS-NK is an H2S location. Below are the most recent H2S values of monitored wells in the Ivishak Pool.
Well Name H2S Level Date of Reading
#1 Closest SHL Well H2S Level NK-25 20 ppm 4/20/2012
#2 Closest SHL Well H2S Level NK-26A 84 ppm 6/15/2023
#1 Closest BHL Well H2S Level NK-42 76 ppm 2/26/2023
#2 Closest BHL Well H2S Level NK-22A 180 ppm 1/22/2023
Max. Recorded H2S on nearest Pad/Facility NK-21 1,580 ppm 6/25/2022
1. The AOGCC will be notified within 24 hours if H2S is encountered in excess of 20 ppm during
drilling operations.
2. The rig will have fully functioning automatic H2S detection equipment meeting the requirements
of 20 AAC 25.066.
3. In the event H2S is detected, wellwork will be suspended and personnel evacuated until a
detailed mitigation procedure can be developed.
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12-1/4” Hole Section:
Hole Cleaning:
Maintain rheology of mud system. Utilize sweeps to evaluate and maintain good hole cleaning
(weighted, high-vis, and low-vis/high-vis tandem sweeps all have seen success, depending on hole
angle). Ensure shakers are set up with appropriate screens to maximize solids removal efficiency. Run
centrifuge as needed to control drilled solids. Monitor ECDs to determine if additional circulation time
is necessary. In a highly deviated wellbore, pipe rotation is critical for effective hole cleaning. Rotate at
maximum RPMs when CBU and keep pipe moving to avoid washing out a particular section of the
wellbore. Ensure to clean the hole with rotation after slide intervals. Do not out drill our ability to clean
the hole. Maintain circulation rate of > 800 gpm
Lost Circulation:
Ensure adequate amounts of LCM are available. Monitor fluid volumes to detect any early signs of lost
circulation. For minor seepage losses, consider adding small amounts of calcium carbonate.
Faulting:
Crossing faults, known or unknown, can result in drilling into unstable formations that may impact
future drilling and liner runs. Talk with Geologist to ensure all known faults are identified and prepared
for accordingly.
H2S:
DS-NK is an H2S location. Below are the most recent H2S values of monitored wells in the Ivishak Pool.
Well Name H2S Level Date of Reading
#1 Closest SHL Well H2S Level NK-25 20 ppm 4/20/2012
#2 Closest SHL Well H2S Level NK-26A 84 ppm 6/15/2023
#1 Closest BHL Well H2S Level NK-42 76 ppm 2/26/2023
#2 Closest BHL Well H2S Level NK-22A 180 ppm 1/22/2023
Max. Recorded H2S on nearest Pad/Facility NK-21 1,580 ppm 6/25/2022
1. The AOGCC will be notified within 24 hours if H2S is encountered in excess of 20 ppm during
drilling operations.
2. The rig will have fully functioning automatic H2S detection equipment meeting the requirements
of 20 AAC 25.066.
3. In the event H2S is detected, wellwork will be suspended and personnel evacuated until a
detailed mitigation procedure can be developed.
Page 76
Prudhoe Bay East
NK-24 Sag Producer
Drilling Procedure
Abnormal Pressures and Temperatures:
P Reservoir pressures are expected to be normal. Utilize MPD to mitigate any abnormal pressure seen.
Ugnu/West Sak Hardstreaks:
Hard formations (which are not necessarily predictable) can be encountered resulting in damage to PDC
cutters. Damage occurs due to high impact loading of the bit cutting structure when hard streaks are hit
at high ROP. Follow the appropriate mitigation strategy of reducing rotary speed while maintaining
WOB.
Colville Breathing:
This is associated with higher mud weights and higher ECD’s in the Colville mudstones. Monitor ECDs
and mud properties. Fingerprint connections to confirm breathing and not a well control event.
Anti-Collision
Take directional surveys every stand, take additional surveys if necessary. Continuously monitor
drilling parameters for signs of magnetic interference with another well. Reference A/C report in
directional plan.
12-1/4” Hole Section Specific AC:
x There are no wells with a CF < 1.0
0.520 psi/ft predicted at 15,994' MD per geo prog. -A.Dewhurst 20NOV23
Page 77
Prudhoe Bay East
NK-24 Sag Producer
Drilling Procedure
8-1/2” x 9-7/8” Hole Section:
Hole Cleaning:
Maintain rheology of mud system. Utilize sweeps to evaluate and maintain good hole cleaning
(weighted, high-vis, and low-vis/high-vis tandem sweeps all have seen success, depending on hole
angle). Ensure shakers are set up with appropriate screens to maximize solids removal efficiency. Run
centrifuge as needed to control drilled solids. Monitor ECDs to determine if additional circulation time
is necessary. In a highly deviated wellbore, pipe rotation is critical for effective hole cleaning. Rotate at
maximum RPMs when CBU and keep pipe moving to avoid washing out a particular section of the
wellbore. Ensure to clean the hole with rotation after slide intervals. Do not out drill our ability to clean
the hole. Reduce ROP (as opposed to flow rate) to control ECD. Maintain circulation rate of > 500 gpm
Lost Circulation:
Ensure adequate amounts of LCM are available. Monitor fluid volumes to detect any early signs of lost
circulation. For minor seepage losses, consider adding small amounts of calcium carbonate.
