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Alaska Oil and Gas Conservation Commission
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HomeMy WebLinkAboutCO 317 BIndex Conservation Order 317B
Pt McIntyre and Pt McIntyre and Stump Island Oil Pool
1. November 8, 1999 Arco Alaska's Pt McIntyre Application to Amend AI04B
2. November 20, 1999 Notice of Hearing and Affidavit of Publication
3. December 1, 1999 Ltr from AOGCC to Arco re: application
4.
January 1, 2000
Meeting sign in sheet with Arco
5.
January 12, 2000
Transcript of hearing, testimony, sign in sheet
6.
March 9, 2000
Ltr from Arco answering questions from hearing
7.
September 9, 2003
BP request to Commingle Production from Pt. McIntyre
Participating Area with IPA Production
8.
October 16, 2003
DOR response to BP's request
9.
October 27, 2003
DNR response to BP's request
10.
November 11, 2003
Revised BP request to Commingle Production from Pt.
McIntyre Participating Area with IPA Production
11.
January 27, 2004
DNR revised response to BP's request
12.
May 23, 2007
Annual Surveillance Reporting Requirements (C031713-
002)
13.
February 20, 2020
BPXA's request for Amin Approval for Conforming PBU
Greater Pt. McIntyre Area Satellite Pool Rules for
Consistency (CO 31713.003)
14.
February 24, 2020
BPXA Request to amend CO 492 rule 3(a) and 6(a)
(co317B.001)
15.
May 21, 2020
Notice of Hearing and mailing
16.
-----------------
Emails
Index Conservation Order 317B
Pt McIntyre and Pt McIntyre and Stump Island Oil Pool
1. November 8, 1999
2. November 20, 1999
3. December 1, 1999
4. January 1, 2000
5. January 12, 2000
6. March 9, 2000
7. September 9, 2003
8. October 16, 2003
9. October 27, 2003
10. November 11, 2003
11. January 27, 2004
12. May 23, 2007
Arco Alaska's Pt McIntyre Application to Amend A104B
Notice of Hearing and Affidavit of Publication
Ltr from AOGCC to Arco re: application
Meeting sign in sheet with Arco
Transcript of hearing, testimony, sign in sheet
Ltr from Arco answering questions from hearing
BP request to Commingle Production from Pt. McIntyre
Participating Area with IPA Production
DOR response to BP's request
DNR response to BP's request
Revised BP request to Commingle Production from Pt.
McIntyre Participating Area with IPA Production
DNR revised response to BP's request
Annual Surveillance Reporting Requirements (C031713-
002)
Conservation Order 317B
go
STATE OF ALASKA
400
OIL AND GAS CONSERVATION COMMISSION
3001 Porcupine Drive
Anchorage, Alaska 99501-3192
Re: The application of ARCO Alaska, Inc. ) Conservation Order No. 317B
("AAI") to amend AID 4 to initiate a Miscible )
Gas Enhanced Oil Recovery Project in the ) Pt. McIntyre Oil Field
Prudhoe Bay Unit, Point McIntyre Oil Pool, ) Pt. McIntyre Oil Pool (amended)
North Slope, Alaska. ) Stump Island Oil Pool
April 19, 2000
IT APPEARING THAT:
By correspondence dated November 8, 1999, AAI requested authorization from the Alaska Oil and Gas
Conservation Commission ("Commission") to initiate a miscible gas tertiary recovery project in the
Point McIntyre Oil Pool located in the Eastern Operating Area of the Prudhoe Bay Unit.
The Commission published notice of opportunity for public hearing in the Anchorage Daily News on
November 20, 1999.
The Commission did not receive a protest or request for a public hearing.
The Commission held a hearing at the Commission's offices on January 12 and 13, 2000.
FINDINGS:
The Commission has issued Conservation Order No. 317 dated July 2, 1993 (revised September 10,
1993) and Conservation Order No. 317A dated April 25, 1996 to govern development of the Pt. McIntyre
Oil Pool.
2. The findings, conclusions and administrative records for the above listed Conservation Orders are
incorporated by reference in this order.
3. AAI is the operator of the Eastern Operating Area of the Prudhoe Bay Unit including the Point McIntyre
Oil Field and the West Beach Oil Pool. There are no other operators within a one-quarter mile radius of
the proposed injection operations.
4. The State of Alaska is the only surface owner within one mile of the Point McIntyre Oil.
Facility modifications at the Lisburne Production Center (LPC) are designed to ensure that the volume of
natural gas liquids extracted at the LPC will not be impacted by the manufacture of miscible injectant
solvent.
6. AAI proposes to use hydrocarbons from the Pt. McIntyre, West Beach, North Prudhoe Bay, Niakuk and
Lisburne Oil Pools processed in the LPC. Components from the natural gas liquid plant downstream from
the feed flash drum will be added to enrich the miscible injectant (MI) stream to be used in the Point
McIntyre enhanced recovery project.
0
Conservation Order No. 30 010
April 19, 2000
page 2
7. Seventy-four producing and service wells were active in the Point McIntyre Oil Pool (PMOP) as of
January 1, 2000. Fifteen water injectors and one gas injector were providing pressure support to the
PMOP, maintaining average reservoir pressure near the original pressure of approximately 4370 psi.
8. The inverted nine -spot waterflood pattern in the PMOP is flexible and can be adapted to changes in
reservoir performance as the enhanced recovery process matures.
The PMOP miscible gas injection project involves conversion of present and future waterflood injectors
to water -alternating -gas (WAG) injection service.
10. A MI slug equivalent to approximately 35 percent hydrocarbon pore volume (HPV) will be placed over a
twenty-three year period.
11. The maximum MI rate that can be manufactured from LPC residue gas is projected to be 50 MMSCFD at
a minimum miscibility pressure of approximately 4350 -psi.
12. An extensive performance history indicates that the Pt. McIntyre waterflood has been able to adequately
balance voidage in the reservoir to maintain an average reservoir pressure of 4370 psi.
13. The minimum miscibility pressure is designed to be as close to average reservoir pressure as possible.
This will maximize the volume of MI that can be manufactured at LPC.
14. Limited supply of MI will require phased implementation and conversion of patterns to WAG injection.
Any volumes of MI in excess of the nominal 50 MMSCFD rate injected in the PMOP will have to be
purchased from an external source.
15. The benefits of using additional MI, up to 100 MMSCFD purchased from an external source for this
project, are being evaluated.
16. Modifications at LPC done in 1999 to manufacture MI included installation of an MI compressor, a new
parallel chiller, new compressor coolers, blending station, and an upgrade of the natural gas liquid plant
piping.
17. MI will be transported to the Point McIntyre drill sites by a new pipeline using existing vertical support
members and new drill site distribution piping.
18. The geologic description of the injection and confining zones for both the PMOP miscible gas tertiary
recovery project and the West Beach Oil Pool (WBOP) enhanced oil recovery project have been
previously submitted in "Application for Modification to Area Injection Order No. 4" dated April 5,
1993.
19. Injection wells in the PMOP have been drilled, cased, cemented according to requirements of 20 AAC
25.005 and tested according to 20 AAC 25.412. Applications and completion records are on file at the
AOGCC.
20. Seawater is currently injected in the Pt. McIntyre waterflood. It is possible that produced water will be
used later in the project. Both water sources have previously been approved in Area Injection Order No.
4B.
21. Estimated average and maximum injection pressures (at pump discharge) for PMOP WAG wells are
expected to be 4100 psi and 4500 psi respectively.
22. Surveillance and performance data for both water and gas injection in the PMOP indicates out of zone
fractures have not occurred.
23. MI injection pressures are not likely to cause fracturing of the PMOP confining zones based on previous
enhanced recovery injection performance.
24. Secondary recovery gas re-injection and pattern waterflood operations in the PMOP are projected to
increase recovery to 42-45% of the original oil in place (OOIP).
Conservation Order No. 3 �.
April 19, 2000
page 3
25. The PMOP MI enhanced recovery project will increase oil recovery from the pool by 6% of the OOIP or
by 32 MMSTB in the area where MI will be applied.
CONCLUSIONS:
Conservation Order No. 317A should be amended to allow implementation of an enhanced recovery
project within the area defined as the Pt. McIntyre Pool.
NGL required for the project will be manufactured from gas processed in the LPC.
Implementation of a miscible gas injection project in the PMOP will significantly increase ultimate
recovery, will not cause waste nor violate correlative rights.
Surveillance activity associated with reservoir development, waterflood, and miscible injection
operations reporting should be consolidated into one report documenting significant activity on an annual
basis.
The record for this order should include the hearing record and administrative files related to
Conservation Order No. 317 and Conservation Order No. 317A, including approvals issued under those
orders.
6. The PMOP miscible gas injection project and the WBOP injection project will not cause waste,
jeopardize correlative rights, or impair ultimate recovery.
NOW, THEREFORE, IT IS ORDERED THAT (1) Conservation Order No. 317B supersedes
Conservation Order No. 317A dated April 25, 1996 and Conservation Order No. 317 dated July2, 1993. (2)
The following rules, in addition to statewide requirements under 20 AAC 25, apply to the affected area
described below:
Umiat Meridian
T12N
R15E
Section 18
All.
Section 19
NI/2.
T12N
R14E
Section 13
All.
Section 14
All.
Section 23
N1/2 NW1/4, N1/2 NEI/4, SWIA NW1/4.
Section 24
NI/2.
T12N
R14E
Section 15
All
Section 16
All
Section 21
N1/2 NE 1/4.
Section 22
N1/2.
T12N
R14E
Section 17
NEIA, N1/2, SE 1/4, E1/2 E1/2 NWI/4,
EI/2 NEI/4 SWI/4.
T12N
R14E
Section 3
All.
Section 4
All.
Section 9
All.
Section 10
All.
•
Conservation Order No. 3 0
April 19, 2000
page 4
400
Those Lands in Block 605 lying northerly of the north boundary of Section 3, T12N, R14E, UM,
AK. (Identical with line 4-5 on Block 605) and lying easterly of the west boundary of Sections 2
and 11, T12N, R14E, UM, AK (Identical with line 5-6 on Block 605) and lying northerly of the
south boundary of Section 11 and 12, T12N, R14E, UM, AK, and lying northerly of the south
boundary of Section 7, T12N, RI 5E, UM, AK (Identical with line 6-7 on Block 605), within the
offshore three-mile arc lines listed as State Area on the "Supplemental Official O.C.S. Block
Diagram," approved 12/9/79, containing 1457.32 hectares.
Rule 1 Plan of Development and Operation
Regular production may not begin until the interests of the working interest and royalty owners
are integrated in accordance with the provisions of 20 AAC 25.517, and the plan of development
and operation has been approved by the Commission under the provisions of AS 31.05.030(d)(9).
Rule 2 Field and Pool Names
The field is the Pt. McIntyre oil field. Hydrocarbons contained within the Kuparuk River and
Kalubik Formations constitute a single associated gas and oil reservoir called the Pt. McIntyre
Oil Pool. Hydrocarbons contained within the Seabee formation constitute a single associated gas
and oil reservoir called the Stump Island Oil Pool.
Rule 3 Pool Definition
The Pt. McIntyre oil pool is defined as the accumulation of hydrocarbons common to and which
correlates with the interval from 9908 to 10665 foot measured depth in the ARCO Pt. McIntyre
No. 11 well.
The Stump Island oil pool is defined as the accumulation of hydrocarbons common to and which
correlates with the interval from 8759 to 8930 foot measured depth in the ARCO Pt. McIntyre
No. 3 well.
Rule 4 Well Spacing
The spacing unit shall be one producing well per 40 acres or quarter -quarter governmental
section. No pay shall be opened in a well closer than 500 feet to the boundary of the affected
area.
Rule 5 Casing and Cementing
a. A conductor casing shall be set at least 75 feet below the surface and sufficient cement shall be used
to fill the annulus behind the pipe. Cement to surface shall be verified by visual inspection. The
Commission may administratively waive or approve other conductor setting depths and sealing
methods that are supported by sound engineering principles.
b. Surface casing shall be set at least 500 feet MD below the base of the permafrost but not below 5000
feet TVDss. Sufficient cement shall be used to fill the annulus behind the casing to the surface; if
Conservation Order No. 3
April 19, 2000
page 5
complete fill -up is not obtained, a top job will be performed before proceeding with drilling
operations.
c. Structural casing is not required.
Rule 6 Completion Practices
Wells completed for production may utilize casing strings or liners cemented through the
productive intervals and perforated, slotted liners, screen -wrapped liners, gravel packs or open
hole methods, or combinations thereof.
Rule 7 Drilling and Production Equipment
Drilling and production equipment must meet the requirements of API RP 7G, Section 8,
"Drillstem Corrosion and Sulfide Stress Cracking," current edition.
Rule 8 Automatic Shut In Equipment
a. Upon completion, each well which is capable of unassisted flow of hydrocarbons to the surface shall
be equipped with:
i. a fail-safe automatic surface safety valve (SSV) capable of preventing uncontrolled
flow.
ii. a fail-safe automatic subsurface safety valve (SSSV), unless other types of
subsurface valve are approved by the Commission, shall be installed in the tubing
string below the base of the permafrost and be capable of preventing uncontrolled
flow.
b. A well that is not capable of unassisted flow of hydrocarbons, as determined by a "no flow"
performance test witnessed by a Commission representative, is not required to have fail-safe
automatic SSSV's.
c. SSSV's may be temporarily removed as part of routine well operations without specific notice to, or
authorization by the Commission.
Rule 9 Wellbore Commingling
a. Production from the Pt. McIntyre and Stump Island oil pools may be commingled in the wellbore of
the Pt. McIntyre No. 3 well.
i. Allocation to each pool may be determined by production profile surveys or separate
zone well tests.
ii. The Commission may require additional production surveillance methods and may
administratively accept alternative methods of allocation of wellbore commingled
production upon application by the operator.
b. Additional wells may be approved administratively for wellbore commingling on a case-by-case
basis upon application to the Commission.
Conservation Order No. SO
April 19, 2000
page 6
Rule 10 Surface Commingling and Common Facilities
a. Production from the Pt. McIntyre and Stump Island oil pools may be commingled on the surface with
production from other pools for processing at the LPC prior to custody transfer.
b. Production from each well will be determined by the following well test allocation methodology.
Allocation data and well test data will be supplied to the Commission monthly in both computer file
and report formats.
i. Conduct well tests to determine production rates for each well.
ii. Calculate each well's theoretical monthly production (TMP) based on well test
rate(s) and actual time on production.
iii. Sum the TMP volume for all wells in all pools.
iv. Determine an allocation factor as the ratio of the metered volume to the TMP for all
wells in all pools (i.e., metered/TMP)
v. Calculate each well's actual monthly production (AMP) volume as:
AMP = TMP x Allocation Factor
c. NGLs will be allocated to each pool based on actual gas production volumes and NGL process
simulations. Process simulations will be updated at least once per year based on NGL samples and
results reported to the Commission.
d. Each producing well will be tested at least twice each month. Wells that have been shut in and
cannot meet the twice monthly test frequency must be tested within five days of startup. All
available test separator capacity within the constraints imposed by operating conditions must be
utilized for well testing.
e. Optimum test duration and stabilization time will be determined on a well by well basis by the
operator.
f. Water volumes will be determined by API/MPMS approved methods, or the use of industry proven,
on-line water cut measurement devices approved by the Commission.
g. API gravity will be determined for each producing well annually by an API/MPMS approved
method.
h. Gas samples will be taken and analyzed for composition from each non -gas lifted producing well
yearly.
i. Quarterly allocation process reviews will be held with the Commission.
j. This rule may be revised or rewritten after an evaluation period of at least one year.
Rule 11 Production Anomalies
In the event of oil production capacity proration at or from the LPC, all commingled pools
produced at the LPC will be prorated by an equivalent percentage of oil production recognizing
mechanical limitations and operational constraints.
Conservation Order No. 31
April 19, 2000
page 7
Rule 12 Reservoir Pressure Monitoring
a. Prior to regular production, a pressure survey shall be taken on each well to determine the reservoir
pressure.
b. A minimum of one bottom hole pressure survey per producing governmental section shall be run
annually. The surveys in part a. of this rule may be used to fulfill the minimum requirements.
c. The datum for all surveys is 8800' TVDss.
d. Pressure surveys will be either a pressure buildup, pressure falloff, RFT, or static bottom hole
pressure after the well has been shut in for an extended period.
The pressure surveys will be reported to the Commission quarterly. Commission form 10-412,
Reservoir Pressure Report, shall be used to report results from these surveys. All data necessary for
complete analysis of each survey need not be submitted with the form 10-412 but must be submitted
upon request.
f. Results and data from any special reservoir pressure monitoring techniques, tests, or surveys also
shall be submitted in accordance with part e. of this rule.
Rule 13 Gas -Oil -Ratio Exemption
Wells producing from the Pt. McIntyre and Stump Island oil pools are exempt from the gas -oil
ratio limit set forth in 20 AAC 25.240(b) so long as the provisions of 20 AAC 25.240(c) apply.
Rule 14 Administrative Action
Upon proper application, the Commission may administratively waive the requirements of any
rule stated above or administratively amend this order as long as the change does not promote
waste, jeopardize correlative rights, and is based on sound engineering principles.
Rule 15 Pt. McIntyre Oil Pool Annual Reservoir Report
An annual Pt. McIntyre Oil Pool surveillance report will be required by April 1 of each year. The report
shall include but is not limited to the following:
a. Progress of enhanced recovery project(s) implementation and reservoir management summary
including engineering and geotechnical parameters.
b. Reservoir voidage balance by month of produced fluids and injected fluids.
c. Analysis of reservoir pressure surveys within the pool.
d. Results and where appropriate, analysis of production and injection log surveys, tracer surveys and
observation well data and surveys.
e. Results of any special monitoring.
f. Future development plans.
g. Review of Annual Plan of Operations and Development.
Conservation Order No. 30
April 19, 2000
page 8
Rule 16 Pt. McIntyre Oil Pool Enhanced Oil Recovery Project
a. Injection of miscible injectant for enhanced recovery operations is approved for the Pt. McIntyre
Pool.
b. An annual report must be submitted to the Commission detailing performance of the PMOP
Enhanced Oil Recovery Project and outlining compositional information for the current miscible
injectant necessary to maintain miscibility under anticipated reservoir conditions. The report should
be submitted in conjunction with the PMOP Annual Reservoir Report.
DONE at Anchorage, Alaska and dated April 19, 2000.
4obert N. tenson, P.E., Chair
Alaska Oil and Gas Conservation Commission
Camille Oechsli Taylor, Commissi6ner
Alaska Oil and Gas Conservation Commission
AS 31.05.080 provides that within 20 days after receipt of written notice of the entry of an order, a person affected by it may file
with the Commission an application for rehearing. A request for rehearing must be received by 4:30 PM on the 23rd day
following the date of the order, or next working day if a holiday or weekend, to be timely filed. The Commission shall grant or
refuse the application in whole or in part within 10 days. The Commission can refuse an application by not acting on it within the
10 -day period. An affected person has 30 days from the date the Commission refuses the application or mails (or otherwise
distributes) an order upon rehearing, both being the final order of the Commission, to appeal the decision to Superior Court.
Where a request for rehearing is denied by nonaction of the Commission, the 30 -day period for appeal to Superior Court runs from
the date on which the request is deemed denied (Le. 10th day after the application for rehearing was filed).
•
STATE OF ALASKA
ALASKA OIL AND GAS CONSERVATION COMMISSION
333 West 7th Avenue, Suite 100
Anchorage, Alaska 99501
Re: AN ORDER rescinding those rules within
existing Conservation Orders relating to
well safety valve systems.
Docket Number: CO -10-21
Other Order No. 66
Statewide, Alaska
January 11, 2011
IT APPEARING THAT:
1. On October 13, 2010 the Alaska Oil and Gas Conservation Commission (AOGCC
or Commission) formally adopted new regulations relating to well safety valve
systems, at 20 AAC 25.265.
2. The newly adopted well safety valve system regulations underwent final review
by the Regulations Section of the Alaska Attorney General's Office and were
forwarded to the Alaska Lieutenant Governor's Office on October 28, 2010.
3. The new regulations were signed by the Lieutenant Governor and took legal effect
on December 3, 2010.
4. To ensure consistency with the new regulations, the AOGCC, on its own motion,
proposed to rescind part or all of the outdated rules within existing Commission
Orders relating to well safety valve systems.
5. On November 4, 2010, pursuant to 20 AAC 25.540, the Commission published in
the Alaska Daily News notice of opportunity for public hearing on December 6,
2010.
6. The Commission received written comments in response to its public notice, and
held a public hearing on December 7, 2010.
7. Oral testimony and written comments were provided at the December 7, 2010
hearing.
FINDINGS:
Well safety valve systems are regulated under newly -adopted 20 AAC 25.265,
which consolidates the requirements previously established in legacy documents,
policies, and statewide guidelines relating to safety valve systems.
2. Thirty-four existing Commission Orders contain rules governing well safety valve
systems. Twenty of those Orders contain broad regulatory requirements for safety
valve systems that are now covered by the newly -adopted regulations. The
remaining fourteen Orders include field- or pool -specific safety valve system
requirements.
Other Order 66 • • Page 2
Statewide, AK
January 11, 2011
3. Within existing Commission Orders are rules unrelated to well safety valve
systems; these rules will continue in effect, unmodified.
4. Existing Commission Orders containing individual rules relating to well safety
valve systems are enumerated in the attached Table.
CONCLUSIONS:
1. Eliminating redundant requirements and standardizing wording for those field -
and pool -specific safety valve system requirements deemed appropriate to retain
will improve regulatory clarity.
2. Twenty existing Commission Orders that include rules relating to well safety
valve systems are rendered unnecessary, and can be replaced by newly -adopted
20 AAC 25.265. As more fully set forth in the attached Table, those Orders are
Conservation Orders 98A, 207A, 300, 311B, 317B, 329A, 341E, 345, 402B,
432D, 452, 457B, 471, 477, 484A, 505B, 553, 559, 570, and a Commission
unnumbered Order signed March 30, 1994 (policy dictating SVS performance
testing requirements).
3. Fourteen existing Commission Orders include field- or pool -specific safety valve
system requirements that the Commission considers appropriate for retention.
Wording for the same safety valve system requirements existing in different
Commission Orders has been standardized. As more fully set forth in the attached
Table, those Orders are Conservation Orders 406B, 423, 430A, 435A, 443B, 449,
456A, 458A, 562, 563, 569, 596, 597, and 605.
NOW, THEREFORE, IT IS ORDERED THAT individual rules in thirty-four existing
Commission Orders that relate to well safety valve systems are hereby rescinded or
revised as enumerated in the Table. Remaining rules unrelated to safety valve systems
within affected Commission Orders remain in effect, unmodified.
DONE at Anchorage, Alaska, and dated diary 11, 201
Daniel T. Se ou' , r., Commissioner, Chair
it s Conservation Commission
'III fl, Co ne
or
a OirmanCa as,Conservation Commission
CatHy P. Ybersterr, Commissioner
Alaska it and Gas Conservation Commission
Other Order 66 •
Statewide, AK
January 11, 2011
RECONSIDERATION AND APPEAL NOTICE
0 Page 3
As provided in AS 31.05.080(a), within 20 days after written notice of the entry of this order or decision, or such further time as the
Commission grants for good cause shown, a person affected by it may file with the Commission an application for reconsideration of
the matter determined by it. If the notice was mailed, then the period of time shall be 23 days. An application for reconsideration
must set out the respect in which the order or decision is believed to be erroneous.
The Commission shall grant or refuse the application for reconsideration in whole or in part within 10 days after it is filed. Failure to
act on it within 10 -days is a denial of reconsideration. If the Commission denies reconsideration, upon denial, this order or decision
and the denial of reconsideration are FINAL and may be appealed to superior court. The appeal MUST be filed within 33 days after
the date on which the Commission mails, OR 30 days if the Commission otherwise distributes, the order or decision denying
reconsideration, UNLESS the denial is by inaction, in which case the appeal MUST be filed within 40 days after the date on which
the application for reconsideration was filed.
If the Commission grants an application for reconsideration, this order or decision does not become final. Rather, the order or
decision on reconsideration will be the FINAL order or decision of the Commission, and it may be appealed to superior court. That
appeal MUST be filed within 33 days after the date on which the Commission mails, OR 30 days if the Commission otherwise
distributes, the order or decision on reconsideration. As provided in AS 31.05.080(b), "[tlhe questions reviewed on appeal are limited
to the questions presented to the Commission by the application for reconsideration."
In computing a period of time above, the date of the event or default after which the designated period begins to run is not included in
the period; the last day of the period is included, unless it falls on a weekend or state holiday, in which event the period runs until 5:00
p.m. on the next day that does not fall on a weekend or state holiday.