Faulting:
No faults are forecasted to be crossed in this interval. Crossing faults, known or unknown, can result in
drilling into unstable formations that may impact future drilling and liner runs. Talk with Geologist to
ensure all known faults are identified and prepared for accordingly.
H2S:
DS-NK is an H2S location. Below are the most recent H2S values of monitored wells in the Ivishak Pool.
Well Name H2S Level Date of Reading
#1 Closest SHL Well H2S Level NK-25 20 ppm 4/20/2012
#2 Closest SHL Well H2S Level NK-26A 84 ppm 6/15/2023
#1 Closest BHL Well H2S Level NK-42 76 ppm 2/26/2023
#2 Closest BHL Well H2S Level NK-22A 180 ppm 1/22/2023
Max. Recorded H2S on nearest Pad/Facility NK-21 1,580 ppm 6/25/2022
1. The AOGCC will be notified within 24 hours if H2S is encountered in excess of 20 ppm during
drilling operations.
2. The rig will have fully functioning automatic H2S detection equipment meeting the requirements
of 20 AAC 25.066.
3. In the event H2S is detected, wellwork will be suspended and personnel evacuated until a
detailed mitigation procedure can be developed.
Page 78
Prudhoe Bay East
NK-24 Sag Producer
Drilling Procedure
Abnormal Pressures and Temperatures:
Reservoir pressures are expected to be normal. Utilize MPD to mitigate any abnormal pressure seen.
Colville Breathing:
This is associated with higher mud weights and higher ECD’s in the Colville mudstones. Monitor ECDs
and mud properties. Fingerprint connections to confirm breathing and not a well control event.
Tuffs or “Shale Wall” (CM1):
The top of the CM1 is lithologically similar to the shallower CM intervals, but contains some
interbedded volcanic tuff beds. Tuffs are hard and abrasive, especially at the top of the interval. Reduce
WOB and ROP to maximize bit and reamer life when drilling through the CM1.
Formation Breakout (HRZ/Kingak instability):
This is related to the fissile (finely laminated) nature of the formation in conjunction with higher pore
pressure, which requires higher mud weight to maintain wellbore stability. If splintering cuttings are
observed at surface, additional circulations and mud weight may be required.
Anti-Collision
Take directional surveys every stand, take additional surveys if necessary. Continuously monitor
drilling parameters for signs of magnetic interference with another well. Reference A/C report in
directional plan.
8.5” x 9-7/8” Hole Section Specific AC:
x There are no wells with a CF < 1.0.
0.545 psi/ft gradient predicted at 18,845' MD per geo prog. -A.Dewhurst 20NOV23
Page 79
Prudhoe Bay East
NK-24 Sag Producer
Drilling Procedure
6-1/8” Hole Section:
Hole Cleaning:
Maintain rheology of mud system. Utilize sweeps to evaluate and maintain good hole cleaning
(weighted, high-vis, and low-vis/high-vis tandem sweeps all have seen success, depending on hole
angle). Ensure shakers are set up with appropriate screens to maximize solids removal efficiency. Run
centrifuge as needed to control drilled solids. Monitor ECDs to determine if additional circulation time
is necessary. In a highly deviated wellbore, pipe rotation is critical for effective hole cleaning. Rotate at
maximum RPMs when CBU and keep pipe moving to avoid washing out a particular section of the
wellbore. Ensure to clean the hole with rotation after slide intervals. Do not out drill our ability to clean
the hole. Reduce ROP (as opposed to flow rate) to control ECD. Maintain circulation rate of > 250 gpm
Lost Circulation:
Ensure adequate amounts of LCM are available. Monitor fluid volumes to detect any early signs of lost
circulation. For minor seepage losses, consider adding small amounts of calcium carbonate.
Faulting:
There are 3 possible fault crossings in this interval (2 high probability and 1 low probability). All 3
faults have throws < 100’ and have a low lost circulation risk. Crossing faults, known or unknown, can
result in drilling into unstable formations that may impact future drilling and liner runs. Talk with
Geologist to ensure all known faults are identified and prepared for accordingly.
H2S:
DS-NK is an H2S location. Below are the most recent H2S values of monitored wells in the Ivishak Pool.
Well Name H2S Level Date of Reading
#1 Closest SHL Well H2S Level NK-25 20 ppm 4/20/2012
#2 Closest SHL Well H2S Level NK-26A 84 ppm 6/15/2023
#1 Closest BHL Well H2S Level NK-42 76 ppm 2/26/2023
#2 Closest BHL Well H2S Level NK-22A 180 ppm 1/22/2023
Max. Recorded H2S on nearest Pad/Facility NK-21 1,580 ppm 6/25/2022
4. The AOGCC will be notified within 24 hours if H2S is encountered in excess of 20 ppm during
drilling operations.