0 0
Fisher, Samantha J (DOA)
From:
Fisher, Samantha J (DOA)
Sent:
Tuesday, January 11, 20114:08 PM
To:
Ballantine, Tab A (LAW); '(foms2@mtaonline. net)';'(michael.j.nelson @conocophillips. com)';
'(Von. L. Hutchins@conocophillips.com)'; 'AKDCWelllntegrityCoordinator'; 'Alan Dennis';
'alaska@petrocalc.com'; 'Anna Raff; 'Barbara F Fullmer'; 'bbritch'; 'Becky Bohrer'; 'Bill
Penrose'; 'Bill Walker'; 'Bowen Roberts'; 'Brad McKim'; 'Brady, Jerry L'; 'Brandon Gagnon';
'Brandow, Cande (ASRC Energy Services)'; 'Brian Havelock'; 'Bruce Webb'; 'carol smyth';
'caunderwood'; 'Chris Gay'; 'Cliff Posey'; 'Crandall, Krissell'; 'D Lawrence'; 'dapa'; 'Daryl J.
Kleppin'; 'Dave Matthews'; 'David Boelens'; 'David House'; 'David Steingreaber';
'ddonkel@cfl.rr.com'; 'Deborah J. Jones'; Delbridge, Rena E (LAA); 'Dennis Steffy'; 'Elowe,
Kristin'; 'Erika Denman'; 'eyancy'; 'Francis S. Sommer'; 'Fred Steece'; 'Gary Laughlin'; 'Gary
Rogers'; 'Gary Schultz'; 'ghammons'; 'Gordon Pospisil'; 'Gorney, David L.'; 'Greg Duggin';
'Gregg Nady'; 'gspfoff; 'Harry Engel'; 'Jdarlington aarlington@gmail.com)'; 'Jeanne
McPherren'; 'Jeff Jones'; 'Jerry McCutcheon'; 'Jill Womack'; 'Jim White'; 'Jim Winegarner';
'Joe Nicks'; 'John Garing'; 'John Katz'; 'John S. Haworth'; 'John Spain'; 'John Tower'; 'Jon
Goltz'; 'Judy Stanek'; 'Julie Houle'; 'Kari Moriarty'; 'Kaynell Zeman'; 'Keith Wiles'; 'Kelly
Sperback'; 'Kim Cunningham'; 'Larry Ostrovsky'; 'Laura Silliphant'; 'Marilyn Crockett'; 'Mark
Dalton'; 'Mark Hanley (mark.hanley@anadarko.com)'; 'Mark Kovac'; 'Mark P. Worcester';
'Marguerite kremer'; 'Michael Dammeyer'; 'Michael Jacobs'; 'Mike Bill'; 'Mike Mason'; 'Mikel
Schultz'; 'Mindy Lewis'; 'MJ Loveland'; 'mjnelson'; 'mkm7200'; 'nelson'; 'Nick W. Glover'; 'NSK
Problem Well Supv'; 'Patty Alfaro'; 'Paul Decker (paul.decker@alaska.gov)'; 'Paul Figel';
'PORHOLA, STAN T'; 'Randall Kanady'; 'Randy L. Skillern'; 'rob.g.dragnich@exxonmobil.com';
'Robert Brelsford'; 'Robert Campbell'; 'Ryan Tunseth'; 'Scott Cranswick'; 'Scott Griffith'; Scott,
David (LAA); 'Shannon Donnelly'; 'Sharmaine Copeland'; Shellenbaum, Diane P (DNR);
Slemons, Jonne D (DNR); 'Sondra Stewman'; 'Steve Lambert'; 'Steve Moothart'; 'Steven R.
Rossberg'; 'Suzanne Gibson'; 'tablerk'; 'Tamera Sheffield'; Taylor, Cammy O (DNR); 'Temple
Davidson'; 'Teresa Imm'; 'Terrie Hubble'; 'Thor Cutler'; 'Tina Grovier'; 'Todd Durkee'; 'Tony
Hopfinger'; 'trmjr1'; 'Valenzuela, Mariam'; 'Vicki Irwin'; 'Walter Featherly'; 'Will Chinn';
Williamson, Mary J (DNR); 'Yereth Rosen'; 'Aaron Gluzman'; Bettis, Patricia K (DNR);
caunderwood@marathonoil.com; 'Dale Hoffman'; 'David Lenig'; 'Gary Orr'; 'Jason Bergerson';
'Joe Longo'; 'Lara Coates'; 'Marc Kuck'; 'Mary Aschoff; 'Matt Gill'; 'Maurizio Grandi';
Ostrovsky, Larry Z (DNR); 'Richard Garrard'; 'Sandra Lemke'; 'Talib Syed'; 'Tiffany Stebbins';
'Wayne Wooster'; 'William Van Dyke'; Woolf, Wendy C (DNR); Aubert, Winton G (DOA)
(winton.aubert@alaska.gov); Brooks, Phoebe L (DOA) (phoebe.brooks@alaska.gov);
Colombie, Jody J (DOA) (jody.colombie@alaska.gov); Crisp, John H (DOA)
gohn.crisp@alaska.gov); Davies, Stephen F (DOA) (steve.davies@alaska.gov); Foerster,
Catherine P (DOA) (cathy.foerster@alaska.gov); Grimaldi, Louis R (DOA)
(lou.grimaldi@alaska.gov); Johnson, Elaine M (DOA) (elaine.johnson@alaska.gov); Jones,
Jeffery B (DOA) (jeff.jones@alaska.gov); Laasch, Linda K (DOA) (linda.laasch@aiaska.gov);
Maunder, Thomas E (DOA) (tom.maunder@alaska.gov); McIver, Bren (DOA)
(bren.mciver@alaska.gov); McMains, Stephen E (DOA) (steve.mcmains@alaska.gov);
Mumm, Joseph (DOA sponsored); Noble, Robert C (DOA) (bob.noble@alaska.gov); Norman,
John K (DOA) Oohn.norman@alaska.gov); Okland, Howard D (DOA)
(howard.okland@alaska.gov); Paladijczuk, Tracie L (DOA) (tracie.paladijczuk@alaska.gov);
Pasqual, Maria (DOA) (maria.pasqual@alaska.gov); Regg, James B (DOA)
aim.regg@alaska.gov); Roby, David S (DOA) (dave.roby@alaska.gov); Saltmarsh, Arthur C
(DOA) (art.saltmarsh@alaska.gov); Scheve, Charles M (DOA) (chuck.scheve@alaska.gov);
Schwartz, Guy L (DOA) (guy.schwartz@alaska.gov); Seamount, Dan T (DOA)
(dan.seamount@alaska.gov); Shartzer, Christine R (DOA)
Subject:
Other 66 Safety Valve Systems
Attachments:
other66. pdf
Scx taux� F4 --4-
A i a ka, OL, a4 -L. C7a k Caww-4rvarU) ►v Cots ►ztimiow
(907)793-1223
(907)276-7542 (frw)
0 0
Mary Jones David McCaleb
XTO Energy, Inc. IHS Energy Group
Cartography GEPS
810 Houston Street, Ste 200 5333 Westheimer, Suite 100
Ft. Worth, TX 76102-6298 Houston, TX 77056
Jerry Hodgden
Richard Neahring
Hodgden Oil Company
NRG Associates
President
40818 th Street
P.O. Box 1655
Golden, CO 80401-2433
Colorado Springs, CO 80901
Bernie Karl CIRI
K&K Recycling Inc. Land Department
P.O. Box 58055 P.O. Box 93330
Fairbanks, AK 99711 Anchorage, AK 99503
North Slope Borough Jill Schneider
P.O. Box 69 US Geological Survey
Barrow, AK 99723 4200 University Drive
Anchorage, AK 99508
Jack Hakkila Darwin Waldsmith
P.O. Box 190083 P.O. Box 39309
Anchorage, AK 99519 Ninilchick, AK 99639
Kenai National Wildlife Refuge Penny Vadla
Refuge Manager 399 West Riverview Avenue
P.O. Box 2139 Soldotna, AK 99669-7714
Soldotna, AK 99669-2139
Richard Wagner
P.O. Box 60868
Fairbanks, AK 99706
George Vaught, Jr.
P.O. Box 13557
Denver, CO 80201-3557
Mark Wedman
Halliburton
6900 Arctic Blvd.
Anchorage, AK 99502
Baker Oil Tools
795 E. 94th Ct.
Anchorage, AK 99515-4295
Gordon Severson
3201 Westmar Circle
Anchorage, AK 99508-4336
James Gibbs
P.O. Box 1597
Soldotna, AK 99669
Cliff Burglin
319 Charles Street
Fairbanks, AK 99701
Orders Establishing Requirements for Well Safety Valve Systems
1/7/2011
Unit/Field
Pool
Conservation
Rule
Rescind Rule?
Existing Order Requirement
25.265(x); 25.265(b); 25.265(d)(2)(H);
"Injection wells (excluding disposal injectors) must be equipped with(i) a double check valve
Order 1
25.265(h)(5)
arrangement or (ii) a single check valve and a SSV. Asubsurface-controlled injection valve or
readopted regulation
SCSSV satisfies the requirements of a single check valve"
25.265(x); 25.2659(b); 25.265(d)(1);
"Injection wells (excluding disposal injectors) must be equipped with(i) a double check valve
fail-safe auto SSV and SCSSV; injection wells (except disposal) require
Colville River Unit
Qannik
605
5
no
(i) double check valve, or (ii) single check valve and SSV; injection
25.265(x); 25.265(b); 25.265(d)(1);
"Injection wells (excluding disposal injectors) must be equipped with(i) a double check valve
Check valve requirements for injectors are not covered by
25.265(h)(5)arrangement
or (ii) a single check valve and a SSV. A subsurface -controlled injection valve or
valve satisfies single check valve requirement; test every 6 months
SCSSV satisfies the requirements of a single check valve."
25.265(a); 25.265(b); 25.265(d)(2)(F);
fail-safe auto SSV and SCSSV; injection wells (except disposal) require
Oooguruk
Oooguruk - Nuigsut
597
6
no
(i) double check valve, or (ii) single check valve and SSV; injection
25.26a(a); 25.265(b); 25.265(d)(2)(H);
"Injection wells (excluding disposal injectors) must be equipped with(i) a double check valve
Check valve requirements for injectors are not covered by
25.265(h)(5)readopted
arrangement or (ii) a single check valve and a SSV. A subsurface -controlled injection valve or
valve satisfies single check valve requirement; test every 6 months
SCSSV satisfies the requirements of a single check valve."
25.265(a); 25.265(b); 25.265(d)(2)(H);
"Injection wells (excluding disposal injectors) must be equipped with(i) a double check valve
fail-safe auto SSV and SCSSV; injection wells (except disposal) require
Oooguruk
Oooguruk - Kuparuk
596
6
no
(i) double check valve, or (ii) single check valve and SSV; injection
25.265(x); 25.265(b); 25.265(d)(2)(H);
"Injection wells (excluding disposal injectors) must be equipped with(i) a double check valve
Check valve requirements for injectors are not covered by
25.265(h)(5)readopted
arrangement or (ii) a single check valve and a SSV. A subsurface -controlled injection valve or
valve satisfies single check valve requirement; test every 6 months
Prudhoe Bay Unit
Raven
570
5
yes
fail-safe auto SSV and SCSSV; maintain list of wells w/ removed or
25.265(h)(5)
replaces SSSV nipple requirement for all wells
25.265(a)
N/A
deactivated SVS; sign on wellhead
25.265(a); 25.265(b); 25.265(d);
N/A
Readopted 25.265(d) dictates which wells require SSSV;
25.265(h)(5)
fail-safe auto SSV and SCSSV; injection wells (except disposal) require
Colville River Unit
Fiord
569
5
no
(i) double check valve, or (ii) single check valve and SSV; injection
25.265(a); 25.265(b); 25.265(d);
N/A
Readopted 25.265(d) dictates which wells require SSSV;
25.265(h)(5)
valve satisfies single check valve requirement; test every 6 months
25.265(a); 25.265(b); 25.265(d);
N/A
Readopted 25.265(d) dictates which wells require SSSV;
25.265(h)(5)
fail-safe auto SSV and SCSSV; injection wells (except disposal) require
Colville River Unit
Nanuq - Kuparuk
563
6
no
(i) double check valve, or (ii) single check valve and SSV; injection
25.265(h)(5)
replaces SSSV nipple requirement for all wells
25.265(a); 25.265(b); 25.265(d);
"Injection wells (excluding disposal injectors) must be equipped with(i) a double check valve
valve satisfies single check valve requirement; test every 6 months
25.265(h)(5)
arrangement or (ii) a single check valve and a SSV. A subsurface -controlled injection valve or
readopted regulation; readopted 25.265(d)(5) does not include
SCSSV satisfies the requirements of a single check valve."
fail-safe auto SSV and SCSSV; injection wells (except disposal) require
Colville River Unit
Nanuq
562
6
no
(i) double check valve, or (ii) single check valve and SSV; injection
25.265(x); 25.265(b); 25.265(d)(1);
"The setting depth of a required subsurface safety valve must be located in the tubing either
Existing pool rule established alternate SSSV setting depth;
25.265(h)(5)
above or below permafrost. Injection wells must be equipped with a double check valve
valve satisfies single check valve requirement; test every 6 months
Prudhoe Bay Unit
Put River
559
3
yes
fail-safe auto SSV; SSSV landing nipple below permafrost; test as
25.265(a); 25.265(b); 25.265(d)(2)(H)
arrangement or (ii) a single check valve and a SSV. A subsurface -controlled injection valve or
readopted regulation
SCSSV satisfies the requirements of a single check valve."
prescribed by Commission
Deep Creek Unit
Happy Valley
553
3
yes
SSV or SSSV
Prudhoe Bay Unit
Orion
505B
3
yes
fail-safe auto SSV; SSSV landing nipple below permafrost; test as
25.265(a); 25.265(b); 25.265(h)(5);
deactivated SVS was replaced with requirement to maintain a
N/A
prescribed by Commission
Prudhoe Ba Unit
Y
Polaris
484A
3
yes
fail-safe auto SSV; SSSV landing nipple below permafrost; test as
prescribed by Commission
Milne Point -
fail-safe auto SSV; SSSV landing nipple below permafrost; gas/MI
Milne Point Unit
477
5
yes
injection well require SSSV or injection valve below permafrost; test
Schrader Bluff
every 6 months
Prudhoe Bay Unit
Borealis
471
3
yes
fail-safe auto SSV; SSSV landing nipple below permafrost; gas/MI
injection well require SSSV below permafrost; test every 6 months
Northstar
NOrthstar
458A
4
no
fail-safe auto SSV and SCSSV; test as prescribed by Commission; 500
ft minimum setting depth for SSSV
Prudhoe Ba Unit
Y
Aurora
4576
3
yes
fail-safe auto SSV; SSSV landing nipple below permafrost; test every 6
months
fail-safe auto SSV; gas/MI injectors require SSV and single check
Kuparuk River Unit
Meltwater
456A
5
no
valve and SSSV landing nipple; water injection wells require (1) double
check valve, or (ii) single check valve and SSV; test every 6 months
Prudhoe Bay Unit
Midnight Sun
452
6
yes
fail-safe auto SSV (all injectors and producers capable of unassisted
flow to surface); test every 6 months
fail-safe auto SSV and SCSSV; SSSV may be installed above or below
Duck Island Unit
Eider
449
7
no
permafrost; injection wells require double check valve; LIPS trip
pressure; test every 6 months
fail-safe auto SSV and SCSSV (producers and gas injectors); water
Colville River Unit
Alpine
443B
5
no
injection wells require (i) double check valve, or (ii) single check valve
and SSV
fail-safe auto SSV; gas/MI injectors require SSV and single check
Kuparuk River Unit
Tabasco
435A
6
no
valve and SSSV landing nipple; water injection wells require (i) double
check valve, or (ii) single check valve and SSV; test every 6 months
fail-safe auto SSV ISM well and artificial lift); sign on well 9 SVS
Kuparuk River Unit;
deactivated; maintain list of wells w/deactivated SVS; test as
Kuparuk
432D
5
yes
prescribed by Commission; CO 432D.009 modifies Rule 5(b) - LPP
Milne Point Unit
may be defeated on W. Sak injectors w/surface pressure <500psi w/
notice when defeated and placed back in service
New Regulation Provisions
Revised Rule - "Well safety valve systems" (2)
Comment
Addressing Re is from Order
25.265(x); 25.265(b); 25.265(d)(2)(H);
"Injection wells (excluding disposal injectors) must be equipped with(i) a double check valve
Check valve requirements for injectors are not covered by
25.265(h)(5)
arrangement or (ii) a single check valve and a SSV. Asubsurface-controlled injection valve or
readopted regulation
SCSSV satisfies the requirements of a single check valve"
25.265(x); 25.2659(b); 25.265(d)(1);
"Injection wells (excluding disposal injectors) must be equipped with(i) a double check valve
Check valve requirements for injectors are not covered by
25.265(h)(5)
arrangement or (ii) a single check valve and a SSV. A subsurface -controlled injection valve or
readopted regulation
SCSSV satisfies the requirements of a single check valve."
25.265(x); 25.265(b); 25.265(d)(1);
"Injection wells (excluding disposal injectors) must be equipped with(i) a double check valve
Check valve requirements for injectors are not covered by
25.265(h)(5)arrangement
or (ii) a single check valve and a SSV. A subsurface -controlled injection valve or
readopted regulation
SCSSV satisfies the requirements of a single check valve."
25.265(a); 25.265(b); 25.265(d)(2)(F);
Requirement to maintain a wellhead sign and list of wells with
25.265(m)
N/A
deactivated SVS was replaced with requirement to maintain a
tag on well when not manned
25.26a(a); 25.265(b); 25.265(d)(2)(H);
"Injection wells (excluding disposal injectors) must be equipped with(i) a double check valve
Check valve requirements for injectors are not covered by
25.265(h)(5)readopted
arrangement or (ii) a single check valve and a SSV. A subsurface -controlled injection valve or
regulation
SCSSV satisfies the requirements of a single check valve."
25.265(a); 25.265(b); 25.265(d)(2)(H);
"Injection wells (excluding disposal injectors) must be equipped with(i) a double check valve
Check valve requirements for injectors are not covered by
25.265(h)(5)arrangement
or (ii) a single check valve and a SSV. A subsurface -controlled injection valve or
readopted regulation
SCSSV satisfies the requirements of a single check valve."
25.265(x); 25.265(b); 25.265(d)(2)(H);
"Injection wells (excluding disposal injectors) must be equipped with(i) a double check valve
Check valve requirements for injectors are not covered by
25.265(h)(5)readopted
arrangement or (ii) a single check valve and a SSV. A subsurface -controlled injection valve or
regulation
SCSSV satisfies the requirements of a single check valve."
25.265(a); 25.265(b); 25.265(d);
N/A
Readopted 25.265(d) dictates which wells require SSSV;
25.265(h)(5)
replaces SSSV nipple requirement for all wells
25.265(a)
N/A
25.265(a); 25.265(b); 25.265(d);
N/A
Readopted 25.265(d) dictates which wells require SSSV;
25.265(h)(5)
replaces SSSV nipple requirement for all wells
25.265(a); 25.265(b); 25.265(d);
N/A
Readopted 25.265(d) dictates which wells require SSSV;
25.265(h)(5)
replaces SSSV nipple requirement for all wells
25.265(a); 25.265(b); 25.265(d);
N/A
Readopted 25.265(d) dictates which wells require SSSV;
25.265(h)(5)
replaces SSSV nipple requirement for all wells
25.265(a); 25.265(b); 25.265(d);
N/A
Readopted 25.265(d) dictates which wells require SSSV;
25.265(h)(5)
replaces SSSV nipple requirement for all wells
25.265(a); 25.265(b); 25.265(d)(1)
"The minimum setting depth for a tubing conveyed subsurface safety valve is 500 feet."
Existing pool rule established a minimum setting depth for the
SSSV
25.265(a); 25.265(b); 25.265(d);
N/A
Readopted 25.265(d) dictates which wells require SSSV;
25.265(h)(5)
replaces SSSV nipple requirement for all wells
25.265(a); 25.265(b); 25.265(d);
"Injection wells (excluding disposal injectors) must be equipped with(i) a double check valve
Check valve requirements for injectors are not covered by
25.265(h)(5)
arrangement or (ii) a single check valve and a SSV. A subsurface -controlled injection valve or
readopted regulation; readopted 25.265(d)(5) does not include
SCSSV satisfies the requirements of a single check valve."
SSSV requirement for MI injectors
25.265(a); 25.265(b); 25.265(d);
N/A
Readopted 25.265(d) dictates which wells require SSSV;
25.265(h)(5)
replaces SSSV nipple requirement for all wells
25.265(x); 25.265(b); 25.265(d)(1);
"The setting depth of a required subsurface safety valve must be located in the tubing either
Existing pool rule established alternate SSSV setting depth;
25.265(h)(5)
above or below permafrost. Injection wells must be equipped with a double check valve
check valve requirements for injectors are not covered by
arrangement"
readopted regulation
"Injection wells (excluding disposal injectors) must be equipped with(i) a double check valve
Check valve requirements for injectors are not covered by
25.265(a); 25.265(b); 25.265(d)(2)(H)
arrangement or (ii) a single check valve and a SSV. A subsurface -controlled injection valve or
readopted regulation
SCSSV satisfies the requirements of a single check valve."
25.265(a); 25.265(b); 25.265(d);
"Injection wells (excluding disposal injectors) must be equipped with(i) a double check valve
Check valve requirements for injectors are not covered by
arrangement or (ii) a single check valve and a SSV. A subsurface -controlled injection valve or
readopted regulation; readopted 25.265(d)(5) does not include
25.265(h)(5)
SCSSV satisfies the requirements of a single check valve."
SSSV requirement for MI injectors
Requirement to maintain a wellhead sign and list of wells with
25.265(a); 25.265(b); 25.265(h)(5);
deactivated SVS was replaced with requirement to maintain a
N/A
tag on well when not manned; administrative approval CO
25.265(m)
432D.009 remains effective [re:defeating the LIPS when surface
injection pressure for West Sak water injector is <500ps]
Page 1 of 2
Orders Establishing Requirements for Well Safety Valve Systems
1/7/2011
Unit/Field
Pool
Conservation
Order 1
Rule
Rescind Rule?
Existing Order Requirement
Kuparuk River Unit
Tarn
430A
6
no
fail-safe auto SSV; gaslMI injectors require SSV and single check
valve and SSSV landing nipple; water injection wells require (i) double
SCSSV satisfies the requirements of a single check valve."
SSSV requirement for MI injectors
25.265(a); 25.265(b); 25.265(h)(5)
"Injection wells must be equipped with a double check valve arrangement."
check valve, or (ii) single check valve and SSV; test every 6 months
Milne Point Unit
Milne Point - Sag
423
7
no
fail-safe auto SSV; injection wells require double check valve; test
25.265(x); 25.265(b); 25.265(d);
River
readopted regulation; readopted 25.265(d)(5) does not include
25.265(h)(5)
SCSSV satisfies the requirements of a single check valve. The Low Pressure Pilot may be
every 6 months
defeated on West Sak water injectors with surface injection pressure less than 500psi "
4066.001 remains effective [re:defeating the LPS when surface
fail-safe auto SSV; gas/MI injectors require SSV and single check
25.265(a); 25.265(b); 25.265(h);
25.265(m)
N/A
valve and SSSV landing nipple; water injection wells require (i) double
Kuparuk River Unit
Kuparuk -West Sak
4066
6
no
check valve, or (ii) single check valve and SSV; test every 6 months;
tag on well when not manned
CO 4066.001 modifies Rule 6(e) - LPP may be defeated on W. Sak
25.265(a); 25.265(b); 25.265(d);
N/A
Readopted 25.265(d) dictates which wells require SSSV;
25.265(h)(5)
injectors w/surface pressure <500psi w/ notice when defeated and
25.265(a); 25.265(b); 25.265(d);
N/A
Readopted 25.265(d) dictates which wells require SSSV;
25.265(h)(5); 25.265(m)
placed back in service
25.265(a); 25.265(b); 25.265(d);
N/A
Readopted 25.265(d) dictates which wells require SSSV;
25.2650); 25.265(m)
fail-safe auto SSV and SCSSV; LPS trip pressure; readily accessible
Badami
Badami
4028
6
yes
control unit; SSSV below permafrost; NTE 210days between tests;
25.265(a); 25.265(b)
N/A
25.265(a); 25.265(b); 25.265(h)(5);
submit test results electronically within 14days; SVS defeated/removed
25.265(m)
N/A
deactivated SVS was replaced with requirement to maintain a
only if well SI or pad continuously manned
Prudhoe Bay Unit
North Prudhoe
345
4
yes
fail-safe auto SSV (S/D well and artificial lift); sign on well if SVS
deactivated; maintain list of wells w/deactivated SVS; test as
25.265(h); 25.265(n); 25.265(0)
N/A
AOGCC Policy - SVS Failures; issued by order of the
Commission 3/30/1994 (signed by Commission Chairman
prescribed by Commission
fail-safe auto SSV (S/D well and artificial lift); if SSSV installed it must
Prudhoe Bay Unit
Prudhoe
341 E
5
yes
be maintained and tested as part of SVS; sign on well if SVS
deactivated; maintain list of wells w/deactivated SVS; test as
prescribed by Commission
Prudhoe Bay Unit
Niakuk
329A
5
yes
fail-safe auto SSV and SCSSV; maintain list of wells w/ removed or
deactivated SVS; sign on wellhead
Prudhoe Bay Unit
Pt. McIntyre
317B
8
yes
fail-safe auto SSV and SCSSV; SSSV may be rermoved as part of
routine well ops w/o notice
Prudhoe Bay Unit
West Beach
311 B
6
yes
fail-safe auto SSV; sign on well if SVS deactivated; maintain list of wells
w/deactivated SVS; test as prescribed by Commission
West Fork
&east Fork (Sterling
300
5
yes
fail-safe auto SVS on each production tubing
Prudhoe Bay Unit
Lisburne
207A
7
yes
fail-safe auto SSV; sign on well if SVS deactivated; maintain list of wells
w/deactivated SVS; test as prescribed by Commission
Prudhoe Bay Unit
Prudhoe - Kuparuk
98A
5
yes
suitable automatic safety valve installed below base of permafrost to
prevent uncontrolled flow
Statewide
N/A
N/A
N/A
yes
Commission policy dictating SVS performance testing
requirements
Footnotes
(1) No SVS rules found in Injection Orders
(2) New title for Revised Rule; "N/A" means entire pool rule to be rescinded
New Regulation Provisions
Re is from Order
Revised Rule - "Well safetyvalves stems" �2 )
CommentAddressin
25.265(a); 25.265(b); 25.265(d);
,injection wells (excluding disposal injectors) must be equipped with(i) a double check valve
Check valve requirements for injectors are not covered by
25.265(h)(5)
arrangement or (ii) a single check valve and a SSV. A subsurface -controlled injection valve or
readopted regulation; readopted 25.265(d)(5) does not include
SCSSV satisfies the requirements of a single check valve."