5. The rig will have fully functioning automatic H2S detection equipment meeting the requirements
of 20 AAC 25.066.
Page 80
Prudhoe Bay East
NK-24 Sag Producer
Drilling Procedure
6. In the event H2S is detected, wellwork will be suspended and personnel evacuated until a
detailed mitigation procedure can be developed.
Abnormal Pressures and Temperatures:
Reservoir pressures are expected to be normal. Utilize MPD to mitigate any abnormal pressure seen.
Shublik Breathing:
This is associated with higher mud weights and higher ECD’s in the Shublik carbonates. This is
different in comparison to the breathing potential in the Colville Mudstones in that the formation will
take fluid, but release gas. If treated like a traditional influx, the subsequent weight-up will start the
process over with more fluid being lost and then more gas being released. Circulating out the gas via
driller’s method and monitor pressures to determine if this is a breathing event or if it is an influx.
Zone 4 and Zone 3 Conglomerates; Zone 2 Hard Streaks:
The top of the CM1 is lithologically similar to the shallower CM intervals, but contains some
interbedded volcanic tuff beds. Tuffs are hard and abrasive, especially at the top of the interval. Reduce
WOB and ROP to maximize bit and reamer life when drilling through the CM1.
Formation Breakout (HRZ/Kingak instability):
This is related to the fissile (finely laminated) nature of the formation in conjunction with higher pore
pressure, which requires higher mud weight to maintain wellbore stability. If splintering cuttings are
observed at surface, additional circulations and mud weight may be required.
Anti-Collision
Take directional surveys every stand, take additional surveys if necessary. Continuously monitor
drilling parameters for signs of magnetic interference with another well. Reference A/C report in
directional plan.
6-1/8” Hole Section Specific AC:
x There are no wells with a CF < 1.0.
Page 81
Prudhoe Bay East
NK-24 Sag Producer
Drilling Procedure
32.0 Parker 273 Rig Layout
Page 82
Prudhoe Bay East
NK-24 Sag Producer
Drilling Procedure
33.0 FIT Procedure
Formation Integrity Test (FIT) and
Leak-Off Test (LOT) Procedures
Procedure for FIT:
1. Drill 20' of new formation below the casing shoe (this does not include rat hole below the shoe).
2. Circulate the hole to establish a uniform mud density throughout the system. P/U into the shoe.
3. Close the blowout preventer (ram or annular).
4. Pump down the drill stem at 1/4 to 1/2 bpm.
5. On a graph with the recent casing test already shown, plot the fluid pumped (volume or strokes) vs.
drill pipe pressure until appropriate surface pressure is achieved for FIT at shoe.
6. Shut down at required surface pressure. Hold for a minimum 10 minutes or until the pressure stabilizes.
Record time vs. pressure in 1-minute intervals.
7. Bleed the pressure off and record the fluid volume recovered.
The pre-determined surface pressure for each formation integrity test is based on achieving an EMW at
least 1.0 ppg higher than the estimated reservoir pressure, and allowing for an appropriate amount of kick
tolerance in case well control measures are required.
Where required, the LOT is performed in the same fashion as the formation integrity test. Instead of
stopping at a pre-determined point, surface pressure is increased until the formation begins to take fluid;
at this point the pressure will continue to rise, but at a slower rate. The system is shut in and pressure
monitored as with an FIT.
Ensure that casing test and subsequent FIT tests are recorded on the same chart. Document incremental
volume pumped and returned during test.
Page 83
Prudhoe Bay East
NK-24 Sag Producer
Drilling Procedure
34.0 Parker 273 Rig Choke Manifold Schematic
Page 84
Prudhoe Bay East
NK-24 Sag Producer
Drilling Procedure
35.0 Casing Design
Page 85
Prudhoe Bay East
NK-24 Sag Producer
Drilling Procedure
36.0 12-1/4” Hole Section MASP
Page 86
Prudhoe Bay East
NK-24 Sag Producer
Drilling Procedure
37.0 8-1/2” x 9-7/8” Hole Section MASP
Page 87
Prudhoe Bay East
NK-24 Sag Producer
Drilling Procedure
38.0 6-1/8” Hole Section MASP
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33-12-16
PRUDHOE BAY
UN NIA NK-25
PRUDHOE BAY
UN NIA NK-23
PRUDHOE
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PRUDHOE BAY
UN NIA NK-38
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NK-04
NK-05
NK-06
NK-12
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NK-15A
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NK-18
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NK-20
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NK-21 NK-22
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Sec.
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Sec. 22
Sec. 24
Sec. 21
Sec. 15
Sec. 17
Sec. 33
Sec. 4Sec. 5
Sec. 27
Sec. 32
Sec. 8
Sec. 36
Sec. 3
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Sec. 25
Sec. 28
Sec. 29
Sec. 34
Sec. 12 Sec. 9 Sec. 10
Sec. 31
(591)
Sec. 18
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Sec. 19
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Sec. 6
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Sec. 30
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Sec. 7
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DSNK
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ADL390314
ADL28320
ADL34635
ADL34625
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NK-24_SHL
NK-24_TPH
NK-24_BHL
Map Date: 2/9/2024
Prudhoe Bay Unit
NK-24 wp19 Well E0 2,700 5,400Feet
Legend
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Page 88
Prudhoe Bay East
NK-24 Sag Producer
Drilling Procedure
39.0 Spider Plot (NAD 27) (Governmental Sections)
Superseded by updated plat. -A.Dewhurst 09FEB24
Page 89
Prudhoe Bay East
NK-24 Sag Producer
Drilling Procedure
40.0 Surface Plat (As Built) (NAD 27)
Page 90
Prudhoe Bay East
NK-24 Sag Producer
Drilling Procedure
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End Dir : 18187.86' M
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Start Dir 6º/100' : 19693' M
D, 9738.85'TVD
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Start Dir 3º/100' : 20776.33' M
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End Dir : 20793.43' M
D, 10042.99' TVD
Fault #2
Start Dir 6º/100' : 21273.07' M
D, 9918.18'TVD
Start Dir 2º/100' : 21491.25' M
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End Dir : 21540.91' M
D, 9884.55' TVD
Fault #3
Start Dir 2º/100' : 21922.07' M
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End Dir : 21927.83' M
D, 9877.75' TVD
Start Dir 3º/100' : 22720.47' M
D, 9862.85'TVD
End Dir : 23064.18' M
D, 9873.87' TVD
Start Dir 2º/100' : 23758.38' M
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Start Dir 3º/100' : 23899.96' M
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End Dir : 24159.67' M
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Start Dir 3º/100' : 24978.39' M
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Mel,
Thecommentwastheretolettherigteamknowthatthereisn’tanurgencytoestablishinjecƟondueto
thedistancebetween9Ͳ5/8”TOCandthe13Ͳ3/8”casingshoe.Thecementvolumepumpedwillnot
makeittotheshoe,evenifwehavegaugehole.
Asanexample,inPAVE1Ͳ1,plannedTOCofthe9Ͳ5/8”intermediatecementjobis~1,350’MDaway
fromthe13Ͳ3/8”surfacecasingshoe.Theplannedopenholeexcessis40%forthecementjob.Ifweend
upwithgaugehole,thiswouldputTOCinsidethesurfacecasingandwouldjeopardizetheOAfreeze
protect.Thus,it’scalledoutaŌerbumpingtheplugtoinjectdowntheannulustoconĮrmapathfor
freezeprotectandconĮrmthepathissƟllopenwithhourlyinjecƟonsunƟlthecementstartsbuilding
compressivestrength.
ThestatementcouldhavebeenwriƩenbeƩer.Itwillnowread:
“InjecƟon immediately aŌer plug bump not necessary due to distance between
planned TOC and surface casing shoe.”
Thisway,itwillnotconŇictwiththefollowingbulletpointthattalksaboutestablishinginjecƟon.
Regards,
FrankVRoach
DrillingEngineer
Hilcorp Alaska, LLC
907.854.2321mobile
907.777.8413office
From:Rixse,MelvinG(OGC)<melvin.rixse@alaska.gov>
Sent:Monday,November27,202317:05
To:FrankRoach<Frank.Roach@hilcorp.com>
Subject:[EXTERNAL]NKͲ24FreezeProtectQuestion
Frank,
Pleaseexplainthecomment“Note:InjecƟonaŌerpackoīsetandtestednotrequiredas……..andthe
casingshoe.”
MelRixse
CAUTION:Externalsender.DONOTopenlinksorattachmentsfromUNKNOWNsenders.
SeniorPetroleumEngineer(PE)
AlaskaOilandGasConservationCommission
907Ͳ793Ͳ1231Office
907Ͳ297Ͳ8474Cell
Mel,
Nosir.TheenƟreIntermediate2secƟonwillbeunderreamedto9Ͳ7/8”.SecƟonshouldread:“Drill8Ͳ
1/2”x9Ͳ7/8”holesecƟonfrom~18,650’tosecƟonTD…”
Regards,
FrankVRoach
DrillingEngineer
Hilcorp Alaska, LLC
907.854.2321mobile
907.777.8413office
From:Rixse,MelvinG(OGC)<melvin.rixse@alaska.gov>
Sent:Monday,November27,202317:16
To:FrankRoach<Frank.Roach@hilcorp.com>
Subject:[EXTERNAL]NKͲ24holesizereduction?
Frank,
AreyoureducingholesizeforthissecƟon?
MelRixse
SeniorPetroleumEngineer(PE)
AlaskaOilandGasConservationCommission
907Ͳ793Ͳ1231Office
907Ͳ297Ͳ8474Cell
CAUTION:Externalsender.DONOTopenlinksorattachmentsfromUNKNOWNsenders.