SSSV requirement for MI injectors
25.265(a); 25.265(b); 25.265(h)(5)
"Injection wells must be equipped with a double check valve arrangement."
Check valve requirements for injectors are not covered by
readopted regulation
"Injection wells (excluding disposal injectors) must be equipped
1 ( 9 Po l ) q pped double check valve
Check valve requirements for injectors are not covered by
25.265(x); 25.265(b); 25.265(d);
ce-c) t
arrangement or (ii) a single check valve and a SSV. Asubsurface-controlled injection valve or
readopted regulation; readopted 25.265(d)(5) does not include
25.265(h)(5)
SCSSV satisfies the requirements of a single check valve. The Low Pressure Pilot may be
SSSV requirement for MI injectors; administrative approval CO
defeated on West Sak water injectors with surface injection pressure less than 500psi "
4066.001 remains effective [re:defeating the LPS when surface
injection pressure for West Sak water injector is <500psi]
25.265(a); 25.265(b); 25.265(h);
25.265(m)
N/A
25.265(a); 25.265(b); 25.265(h)(5);
Requirement to maintain a wellhead sign and list of wells with
25.265(m)
N/A
deactivated SVS was replaced with requirement to maintain a
tag on well when not manned
25.265(a); 25.265(b); 25.265(d);
N/A
Readopted 25.265(d) dictates which wells require SSSV;
25.265(h)(5)
replaces SSSV nipple requirement for all wells
25.265(a); 25.265(b); 25.265(d);
N/A
Readopted 25.265(d) dictates which wells require SSSV;
25.265(h)(5); 25.265(m)
replaces SSSV nipple requirement for all wells
25.265(a); 25.265(b); 25.265(d);
N/A
Readopted 25.265(d) dictates which wells require SSSV;
25.2650); 25.265(m)
replaces SSSV nipple requirement for all wells
25.265(a); 25.265(b); 25.265(d);
N/A
Readopted 25.265(d) dictates which wells require SSSV;
25.265(h)(5); 25.265(m)
replaces SSSV nipple requirement for all wells
25.265(a); 25.265(b)
N/A
25.265(a); 25.265(b); 25.265(h)(5);
Requirement to maintain a wellhead sign and list of wells with
25.265(m)
N/A
deactivated SVS was replaced with requirement to maintain a
tag on well when not manned
25.265(d)
N/A
Readopted 25.265(d) dictates which wells require SSSV;
replaces SSSV nipple requirement for all wells
25.265(h); 25.265(n); 25.265(0)
N/A
AOGCC Policy - SVS Failures; issued by order of the
Commission 3/30/1994 (signed by Commission Chairman
Dave Johnson)
Page 2 of 2
•
•
Public Hearing Record
And
Backup Information available in Other 66
�oALAI,a))KA
FRANK H. MURKOWSKI, GOVERNOR
�s[J•►7KA OIL � GAS 333 W. 7tl1 AVENUE, SUITE 100
CONSERVATIONCOMUSS`ION ANCHORAGE, ALASKA 99501-3539
PHONE (907) 279-1433
FAX (907) 2767542
ADMINISTRATIVE APPROVAL NO 317B.001
Mr. Francis Sommer
Prudhoe Bay Asset Manager
BP Exploration (Alaska) Inc.
P. 0. Box 196612
Anchorage, AK 99519-6612
Dear Mr. Sommer:
By letter dated September 9, 2003, BP Exploration (Alaska), Inc. ("BPXA") requested
authorization to commingle a portion of production from the Pt. McIntyre Oil Pool
("PMOP"), Drillsite PM2 with production from the Prudhoe Oil Pool and process the
fluids within Prudhoe Bay Unit ("PBU") Initial Participating Area ("IPA"). This will
require a change in Conservation Order 317B, Rule 10 concerning allocation of
production, which currently allows commingling of PMOP production only at the
Lisburne Production Center.
The production will be diverted to the low-pressure system of Gathering Center 1
("GC 1 "), greatly decreasing wellhead pressure. This has several effects:
o Oil production from PMOP will increase due to less backpressure.
o Gas and water constraints at the Lisburne Production Center ("LPC") will
be reduced due to the diversion of fluids to GCI.
o Additional water volumes flowing from PM2 to GC1 will be available for
injection to other oil pools needing greater water injection volumes for
reservoir performance.
o PMOP producers that cannot currently flow will be brought on line,
increasing reserves and improving the pattern conformance.
Initially, BPXA proposed that NGLs processed at GC1 not be allocated back to the Pt.
McIntyre reservoir. Rather, all gas produced into the GCI facilities would be treated as
indigenous IPA natural gas. By letter dated October 16, 2003, the Department of
Revenue ("DOR") proposed an alternative method of allocation of NGLs. By letter dated
October 27, 2003, the Department of Natural Resources ("DNR) endorsed DOR's
proposal. Per your letter of November 11, 2003 we understand that you agree with
DOR's proposal.
CO 317B.001
December 10, 2003
Page 2 of 3
The Commission finds that the proposed commingling of production from the PMOP
with other PBU production will significantly increase ultimate recovery, will not promote
waste or jeopardize correlative rights, and is based on sound engineering principles.
Rule 10 is amended to read as follows:
a. Production from the Pt. McIntyre and Stump Island Oil Pools may be
commingled at the surface with production from other pools for
processing at the Lisburne Production Center ("LPC") and production
from the Pt. McIntyre Oil Pool Drillsite PM2 may be commingled at
the surface with production from other pools for processing at the
Prudhoe Bay Unit IPA Gathering Center 1 ("GC1" ), prior to custody
transfer.
b. Daily production from all wells will be based on empirical well
performance curves derived from 3-phase flow equations and
production well test data, and will be a function of flowing tubing
pressure and gas -lift rate. The method is described within the
"Prudhoe Bay Unit (PBU) Western Satellite Production Metering Plan
— Policies and Procedures Document" dated August 1, 2002
c. A minimum of two well tests per month will be performed on each
well, when operational conditions allow.
d. Wells will use the associated process facility allocation factor for oil,
gas, and water. Pt. McIntyre wells that flow to both GCI and LPC in
the same month will use a prorated (GC 1 and LPC) well allocation
factor for oil, gas, and water.
e. Natural gas liquids ("NGLs") processed at the LPC will be allocated to
each pool based on actual gas production volumes and NGL process
simulations. Process simulations will be updated at least once per year
based on NGL samples and results reported to the Commission.
f. NGLs attributable to the PM2 to GC 1 gas stream and recovered at the
CGF will be allocated by calculating the amount of separator off -gas,
excluding gas lift gas, attributable to Pt. McIntyre wells producing into
GC -1. The percentage of total separator off -gas delivered to the CGF,
that is Pt. McIntyre formation gas, multiplied by the total NGL
recovery at CGF, yields the amount of NGLs to be allocated to Pt.
McIntyre.
g. Water volumes will be determined by API/MPMS approved methods,
or the use of industry proven, on-line water cut measurement devices
approved by the Commission.
h. API gravity will be determined for each producing well annually by an
API/MPMS approved method.
i. Gas samples will be taken and analyzed for composition from each
non -gas lifted producing well yearly.
CO 317B.001
December 10, 2003
Page 3 of 3
Yearly allocation process reviews will be held with the Commission.
The initial allocation review will be no later than July 1, 2004.
DONE at Anchorage, Alaska and dated December 10, 2003.
Sarah Palm Daniel T. Seamount, Jr.
Chair
Commissioner
zffmE o ALASKA
SARAH PALIN, GOVERNOR
ALASKA OIL AND GABS 333 W 7th AVENUE, SUITE 100
CONSERVATION COMIISSION ANCHORAGE, ALASKA 99501-3539
PHONE (907) 279-1433
FAX (907) 276-7542
ADMINISTRATIVE APPROVAL NO. 31713.002
Mr. Mark C. Weggeland
GPMA Resource Manager
BP Exploration (Alaska) Inc.
P.O. Box 196612
Anchorage, AK 99519-6612
Dear Mr. Weggeland:
The Alaska Oil and Gas Conservation Commission ("Commission") is amending the
reporting dates of Rule 15 Pt. McIntyre Oil Pool Annual Reservoir Report of
Conservation Order 317B - Pt. McIntyre Oil Field, Pt. McIntyre Oil Pool, Stump Island
Oil Pool. The change is necessary so that the rule is not contradictory to the schedule
agreed upon by the Commission and BP Exploration (Alaska) Inc.
Rule 15 Pt. McIntyre Oil Pool Annual Reservoir Report is amended to read as follows
(additions are in bold and [deletions are bracketed]):
Rule 15 Pt. McIntyre Oil Pool Annual Reservoir Report
An annual Pt. McIntyre Oil Pool surveillance report will be required on a
schedule agreed upon by the Commission and the operator [by April 1 of each
year]. The report shall include but is not limited to the following:
a. Progress of enhanced recovery project(s) implementation and reservoir
management summary including engineering and geotechnical parameters.
b. Reservoir voidage balance by month of produced fluids and injected fluids.
c. Analysis of reservoir pressure surveys within the pool.
d. Results and where appropriate, analysis of production and injection log
surveys, tracer surveys and observation well data and surveys.
e. Results of any special monitoring.
f. Future development plans.
CO 317B.002 •
May 23, 2007
Page 2 of 2
g. Review of Annual Plan of Operations and Development.
As provided in AS 31.05.080, within 20 days after written notice of this decision, or such
further time as the Commission grants for good cause shown, a person affected by it may
file with the Commission an application for rehearing. A request for rehearing is
considered timely if it is received by 4:30 PM on the 23rd day following the date of this
letter, or the next working day if the 23rd day falls on a holiday or weekend. A person
may not appeal a Commission decision to Superior Court unless rehearing has been
requested.
aka and dated May 23, 2007.
IV '
Daniel T. Seamount, Jr.
Commissioner
zX --
Cathy . Foerster
Com issioner
Various Administrative Approvals for North So
•
Subject: Various Administrative Approvals for North Slope
From: Jody Colombie <jody_colombie@admin.state.ak.us>
Date: Thu, 24 May 2007 06:39:39 -0800
To: undisclosed -recipients:;
BCC: Cynthia B Mciver <bren_mciver@admin.state.ak.us>, Christine Hansen
<c:hansen@iogcc.state.ok.us>, Terrie Hubble <hubbletl@bp.com>, Sondra Stewman
<StewmaSD@BP.com>, stanekj <stanekj@unocal.com>, trmjrl <trmjrl@aol.com>, jdarlington
<jdarlington@forestoil.com>, nelson <knelson@petroleumnews.com>, Mark Dalton
<mark.dalton@hdrinc.com>, Shannon Donnelly<shannon.donnelly@conocophillipscom>, "Mark P.
Worcester" <mark.p.Worcester@conocophillips.corn>, Bob <bob@inletkeeper.org>, tjr
<tjr@dnr.state.ak.us>, bbritch <bbritch@alaska.net>, mjnelson <mjnelson@purvingertz.com>, Charles
O'Donnell <charles.o'donnell@veco.com>, "Randy L. Skillern" <SkilleRL@BP.com>, "Deborah J.
Jones" <JonesD6@BP.com>, "Steven R. Rossberg" <RossbeRS@BP.com>, Lois
<lois@inletkeeper.org>, Dan Bross <kuacnews@kuac.org>, Gordon Pospisil <PospisG@BP.com>,
"Francis S. Sommer" <SommerFS@BP.com>, Mikel Schultz <Mikel.Schultz@BP.com>, "Nick W.