1
Dewhurst, Andrew D (OGC)
From:Frank Roach <Frank.Roach@hilcorp.com>
Sent:Tuesday, February 13, 2024 08:51
To:Joseph Lastufka; Dewhurst, Andrew D (OGC); Davies, Stephen F (OGC); Guhl, Meredith D (OGC); Roby, David S (OGC); Rixse,
Melvin G (OGC)
Subject:RE: [EXTERNAL] RE: PBU NK-24 (PTD unknown) updated map
Andrew,
Joeiscorrect.TherigdealtwithphaseweatherduringthemovetoDSͲ11andsubsequentlytooklongertorigup.That
putusabout5daysbehindplanfromthestart,butwe’vebeenholdingthat5dayssincespud.
Currently,weareforecasƟngtoreleasearoundMarch4.
Regards,
FrankVRoach
DrillingEngineer
Hilcorp Alaska, LLC
907.854.2321mobile
907.777.8413office
From:JosephLastufka<Joseph.Lastufka@hilcorp.com>
Sent:Monday,February12,202417:07
To:Dewhurst,AndrewD(OGC)<andrew.dewhurst@alaska.gov>;Davies,StephenF(OGC)<steve.davies@alaska.gov>;
Guhl,MeredithD(OGC)<meredith.guhl@alaska.gov>;Roby,DavidS(OGC)<dave.roby@alaska.gov>;Rixse,MelvinG
(OGC)<melvin.rixse@alaska.gov>;FrankRoach<Frank.Roach@hilcorp.com>
Subject:RE:[EXTERNAL]RE:PBUNKͲ24(PTDunknown)updatedmap
Andy,
ThatlookspreƩyaccuratebutitalsomaybeanextraweek(~3/4orso)ͲI’llhavetodefertoFrankRoachthedrilling
engineerforconĮrmaƟon.Oneofuswillgetbacktoyoutomorrow.Thanksforchecking!
Thanks,
Joe Lastufka
Sr. Drilling Technologist
Hilcorp North Slope, LLC
Office: (907)777-8400, Cell:(907)227-8496
From:Dewhurst,AndrewD(OGC)<andrew.dewhurst@alaska.gov>
Sent:Monday,February12,20244:48PM
To:JosephLastufka<Joseph.Lastufka@hilcorp.com>;Davies,StephenF(OGC)<steve.davies@alaska.gov>;Guhl,
MeredithD(OGC)<meredith.guhl@alaska.gov>;Roby,DavidS(OGC)<dave.roby@alaska.gov>;Rixse,MelvinG(OGC)
<melvin.rixse@alaska.gov>
Subject:[EXTERNAL]RE:PBUNKͲ24(PTDunknown)updatedmap
Youdon'toftengetemailfromfrank.roach@hilcorp.com.Learnwhythisisimportant
CAUTION:Externalsender.DONOTopenlinksorattachmentsfromUNKNOWNsenders.
2
Joe,
IwrotedownthatthePBUNKͲ24wasscheduledtospudonthe28thofthismonth.Isthatcorrect?
Andy
From:JosephLastufka<Joseph.Lastufka@hilcorp.com>
Sent:Friday,February9,202410:18
To:Davies,StephenF(OGC)<steve.davies@alaska.gov>;Dewhurst,AndrewD(OGC)<andrew.dewhurst@alaska.gov>;
Guhl,MeredithD(OGC)<meredith.guhl@alaska.gov>;Roby,DavidS(OGC)<dave.roby@alaska.gov>;Rixse,MelvinG
(OGC)<melvin.rixse@alaska.gov>
Cc:FrankRoach<Frank.Roach@hilcorp.com>;MichaelSchoetz<mschoetz@hilcorp.com>
Subject:PBUNKͲ24(PTDunknown)updatedmap
Hello,
WantedtoprovideyouwithanupdatedmapforPBUNKͲ24submiƩedon11/17/23.LookslikethemapincludedNiakuk
PoolwhentheyshouldhavebeenlabeledandshownasRavenPool.
ForclariĮcaƟon,HilcorpisawarethattheproducƟveintervalasshowninthismapisoutsideofthecurrentRavenPool
aīectedarea.Hilcorphasapendingexpansionrequestthatifgrantedwillencompasstheproposedwellbore.
Thanks,
Joe Lastufka
Sr. Drilling Technologist
Hilcorp North Slope, LLC
Office: (907)777-8400, Cell:(907)227-8496
The information contained in this email message is confidential and may be legally privileged and is intended only for the use of the individual or entity named
above. If you are not an intended recipient or if you have received this message in error, you are hereby notified that any dissemination, distribution, or copy of this
email is strictly prohibited. If you have received this email in error, please immediately notify us by return email or telephone if the sender's phone number is listed
above, then promptly and permanently delete this message.
While all reasonable care has been taken to avoid the transmission of viruses, it is the responsibility of the recipient to ensure that the onward transmission,
opening, or use of this message and any attachments will not adversely affect its systems or data. No responsibility is accepted by the company in this regard and
the recipient should carry out such virus and other checks as it considers appropriate.