Glover" <GloverNW@BP.com> "Daryl J. Kleppin" <KleppiDE@BP.com>, "Janet D. Platt"
<PlattJD@BP.com>, "Rosanne M. Jacobsen" <JacobsRM@BP.com>, ddonkel <ddonkel@cfl.rr.com>,
mckay <mckay@gci.net>, Barbara F Fullmer <barbara.Efullmer@conocophillips.com>, doug_schultze
<doug_schultze@xtoenergy.com> Hank Alford <hank.alford@exxonmobil.com>, Mark Kovac
<yesno I @gci.net>, gspfoff <gspfoff@aurorapower.com>, Gregg Nady <gregg.nady@shell.com>, Fred
Steece <fred.steece@state.sd.us> rcrotty <rcrotty@ch2m.com>, jejones <jejones@aurorapower.com>,
dapa <dapa@alaska.net> , eyancy <eyancy@seal-tite.net>, "James M. Ruud"
<james.m.ruud@conocophillips.com>, Brit Lively <bl@mapalaska.com>, jah <j ah@dnr. state. ak.us>,
buonoje <buonoje@bp.com>, Mark Hanley <mark_hanley@anadarko.com>, Julie Houle
<julie_houle@dnr.state. ak.us>, John W Katz <jwkatz@alaskadc.org>, tablerk'<tablerk@unocal.com>
Brady <brady@aoga.org>, Brian Havelock <beh@dnr.state.ak.us> Jim White <jimwhite@satx.rr.com>,
"John S. Haworth" <john.s.haworth@exxonmobil.com>, marty <marty@rkindustrial.com>, ghammons
<ghammons@aol.com>, rmclean <rmclean@pobox.alaska.net>, mkm7200 <mkm7200@aol.com>,
Brian Gillespie<ifbmg@uaa.alaska.edu>, David L.Boelens <dboelens@aurorapower.com>, Todd
Durkee <todd.durkee@anadarko.com>, Gary Schultz <gary_schultz@dnr.state.ak.us>, Wayne Rancier
<RANCIER@petro-canada.ca>, Brandon Gagnon <bgagnon@brenalaw.com>, Paul Winslow
<pmwinslow@forestoil.com>, Sharmaine Copeland <copelasv@bp.com>, Kristin Dirks
<kristin dirks@dnr.state.ak.us>, Kaynell Zeman <kjzeman@marathonoil.eom>, John Tower
<John.Tower@eia.doe.gov>, Bill Fowler <Bill_Fowler@anadarko.COM>, Scott Cranswick
<scott.cranswick@mms.gov>, Brad McKim <mckimbs@BP.com>, James Scherr
<james.scherr@mms.gov>, Tim Lawlor <Tim Lawlor@ak.,blm.gov>, Lynnda Kahn
<Lynnda_Kahn@fws.gov>, Jerry Dethlefs <Jerry.CDethlefs@conocophillips.com>, crockett@aoga.org,
Tamera Sheffield <sheffield@aoga.org>, Jon Goltz <Jon. Goltz@conocophillips. com>, Roger Belman
<roger.belman@conocophillips.com>, Mindy Lewis <mlewis@brenalaw.com>,'Kari Moriarty
<moriarty@aoga.org>, Patty Alfaro <palfaro@yahoo.com>, , Gary Rogers
<gary_rogers@revenue.state.ak.us>, Arthur Copoulos <Arthur_Copoulos@dnr.state. ak.us>,`Ken
<klyons@otsintl.com>, Steve Lambert <salambert@unocal.com>, Joe Nicks'<news@radiokenai.com>,
Jerry McCutcheon <susitnahydronow@yahoo.com>, Bill Walker <bill-wwa@ak.net>, Paul Decker
<paul_decker@dnr. state. ak.us>, Aleutians East Borough <admin@aleutianseast.org> Marquerite
kremer <marguerite_kremer@dnr.state. ak.us>, Mike Mason <mike@kbbi.org>, Garland Robinson
<gbrobinson@marathonoil.com> Cammy Taylor <cammy_taylor@dnr.state. ak.us>, Thomas E
Maunder <tom_maunder@admin.state.ak.us>, :Stephen F Davies <steve_davies@admin. state.ak.us>,
Keith Wiles <kwiles@marathonoil.com>, `Deanna Gamble <dgamble@kakivik.com>, James B Regg
of 3 5/24/2007 6:40 AM
Various Administrative Approvals for North Sib
•
<jim_regg@admin. state.ak.us>, Catherine P Foerster<cathy_foerster@admin.state.akus>, gregory
micallef <micallef@clearwire.net>, Laura Silliphant <Laura_silliphant@dnr.state. ak.us>, David
Steingreaber <david.esteingreaber@exxonmobil.corn>, akpratts@acsalaska.net, Robert Campbell
<Robert. Campbell@reuters. com>, Steve Moothart <steve_moothart@dnr.state.ak.us>, Anna Raff
<anna.raff@dowj ones. com>, Cliff Posey <cliff@posey.org>, , Meghan Powell
<Meghan.Powell@asrcenergy.com>, Temple Davidson <temple_davidson@dnr.state.akus>, Walter
Featherly<WFeatherly@PattonBoggs.com>, Tricia Waggoner <twaggoner@nrginc.com>, John Spain
<jps@stateside.com>, Cody Rice <Cody_Rice@legis.state.ak.us>,;John Garing;<garingJD@bp.com>,
Harry Engel <engelhr@bp.com>, Jim Winegarner<jimwinegarner@brooksrangepetro.com>, Matt
Rader <matt_rader@dnr.state. ak.us>, carol smyth <carol. smyth@shell. com>, Arthur C Saltmarsh
<art_saltmarsh@admin. state.ak.us>, Chris Gay <cdgay@marathonoil.com>, foms@mtaonline.net, Rudy
Brueggeman<rudy.brueggemann@international.gc.ca>, Cary Carrigan <cary@kfgd.com>, Sonja
Frankllin <sfranklin6@bloomberg.net>, Mike Bill <Michael'.Bill@bp.com>, Walter Quay
<WQuay@chevron.com>, "Alan Birnbaum <\"\"Alan J Birnbaum \">"
<alan_bimbaum\"@law. state.ak.us>, Randall Kanady<Randall.B.Kanady@conocophillips.com>, MJ
Loveland <N1878@conocophillips.com>, Dave Roby<dave_roby@admin. state.ak.us>, James B Regg
<j im_regg@admin. state. ak. us>
Jody Colombie <jody colombie@admin. state. ak.us>
Special Staff Assistant
Alaska Oil and Gas Conservation Commission
Department of Administration
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Kenai National Wildlife Refuge Penny Vadla Richard Wagner
Refuge Manager 399 West Riverview Avenue PO Box 60868
PO Box 2139 Soldotna, AK 99669-7714 Fairbanks, AK 99706
Soldotna, AK 99669-2139
Cliff Burglin Bernie Karl North Slope Borough
PO Box 70131 K&K Recycling Inc. PO Box 69
Fairbanks, AK 99707 PO Box 58055 Barrow, AK 99723
Fairbanks, AK 99711
Williams Thomas
Arctic Slope Regional Corporation
Land Department
Box 129
Barrow, AK
99723
vl
Mary Jones
David McCaleb
Mona Dickens
XTO Energy, Inc.
IHS Energy Group
Tesoro Refining and Marketing Co.
Cartography
GEPS
Supply & Distribution
810 Houston Street, Ste 2000
5333 Westheimer, Ste 100
300 Concord Plaza Drive
Ft. Worth, TX 76102-6298
Houston, TX 77056
San Antonio, TX 78216
George Vaught, Jr.
Jerry Hodgden
Richard Neahring
PO Box 13557
Hodgden Oil Company
NRG Associates
Denver, CO 80201-3557
408 18th Street
President
Golden, CO 80401-2433
PO Box 1655
Colorado Springs, CO 80901
John Levorsen
Michael Parks
Mark Wedman
200 North 3rd Street, #1202
Marple's Business Newsletter
Halliburton
Boise, ID 83702
117 West Mercer St, Ste 200
6900 Arctic Blvd.
Seattle, WA 98119-3960
Anchorage, AK 99502
Baker Oil Tools
Schlumberger
Ciri
4730 Business Park Blvd., #44
Drilling and Measurements
Land Department
Anchorage, AK 99503
2525 Gambell Street #400
PO Box 93330
Anchorage, AK 99503
Anchorage, AK 99503
Ivan Gillian
Jill Schneider
Gordon Severson
9649 Musket Bell Cr.#5
US Geological Survey
3201 Westmar Cr.
Anchorage, AK 99507
4200 University Dr.
Anchorage, AK 99508-4336
Anchorage, AK 99508
Jack Hakkila
Darwin Waldsmith
James Gibbs
PO Box 190083
PO Box 39309
PO Box 1597
Anchorage, AK 99519
Ninilchick, AK 99639
Soldotna, AK 99669
Kenai National Wildlife Refuge Penny Vadla Richard Wagner
Refuge Manager 399 West Riverview Avenue PO Box 60868
PO Box 2139 Soldotna, AK 99669-7714 Fairbanks, AK 99706
Soldotna, AK 99669-2139
Cliff Burglin Bernie Karl North Slope Borough
PO Box 70131 K&K Recycling Inc. PO Box 69
Fairbanks, AK 99707 PO Box 58055 Barrow, AK 99723
Fairbanks, AK 99711
Williams Thomas
Arctic Slope Regional Corporation
Land Department
Box 129
Barrow, AK
99723
vl
Tlir STATE.
°ALASKA
GOVERNOR MICHAEL I. DUNLEAVY
ADMINISTRATIVE APPROVAL
CONSERVATION ORDER NO. 207D.001
CONSERVATION ORDER NO. 311B.003
CONSERVATION ORDER NO. 317B.003
CONSERVATION ORDER NO. 329B.005
CONSERVATION ORDER NO. 345.002
CONSERVATION ORDER NO. 362A.006
CONSERVATION ORDER NO. 570.010
Ms. Katrina Garner
PBU Area Manager
BP Exploration (Alaska) Inc.
P.O. Box 196612
Anchorage, AK 99519-6612
Re: Docket Number: CO -20-003
Alaska Oil and Gas
Conservation Commission
333 West Seventh Avenue
Anchorage, Alaska 99501-3572
Main: 907.279.1433
Fax: 907.276.7542
www.aogcc.olaska.gov
Request for Administrative Approval for Conforming Prudhoe Bay Unit (PBU)
Greater Point McIntyre Area Satellite Pool Rules for Consistency
Prudhoe Bay Unit
Lisburne Oil Pool — Conservation Order (CO) 207D
West Beach Oil Pool — CO 311 B
Pt. McIntyre and Stump Island Oil Pools — CO 317B
Niakuk Oil Pool — CO 329B
North Prudhoe Bay Oil Pool — CO 345
Greater Point McIntyre Area — CO 362A
Raven Oil Pool — CO 570
Dear Ms. Garner:
By letter dated February 20, 2020, BP Exploration (Alaska) Inc. (BPXA) requested administrative
approval to amend the pool rules in the above referenced orders to bring conformity and
consistency to the rules governing operations in the pools in the Greater Point McIntyre Area
(GPMA), to make operations more efficient, and to make compliance oversight for the Alaska Oil
and Gas Conservation Commission (AOGCC) simpler.
There are several requests that apply broadly across multiple GPMA pools. These are as follows.
COs 207D.001, 31 1B.003,317B.003, 329B.005, 345.002,362A.006,570.010
April 3, 2020
Page 2 of 12
Well Spacing Requirements:
Currently, the Lisburne Oil Pool (LOP) has an interwell spacing requirement of one well per
government quarter section and no pay opened within 1,000 feet of another well. The West Beach
Oil Pool (WBOP) has an interwell spacing requirement of one well per 160 acres until
circumstances warrant the AOGCC changing it. The Pt. McIntyre Oil Pool (PMOP) has a spacing
requirement of one well per 40 acres with no pay open within 500 feet of another well. The Niakuk
Oil Pool (NOP) gives the AOGCC the authority to approve the drilling of any well that is at least
500 feet from the affected area boundary and does not have open pay within 1,000 feet of another
well. The Raven Oil Pool (ROP) has an interwell spacing requirement of 20 acres with no pay
open within 500 feet of the affected area external boundary.
BPXA requests that the interwell spacing requirements be eliminated and that the only spacing
requirement be a 500 -foot offset from property lines where the landowner is not the same on both
sides of the line. At the time the spacing requirements in these pool rules were imposed wells were
being drilled nearly vertically. Because modern horizontal and multi -lateral wells are now being
utilized to develop pools, BPXA needs flexibility to drill wells as dictated by the geology and
reservoir models in order to maximize recovery. Standardizing the spacing requirements by
eliminating interwell spacing requirements while retaining property offset requirements will result
in improved recovery while protecting correlative rights.