The information contained in this email message is confidential and may be legally privileged and is intended only for the use of the individual or entity named
above. If you are not an intended recipient or if you have received this message in error, you are hereby notified that any dissemination, distribution, or copy of this
email is strictly prohibited. If you have received this email in error, please immediately notify us by return email or telephone if the sender's phone number is listed
above, then promptly and permanently delete this message.
While all reasonable care has been taken to avoid the transmission of viruses, it is the responsibility of the recipient to ensure that the onward transmission,
opening, or use of this message and any attachments will not adversely affect its systems or data. No responsibility is accepted by the company in this regard and
the recipient should carry out such virus and other checks as it considers appropriate.
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.
1
Dewhurst, Andrew D (OGC)
From:Joseph Lastufka <Joseph.Lastufka@hilcorp.com>
Sent:Friday, February 9, 2024 10:18
To:Davies, Stephen F (OGC); Dewhurst, Andrew D (OGC); Guhl, Meredith D (OGC); Roby, David S (OGC); Rixse, Melvin G (OGC)
Cc:Frank Roach; Michael Schoetz
Subject:PBU NK-24 (PTD unknown) updated map
Attachments:NorthSlope_PBU_NK-24_wp19.pdf
Follow Up Flag:Follow up
Flag Status:Completed
Hello,
WantedtoprovideyouwithanupdatedmapforPBUNKͲ24submiƩedon11/17/23.LookslikethemapincludedNiakuk
PoolwhentheyshouldhavebeenlabeledandshownasRavenPool.
ForclariĮcaƟon,HilcorpisawarethattheproducƟveintervalasshowninthismapisoutsideofthecurrentRavenPool
aīectedarea.Hilcorphasapendingexpansionrequestthatifgrantedwillencompasstheproposedwellbore.
Thanks,
Joe Lastufka
Sr. Drilling Technologist
Hilcorp North Slope, LLC
Office: (907)777-8400, Cell:(907)227-8496
The information contained in this email message is confidential and may be legally privileged and is intended only for the use of the individual or entity named
above. If you are not an intended recipient or if you have received this message in error, you are hereby notified that any dissemination, distribution, or copy of this
email is strictly prohibited. If you have received this email in error, please immediately notify us by return email or telephone if the sender's phone number is listed
above, then promptly and permanently delete this message.
While all reasonable care has been taken to avoid the transmission of viruses, it is the responsibility of the recipient to ensure that the onward transmission,
opening, or use of this message and any attachments will not adversely affect its systems or data. No responsibility is accepted by the company in this regard and
the recipient should carry out such virus and other checks as it considers appropriate.
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.
1
Dewhurst, Andrew D (OGC)
From:Joseph Lastufka <Joseph.Lastufka@hilcorp.com>
Sent:Thursday, December 7, 2023 16:31
To:AOGCC Permitting (CED sponsored)
Cc:Davies, Stephen F (OGC); Dewhurst, Andrew D (OGC); Guhl, Meredith D (OGC)
Subject:PBU 11-42 10-401 Permit to Drill
Attachments:PBU 11-42 10-401.pdf; 11-42 wp10.txt; PBU 11-42 10-401.xml
Hello,
DuetoequipmentavailabilityissueswithtoolsplannedforNKͲ24,thishascontributedtothespuddateonNKͲ24being
pushedlaterthanDecember13,andtomoveforwardwithPBU11Ͳ42.PleaseletmeknowifyouhaveanyquesƟons.
Thanks!
Thanks,
Joe Lastufka
Sr. Drilling Technologist
Hilcorp North Slope, LLC
Office: (907)777-8400, Cell:(907)227-8496
The information contained in this email message is confidential and may be legally privileged and is intended only for the use of the individual or entity named
above. If you are not an intended recipient or if you have received this message in error, you are hereby notified that any dissemination, distribution, or copy of this
email is strictly prohibited. If you have received this email in error, please immediately notify us by return email or telephone if the sender's phone number is listed
above, then promptly and permanently delete this message.
While all reasonable care has been taken to avoid the transmission of viruses, it is the responsibility of the recipient to ensure that the onward transmission,
opening, or use of this message and any attachments will not adversely affect its systems or data. No responsibility is accepted by the company in this regard and
the recipient should carry out such virus and other checks as it considers appropriate.
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.
1
Dewhurst, Andrew D (OGC)
From:Frank Roach <frank.roach@hilcorp.com>
Sent:Thursday, December 7, 2023 15:20
To:Dewhurst, Andrew D (OGC)
Cc:Davies, Stephen F (OGC); Guhl, Meredith D (OGC); Roby, David S (OGC); Rixse, Melvin G (OGC); Joseph Lastufka
Subject:RE: [EXTERNAL] RE: PBU NK-24 (PTD 223-108) - Questions
Andy,
Thankyouforthephonediscussionearlierthisweek.Toansweryourbulletpointsbelow:
x We’vehadsomedownƟmeonPAVE1Ͳ1andhaverunintosomeequipmentavailabilityissueswithtools
plannedforNKͲ24.ThesehavecontributedtothespuddateonNKͲ24beingpushedlaterthanDecember13.