Pressure Survey Requirements:
BPXA requests that the pressure survey requirements be modified so that compliance with
regulatory oversight becomes simpler and data is collected in a meaningful manner. Currently, the
Lisburne Oil Pool (LOP) requires at least one pressure survey be taken each year from each
producing drillsite and that the results be submitted monthly, while the West Beach Oil Pool
(WBOP), Pt. McIntyre Oil Pool (PMOP), and Niakuk Oil Pool (NOP) require one pressure survey
per producing governmental section per year and results submitted quarterly. North Prudhoe Bay
Oil Pool (NPBOP) requires one pressure survey per producing governmental section but doesn't
specify when the results need to be reported, and Raven Oil Pool (ROP) requires one pressure
survey per reservoir compartment where production wells exist and specifies the results are to be
reported in the annual reservoir surveillance report. The inconsistency in where pressure surveys
need to be collected and how the results are to be reported makes it more difficult for the operator
to stay in compliance without yielding any benefit that could not be obtained by more uniform
collection and reporting requirements.
Moreover, after decades of development and reporting, the pools in the PBU are well understood
and have sophisticated reservoir models. At this point, monitoring of reservoir pressure is
important for proper reservoir development and targeted pressure surveys would provide the most
useful information for reservoir development purposes. Presenting the results of the reservoir
pressure surveys from the prior year in the annual reservoir surveillance report and proposing a
plan for collection of reservoir pressure surveys in the coming year as part of the annual reservoir
surveillance report will give the AOGCC an opportunity to review the data and ensure the proposed
plans are adequate. This is consistent with how the other pools in the PBU are managed.
COs 207D.001, 31 1B.003, 317B.003, 329B.005, 345.002,362A.006, 570.010
April 3, 2020
Page 3 of 12
Well Testing:
The GPMA pools have inconsistent well testing requirements that include quarterly allocation
process reviews, monthly allocation reports, determining water volumes by API approved methods
or an on-line water cut meter, monthly or annual API gravities for each well depending on the
pool, gas samples collected yearly from each non -gas lifted producer, a minimum of two well tests
per well, and twice monthly well tests. BPXA requests to eliminate the quarterly allocation process
reviews and monthly allocation reports and proposes instead to provide an allocation factor report
as part of the annual surveillance report as is done elsewhere in the PBU. BPXA also requests
eliminating the water volume calculation, API gravity, and gas sampling requirements since at this
point, recovery methods in these pools are unchanging and render this data of little benefit. Finally,
BPXA requests to eliminate the requirement to test each producing well at least twice each month
and instead require a minimum of one test per month per well. This request is consistent with how
the rest of the PBU is managed and allows BPXA to maximize its well testing resources by testing
the wells with stable production less frequently and testing the wells with less stable production
more frequently to improve the overall allocation of production.
Additionally, BPXA makes several requests that apply only to a single pool. These include the
following.
LOP Gas Oil Ratio (GOR) Testing Requirement:
The LOP requires a GOR test on each producer within 90 to 120 days of commencement of regular
production and then semiannually thereafter. The monthly well testing requirements for allocation
purposes will provide adequate information as to the producing GOR of the wells so as to render
the current rule unnecessary.
LOP Gas Cap Water Injection (GCWI) Project:
BPXA proposes to remove the 20,000 BWPD injection rate limit and raise the injection pressure
limit from 0.55 psi/ft to 0.85 psi/ft. When the LOP GCWI was initially approved it was thought
that the water injection rate and pressure must be constrained to prevent parting the LOP matrix to
prevent premature water breakthrough. After several years of operation, such strict limits on
injection rates and pressure do not appear to be necessary and the GCWI project will still function
as planned if injection rates are constrained to 0.85 psi/ft.
PMOP Enhanced Oil Recovery (EOR) Project Report:
BPXA requests elimination of the annual EOR project report for the PMOP because miscible
injectant for this pool is now being supplied by PBU Central Gas Facility and not from the Lisburne
Production Center. As such, a PMOP EOR project specific report is no longer needed as the MI
composition is the same as elsewhere in the PBU.
Conclusions:
Each of the affected COs contain an administrative action rule that allows the AOGCC to
administratively amend the orders provided the proposed change does not promote waste,
jeopardize correlative rights, is based on sound engineering and geoscience principles, and will
COs 207D.001, 311 B.003, 317B.003, 329B.005, 345.002, 362A.006,570.010
April 3, 2020
Page 4 of 12
not increase the risk of fluid movement into freshwater. All of BPXA's requested changes comply
with these requirements. The proposals to consolidate the rules across the GPMA pools, eliminate
or modify the GOR testing and GCWI project rules in the LOP, and eliminating the requirement
for an unnecessary EOR project report for the PMOP will simplify operations for BPXA, make
uniform the compliance requirements, and will not impact ultimate recovery. Eliminating interwell
spacing requirements, while maintaining a minimum offset distance from property lines where
ownership changes, will maximize ultimate recovery while also protecting correlative rights. The
only proposed change that could potentially have an impact on fluid movement into fresh water is
the elimination of the water injection rate limitation and increasing the water injection pressure
limitation for the LOP GCWI. However, since the proposed injection pressure limit is below the
fracture gradient of the confining interval this will ensure the LOP GCWI injection remains in the
LOP. The proposed changes can be made administratively.
Finally, on its own motion, the AOGCC is revising the administrative action rules, where
necessary, to be consistent and uniform with the language currently used by the AOGCC for these
rules.
Now, therefore, it is ordered that the subject conservation orders are amended as shown below.
Lisburne Oil Pool — Conservation Order No. 207D
Rule 3. WELL SPACING
There shall be no restrictions to well spacing within the affected area except that no pay
may be opened in a well which is closer than 500 feet of an external property line where
the owners and landowners are not the same on both sides of the line.
Rule 9. GAS -OIL RATIO TESTS (Rescinded)
Rule 10. PRESSURE SURVEYS
a. An Annual Pressure Surveillance Plan shall be submitted to the AOGCC in conjunction
with the Annual Lisburne Oil Pool Reservoir Surveillance Report by June 151 of each
year. This plan will contain the number and approximate location of pressure surveys
anticipated for the next calendar year and, unless AOGCC orders otherwise, the plan
will be deemed approved 45 days after submission to AOGCC.
b. Data from the surveys required in (a) of this rule shall be submitted with the Annual
Lisburne Oil Pool Reservoir Surveillance Report by June 15Th of each year on Form 10-
412. Data submitted shall include rate, pressure, time depths, temperature and any well
condition necessary for the complete analysis of each survey. The datum for the
pressure surveys is 8,900 true vertical feet subsea. Transient pressure surveys obtained
by a shut-in build-up test, and injection well pressure fall-off test, a multirate test, or
an interference test are acceptable. Calculation of bottom -hole pressures from surface
data will be permitted for water injection wells. Other quantitative methods may be
administratively approved by the AOGCC.
c. Results and data from any special reservoir pressure monitoring techniques, tests, or
surveys shall also be submitted as prescribed in (b) of this rule.
COs 207D.001, 311B.003, 31713.003, 329B.005, 345.002, 362A.006, 570.010
April 3, 2020
Page 5 of 12
Rule 16. GAS -CAP WATER INJECTION PROJECT
a. Water injection is authorized into Well L5-29 only and is limited to perforations within
the upper Wahoo Formation (Zone 6) between the measured depths of 13,585' and
13,634'; and
b. Injection pressures must be maintained below 0.85 psi/ft.
West Beach Oil Pool— Conservation Order No. 311B
Rule 3 Well Soacina
There shall be no restrictions to well spacing within the affected area except that no pay
may be opened in a well which is closer than 500 feet of an external property line where the
owners and landowners are not the same on both sides of the line.
Rule 7 Common Facilities and Surface Comminelina
a. Production from the West Beach Pool may be commingled on the surface with
production from other pools prior to custody transfer.
b. NGLs will be allocated to each pool based on actual gas production volumes and
NGL process simulations. Process simulations will be updated at least once per year
based on NGL samples and results reported to the AOGCC.
C. Each producing well will be tested at least once each month. Wells that have been
shut-in and cannot meet the once -monthly test frequency must be tested within five
days of startup. All available test separator capacity within the constraints imposed
by operating conditions must be utilized for well testing.
d. Optimum test duration and stabilization time will be determined on a well -by -well
basis by the operator.
Rule 9 Reservoir Pressure Monitorine
a. An Annual Pressure Surveillance Plan shall be submitted to the AOGCC in conjunction
with the Annual West Beach Oil Pool Reservoir Surveillance Report by June 151h of each
year. This plan will contain the number and approximate location of pressure surveys
anticipated for the next calendar year and, unless AOGCC orders otherwise, the plan will
be deemed approved 45 days after submission to AOGCC.
b. Data from the surveys required in (a) of this rule shall be submitted with the Annual West
Beach Oil Pool Reservoir Surveillance Report by June 15th of each year on Form 10-412.
Data submitted shall include rate, pressure, time depths, temperature and any well
condition necessary for the complete analysis of each survey. The datum for the pressure
surveys is 8,800 true vertical feet subsea. Transient pressure surveys obtained by a shut-
in build-up test, and injection well pressure fall-off test, a multirate test, or an interference
test are acceptable. Calculation of bottom -hole pressures from surface data will be
COs 20713.001, 31113.003, 317B.003, 32913.005, 345.002, 362A.006, 570.010
April 3, 2020
Page 6 of 12
permitted for water injection wells. Other quantitative methods may be administratively
approved by the AOGCC.
c. Results and data from any special reservoir pressure monitoring techniques, tests, or
surveys shall also be submitted as prescribed in (b) of this rule.
Rule 11 Administrative Action
Upon proper application, or its own motion, and unless notice and public hearing are
otherwise required, the AOGCC may administratively waive the requirements of any rule
stated herein or administratively amend this order as long as the change does not promote
waste or jeopardize correlative rights, is based on sound engineering and geoscience
principles, and will not result in an increased risk of fluid movement into freshwater aquifers.
Pt. McIntyre and Stump Island Oil Pools — Conservation Order No. 317B
Rule 4 Well Soacine
There shall be no restrictions to well spacing within the affected area except that no pay may
be opened in a well which is closer than 500 feet of an external property line where the owners
and landowners are not the same on both sides of the line.
Rule 10 Surface Commineline and Common Facilities
a. Production from the Pt. McIntyre and Stump Island Oil Pools may be commingled at
the surface with production from other pools for processing at the Lisburne Production
Center ("LPC") and production from the Pt. McIntyre Oil Pool Drillsite PM2 may be
commingled at the surface with production from other pools for processing at the
Prudhoe Bay Unit IPA Gathering Center 1 ("GC I"), prior to custody transfer.
b. Daily production from all wells will be based on empirical well performance curves
derived from 3-phase flow equations and production well test data, and will be a
function of flowing tubing pressure and gas -lift rate. The method is described within
the "Prudhoe Bay Unit (PBU) Western Satellite Production Metering Plan — Policies
and Procedures Document' dated August 1, 2002.
c. Each producing well will be tested at least once each month. Wells that have been shut
in and cannot meet the once -monthly test frequency must be tested within five days of
startup. All available test separator capacity within the constraints imposed by
operation conditions must be utilized for well testing.
d. Optimum test duration and stabilization time will be determined on a well by well basis
by the operator.
e. Wells will use the associated process facility allocation factor for oil, gas, and water.
Pt. McIntyre wells that flow to both GC 1 and LPC in the same month will use a prorated
(GC 1 and LPC) well allocation factor for oil, gas, and water.
f Natural gas liquids ("NGLs") processed at the LPC will be allocated to each pool based
on actual gas production volumes and NGL process simulations. Process simulations
will be updated at least once per year based on NGL samples and results reported to
the AOGCC.
COs 207D.001, 311B.003, 317B.003, 329B.005, 345.002, 362A.006, 570.010
April 3, 2020
Page 7 of 12
g. NGLs attributable to the PM2 to GC1 gas stream and recovered at the CGF will be
allocated by calculating the amount of separator off -gas, excluding gas lift gas,
attributable to Pt. McIntyre wells producing into GC -1. The percentage of total
separator off -gas delivered to the CGF, that is Pt. McIntyre formation gas, multiplied
by the total NGL recovery at CGF, yields the amount of NGLs to be allocated to Pt.
McIntyre.
h. Allocation data and well test data will be supplied to the AOGCC via the Annual
Reservoir Surveillance Report.