WewillwaitfortheupdatedpoolordertodrillNKͲ24.
x PleaseseethebelowscreenshotandtableshowingdistancesfromtheNKͲ24wellpathtotheclosestpointof
theDuckIslandUnitboundary.Theclosestourplancomesisat22,300’MD,wheretheunitboundaryis~652’
away.
You don't often get email from frank.roach@hilcorp.com. Learn why this is important
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.
2
LetmeknowifyouhaveanyaddiƟonalquesƟons.
Regards,
FrankVRoach
DrillingEngineer
Hilcorp Alaska, LLC
907.854.2321mobile
907.777.8413office
From:Dewhurst,AndrewD(OGC)<andrew.dewhurst@alaska.gov>
Sent:Tuesday,December5,202308:13
To:FrankRoach<frank.roach@hilcorp.com>;JosephLastufka<Joseph.Lastufka@hilcorp.com>
Cc:Davies,StephenF(OGC)<steve.davies@alaska.gov>;Guhl,MeredithD(OGC)<meredith.guhl@alaska.gov>;Roby,
DavidS(OGC)<dave.roby@alaska.gov>;Rixse,MelvinG(OGC)<melvin.rixse@alaska.gov>
Subject:[EXTERNAL]RE:PBUNKͲ24(PTD223Ͳ108)ͲQuestions
3
Frank,
Idon’tthinkIreceivedareplyonthisPTD.WouldyoupleasetakealookatthetwoquesƟonbelow?
Thanks,
Andy
From:Dewhurst,AndrewD(OGC)
Sent:Monday,November20,202315:41
To:FrankRoach<frank.roach@hilcorp.com>
Cc:Davies,StephenF(OGC)<steve.davies@alaska.gov>;Guhl,MeredithD(OGC)<meredith.guhl@alaska.gov>;Roby,
DavidS(OGC)<dave.roby@alaska.gov>;Rixse,MelvinG(OGC)<melvin.rixse@alaska.gov>
Subject:PBUNKͲ24(PTD223Ͳ108)ͲQuestions
Frank,
IamcompleƟngthereviewofthePBUNKͲ24andhavetwoquesƟons:
x TheNKͲ24istargeƟngreservoiroutsideofthecurrentRavenOilPoolboundary.Meanwhile,Hilcorphasapplied
fortheexpansionofthispool.
ItispossiblethattheexpansionmaynotbeissuedbeforetheanƟcipatedspuddateofDecember13th.Inthe
meanƟme,youcoulddrillthiswellunderstatewideregulaƟons(vs.poolrules).Fromthedrillingaspect,Idon’t
seeanychangethiswouldmake.Doyouwishto(1)drillassoonaspossibleandproceedwiththepermitunder
staterules,or(2)waitunƟltheoilpoolorderhasbeenupdated?
x WouldyoupleaseprovidetheclosestdistancefromthewellboretotheDuckIslandUnitboundary(SEcornerof
SecƟon21,T12N,R16E)?
Thanks,
Andy
AndrewDewhurst
SeniorPetroleumGeologist
AlaskaOilandGasConservaƟonCommission
333W.7thAve,Anchorage,AK99501
andrew.dewhurst@alaska.gov
Direct:(907)793Ͳ1254
The information contained in this email message is confidential and may be legally privileged and is intended only for the use of the individual or entity named
above. If you are not an intended recipient or if you have received this message in error, you are hereby notified that any dissemination, distribution, or copy of this
email is strictly prohibited. If you have received this email in error, please immediately notify us by return email or telephone if the sender's phone number is listed
above, then promptly and permanently delete this message.
While all reasonable care has been taken to avoid the transmission of viruses, it is the responsibility of the recipient to ensure that the onward transmission,
opening, or use of this message and any attachments will not adversely affect its systems or data. No responsibility is accepted by the company in this regard and
the recipient should carry out such virus and other checks as it considers appropriate.
CAUTION:Externalsender.DONOTopenlinksorattachmentsfromUNKNOWNsenders.
Revised 7/2022
TRANSMITTAL LETTER CHECKLIST
WELL NAME: ______________________________________
PTD: _____________________________________________
___ Development ___ Service ___ Exploratory ___ Stratigraphic Test ___ Non-Conventional
FIELD: __________________________ POOL: ____________________________________
Check Box for Appropriate Letter / Paragraphs to be Included in Transmittal Letter
CHECK OPTIONS TEXT FOR APPROVAL LETTER
MULTI
LATERAL
(If last two digits
in API number are
between 60-69)
The permit is for a new wellbore segment of existing well Permit
Number _____________, API Number 50-______________________.
Production from or injection into this wellbore must be reported under
the original API Number stated above.
Spacing
Exception
The permit is approved subject to full compliance with 20 AAC 25.055.
Approval to produce or inject is contingent upon issuance of a
conservation order approving a spacing exception. The Operator
assumes the liability of any protest to the spacing exception that may
occur.
Dry Ditch Sample
All dry ditch sample sets submitted to the AOGCC must be in no greater
than 30-foot sample intervals from below the permafrost or from where
samples are first caught and 10-foot sample intervals through target
zones.
Non-
Conventional
Well
Please note the following special condition of this permit: Production or
production testing of coal bed methane is not allowed for this well until
after the Operator has designed and implemented a water-well testing
program to provide baseline data on water quality and quantity. The
Operator must contact the AOGCC to obtain advance approval of such
a water-well testing program.
Well Logging
Requirements
Regulation 20 AAC 25.071(a) authorizes the AOGCC to specify types
of well logs to be run. In addition to the well logging program proposed
by the Operator in the attached application, the following well logs are
also required for this well:
Per Statute AS 31.05.030(d)(2)(B) and Regulation 20 AAC 25.071,
composite curves for all well logs run must be submitted to the AOGCC
within 90 days after completion, suspension, or abandonment of this
well, or within 90 days of acquisition of the data, whichever occurs first.
PBU NK-24
223-108
SAG RIVER UNDEFINED OIL POOL
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c
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e
d
p
a
r
t
y
Ye
s
10
O
p
e
r
a
t
o
r
h
a
s
a
p
p
r
o
p
r
i
a
t
e
b
o
n
d
i
n
f
o
r
c
e
Ye
s
11
P
e
r
m
i
t
c
a
n
b
e
i
s
s
u
e
d
w
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t
h
o
u
t
c
o
n
s
e
r
v
a
t
i
o
n
o
r
d
e
r
Ye
s
12
P
e
r
m
i
t
c
a
n
b
e
i
s
s
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e
d
w
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t
h
o
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t
a
d
m
i
n
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s
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r
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t
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v
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a
p
p
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a
l
Ye
s
13
C
a
n
p
e
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m
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t
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e
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p
p
r
o
v
e
d
b
e
f
o
r
e
1
5
-
d
a
y
w
a
i
t
NA
14
W
e
l
l
l
o
c
a
t
e
d
w
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t
h
i
n
a
r
e
a
a
n
d
s
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a
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t
h
o
r
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d
b
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n
j
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c
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r
#
(
p
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t
I
O
#
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n
c
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m
m
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s
)
(
F
o
r
NA
15
A
l
l
w
e
l
l
s
w
i
t
h
i
n
1
/
4
m
i
l
e
a
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v
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w
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d
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t
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d
(
F
o
r
s
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r
v
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c
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w
e
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l
o
n
l
y
)
NA
16
P
r
e
-
p
r
o
d
u
c
e
d
i
n
j
e
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t
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r
:
d
u
r
a
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f
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d
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s
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F
o
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s
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)
NA
17
N
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18
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19
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20
C
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T
v
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9
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5
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8
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t
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d
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21
C
M
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v
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7
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p
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.
22
C
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w
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k
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Ye
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23
C
a
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p
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t
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2
7
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.
24
A
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k
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g
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r
r
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p
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t
NA
T
h
i
s
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s
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.
25
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f
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h
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1
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.
26
A
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v
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6
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27
I
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d
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v
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,
d
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.
28
D
r
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l
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p
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p
s
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29
B
O
P
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d
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30
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p
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5
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31
C
h
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p
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/
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P
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5
3
(
M
a
y
8
4
)
Ye
s
32
W
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k
w
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w
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d
.
33
I
s
p
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s
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n
c
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f
H
2
S
g
a
s
p
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b
a
b
l
e
NA
T
h
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s
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s
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d
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v
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l
o
p
m
e
n
t
w
e
l
l
.
34
M
e
c
h
a
n
i
c
a
l
c
o
n
d
i
t
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n
o
f
w
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w
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h
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n
A
O
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v
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f
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d
(
F
o
r
s
e
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v
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c
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w
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l
l
o
n
l
y
)
No
H
2
S
m
e
a
s
u
r
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s
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.
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K
-
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s
1
,
5
8
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p
p
m
(
2
0
2
2
)
35
P
e
r
m
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t
c
a
n
b
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s
s
u
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d
w
/
o
h
y
d
r
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l
f
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p
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t
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,
H
R
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g
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k
36
D
a
t
a
p
r
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n
t
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d
o
n
p
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t
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n
t
i
a
l
o
v
e
r
p
r
e
s
s
u
r
e
z
o
n
e
s
NA
37
S
e
i
s
m
i
c
a
n
a
l
y
s
i
s
o
f
s
h
a
l
l
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w
g
a
s
z
o
n
e
s
NA
38
S
e
a
b
e
d
c
o
n
d
i
t
i
o
n
s
u
r
v
e
y
(
i
f
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f
f
-
s
h
o
r
e
)
NA
39
C
o
n
t
a
c
t
n
a
m
e
/
p
h
o
n
e
f
o
r
w
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k
l
y
p
r
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g
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s
s
r
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p
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s
[
e
x
p
l
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r
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r
y
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n
l
y
]
Ap
p
r
D
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t
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Ap
p
r
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R
Da
t
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11
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2
8
/
2
0
2
3
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p
r
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D
Da
t
e
11
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1
7
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2
0
2
3
Ad
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t
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g
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m
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2
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