Rule 12 Reservoir Pressure Monitoring
a. An Annual Pressure Surveillance Plan shall be submitted to the AOGCC in conjunction
with the Annual Pt. McIntyre Oil Pool Reservoir Surveillance Report by June 15th of each
year. This plan will contain the number and approximate location of pressure surveys
anticipated for the next calendar year and, unless AOGCC orders otherwise, the plan will
be deemed approved 45 days after submission to AOGCC.
b. Data from the surveys required in (a) of this rule shall be submitted with the Annual Pt.
McIntyre Oil Pool Reservoir Surveillance Report by June 15`h of each year on Form 10-
412. Data submitted shall include rate, pressure, time depths, temperature and any well
condition necessary for the complete analysis of each survey. The datum for the pressure
surveys is 8,800 true vertical feet subsea. Transient pressure surveys obtained by a shut-in
build-up test, and injection well pressure fall-off test, a multirate test, or an interference
test are acceptable. Calculation of bottom -hole pressures from surface data will be
permitted for water injection wells. Other quantitative methods may be administratively
approved by the AOGCC.
c. Results and data from any special reservoir pressure monitoring techniques, tests, or
surveys shall also be submitted as prescribed in (b) of this rule.
Rule 14 Administrative Action
Upon proper application, or its own motion, and unless notice and public hearing are otherwise
required, the AOGCC may administratively waive the requirements of any rule stated herein
or administratively amend this order as long as the change does not promote waste or
jeopardize correlative rights, is based on sound engineering and geoscience principles, and will
not result in an increased risk of fluid movement into freshwater aquifers.
Rule 16 Pt. McIntyre Oil Pool Enhanced Oil Recovery Project
Injection of miscible injectant for enhanced recovery operations is approved for the Pt.
McIntyre Pool.
COs 207D.001, 31113.003, 31713.003, 32913.005, 345.002,362A.006,570.010
April 3, 2020
Page 8 of 12
Niakuk Oil Pool — Conservation Order No. 329B
Rule 3 Well Spacing
There shall be no restrictions to well spacing within the affected area except that no pay may
be opened in a well which is closer than 500 feet of an external property line where the owners
and landowners are not the same on both sides of the line.
Rule 6 Surface Commingling and Common Facilities
a. Production from the Niakuk oil pool may be commingled on the surface with production
from other pools for processing at the LPC prior to custody transfer.
b. Production from each well will be determined by the following well test allocation
methodology. Allocation data and well test data will be supplied to the AOGCC via the
Annual Reservoir Surveillance Report.
Conduct well tests to determine production rates for each well.
ii. Calculate each well's theoretical monthly production (TMP) based on well test rate(s)
and actual time on production.
iii. Sum the TMP volume for all wells in all pools.
iv. Determine an allocation factor as the ratio of the metered volume to the TMP for all
wells in all pools (i.e., metered/TMP)
Calculate each well's actual monthly production (AMP) volume as:
AMP = TMP x Allocation Factor
c. NGL's will be allocated to each pool based on actual gas production volumes and NGL
process simulations. Process simulations will be updated at least once per year based on
NGL samples and results reported to the AOGCC.
d. Each producing well will be tested at least once each month. Wells that have been shut in
and cannot meet the once -monthly test frequency must be tested within five days of
startup. All available test separator capacity within the constraints imposed by operating
conditions must be utilized for well testing.
e. Optimum test duration and stabilization time will be determined on a well by well basis
by the operator.
Rule 8 Reservoir Pressure Monitoring
a. An Annual Pressure Surveillance Plan shall be submitted to the AOGCC in conjunction
with the Annual Niakuk Oil Pool Reservoir Surveillance Report by June 15th of each year.
This plan will contain the number and approximate location of pressure surveys anticipated
for the next calendar year and, unless AOGCC orders otherwise, the plan will be deemed
approved 45 days after submission to AOGCC.
COs 207D.001, 31 1B.003, 317B.003, 329B.005, 345.002, 362A.006,570.010
April 3,2020
Page 9 of 12
b. Data from the surveys required in (a) of this rule shall be submitted with the Annual Niakuk
Oil Pool Reservoir Surveillance Report by June 15`h of each year on Form 10-412. Data
submitted shall include rate, pressure, time depths, temperature and any well condition
necessary for the complete analysis of each survey. The datum for the pressure surveys is
8,800 true vertical feet subsea. Transient pressure surveys obtained by a shut-in build-up
test, and injection well pressure fall-off test, a multirate test, or an interference test are
acceptable. Calculation of bottom -hole pressures from surface data will be permitted for
water injection wells. Other quantitative methods may be administratively approved by the
AOGCC.
c. Results and data from any special reservoir pressure monitoring techniques, tests, or
surveys shall also be submitted as prescribed in (b) of this rule.
Rule 12 Administrative Action
Upon proper application, or its own motion, and unless notice and public hearing are otherwise
required, the AOGCC may administratively waive the requirements of any rule stated herein
or administratively amend this order as long as the change does not promote waste or
jeopardize correlative rights, is based on sound engineering and geoscience principles, and will
not result in an increased risk of fluid movement into freshwater aquifers.
North Prudhoe Bay Oil Pool — Conservation Order No. 345
Rule 5 Surface ComminElin¢ and Common Facilities
a. Production from the North Prudhoe Bay Oil Pool may be commingled on the
surface with production from other pools for processing at the LPC prior to
custody transfer.
b. Production from each well will be determined by the following well test
allocation methodology. Allocation data and well test data will be supplied to the
AOGCC via the Annual Reservoir Surveillance Report.
I . Conduct well tests to determine production rates for each well.
2. Calculate each well's theoretical monthly production (TMP) based on well
test rate(s) and actual time on production.
3. Sum the TMP volume for all wells in all pools.
4. Determine an allocation factor as the ratio of the metered volume to the TMP
for all wells in all pools (i.e., metered/TMP).
5. Calculate each well's actual monthly production (AMP) volume as:
AMP = TMP x Allocation Factor
c. NGLs will be allocated to each pool based on actual gas production volumes and
NGL process simulations. Process simulations will be updated at least once per
year based on NGL samples and results reported to the AOGCC.
COs 207D.001, 31113.003, 31713.003, 32913.005, 345.002, 362A.006,570.010
April 3, 2020
Page 10 of 12
d. At a minimum, each producing well will be tested at least once each month. Wells
that have been shut in and cannot meet the once -monthly test frequency must be
tested within five days of startup.
e. Optimum test duration and stabilization time will be determined on a well -by -
well basis by the operator or, in its discretion, by the AOGCC.
Rule 7 Reservoir Pressure Monitorine
a. An Annual Pressure Surveillance Plan shall be submitted to the AOGCC in conjunction
with the Annual North Prudhoe Bay Oil Pool Reservoir Surveillance Report by June 1511
of each year. This plan will contain the number and approximate location of pressure
surveys anticipated for the next calendar year and, unless AOGCC orders otherwise, the
plan will be deemed approved 45 days after submission to AOGCC.
b. Data from the surveys required in (a) of this rule shall be submitted with the Annual North
Prudhoe Bay Oil Pool Reservoir Surveillance Report by June 151h of each year on Form
10-412. Data submitted shall include rate, pressure, time depths, temperature and any well
condition necessary for the complete analysis of each survey. The datum for the pressure
surveys is 8,800 true vertical feet subsea. Transient pressure surveys obtained by a shut-in
build-up test, and injection well pressure fall-off test, a multirate test, or an interference
test are acceptable. Calculation of bottom -hole pressures from surface data will be
permitted for water injection wells. Other quantitative methods may be administratively
approved by the AOGCC.
c. Results and data from any special reservoir pressure monitoring techniques, tests, or
surveys shall also be submitted as prescribed in (b) of this rule.
Rule 11 Administrative Action
Upon proper application, or its own motion, and unless notice and public hearing are otherwise
required, the AOGCC may administratively waive the requirements of any rule stated herein
or administratively amend this order as long as the change does not promote waste or
jeopardize correlative rights, is based on sound engineering and geoscience principles, and will
not result in an increased risk of fluid movement into freshwater aquifers.
COs 207D.001, 31 1B.003,317B.003, 329B.005, 345.002, 362A.006, 570.010
April 3, 2020
Page 11 of 12
Greater Pt. McIntyre Area — Conservation Order No. 362A.005
Rule 1: Lisburne Production Facilities
Produced fluids from the Lisburne Oil Pool, West Beach Oil Pool, North Prudhoe Bay Oil
Pool, Niakuk Oil Pool, Pt. McIntyre Oil Pool, Stump Island Oil Pool, and Raven Oil Pool may
continue to be commingled on the surface for processing at the Lisburne Production Center.
Production from each pool may be assigned on the basis of at least once monthly well tests
using procedures described in individual conservation orders for those pools or in this order.
The AOGCC may approve a different test frequency for individual wells upon application.
Raven Oil Pool — Conservation Order No. 570
Rule 3: Well Soacine
There shall be no restrictions to well spacing within the affected area except that no pay may
be opened in a well which is closer than 500 feet of an external property line where the owners
and landowners are not the same on both sides of the line.
Rule 6: Common Production Facilities and Surface Comminelina
a. Production from the Raven Oil Pool may be commingled on the surface with production
from other pools for processing at the LPC prior to custody transfer.
b. Production from each well will be determined by the following well test allocation
methodology. Allocation data and well test data will be supplied to the AOGCC via the
Annual Reservoir Surveillance Report.
i. Conduct well tests to determine production rates for each well.
ii. Calculate each well's theoretical monthly production (TMP) based on well test rate(s)
and actual time on production.
iii. Sum the TMP volume for all wells in all pools.
iv. Determine an allocation factor as the ratio of the metered volume to the TMP for all
wells in all pools (i.e., metered/TMP).
v. Calculate each well's actual monthly production (AMP) volume as:
AMP = TMP x Allocation Factor
c. NGL's will be allocated to each pool based on actual gas production volumes and NGL
process simulations. Process simulations will be updated at least once per year based on
NGL samples and results reported to the AOGCC.
d. Each producing well will be tested at least once each month. Wells that have been shut in
and cannot meet the once -monthly test frequency must be tested within five days of
startup. All available test separator capacity within the constraints imposed by operating
conditions must be utilized for well testing.
e. Optimum test duration and stabilization time will be determined on a well by well basis
by the operator.
COs 207D.001, 31113.003, 317B.003, 329B.005, 345.002,362A.006, 570.010
April 3, 2020
Page 12 of 12
Rule 7: Reservoir Pressure Monitoring
a. An Annual Pressure Surveillance Plan shall be submitted to the AOGCC in conjunction
with the Annual Raven Oil Pool Reservoir Surveillance Report by June 15th of each year.
This plan will contain the number and approximate location of pressure surveys anticipated
for the next calendar year and, unless AOGCC orders otherwise, the plan will be deemed
approved 45 days after submission to AOGCC.
b. Data from the surveys required in (a) of this rule shall be submitted with the Annual North
Raven Oil Pool Reservoir Surveillance Report by June 15" of each year on Form 10-412.
Data submitted shall include rate, pressure, time depths, temperature and any well
condition necessary for the complete analysis of each survey. The datum for the pressure
surveys is 9,850 true vertical feet subsea. Transient pressure surveys obtained by a shut-in
build-up test, and injection well pressure fall-off test, a multirate test, or an interference
test are acceptable. Calculation of bottom -hole pressures from surface data will be
permitted for water injection wells. Other quantitative methods may be administratively
approved by the AOGCC.
c. Results and data from any special reservoir pressure monitoring techniques, tests, or
surveys shall also be submitted as prescribed in (b) of this rule.
DONE at Anchorage, Alaska and dated April 3, 2020.
Jeremy M. °",,,,"",,,=w
Price
Jeremy M. Price
Chair, Commissioner
Daniel T. oau.rrsu�.awwMnr.
Seamount, Jr. mi�mioa`nvumwaroa
Daniel T. Seamount, Jr.
Commissioner
AND APPEAL
Jessie L.
Chmielowski 13:ss:`si`o"eoo�
Jessie L. Chmielowski
Commissioner
As provided in AS 31.05.080(a), within 20 days after written notice of the entry of this order or decision, or such further time
as the AOGCC grants for good cause shown, a person affected by it may file with the AOGCC an application for reconsideration
of the matter determined by it. If the notice was mailed, then the period of time shall be 23 days. An application for
reconsideration must set out the respect in which the order or decision is believed to be erroneous.
The AOGCC shall grant or refuse the application for reconsideration in whole or in part within 10 days after it is filed. Failure
to act on it within 10 -days is a denial of reconsideration. If the AOGCC denies reconsideration, upon denial, this order or
decision and the denial of reconsideration are FINAL and may be appealed to superior court. The appeal MUST be filed within
33 days after the date on which the AOGCC mails, OR 30 days if the AOGCC otherwise distributes, the order or decision
denying reconsideration, UNLESS the denial is by inaction, in which case the appeal MUST be filed within 40 days after the
date on which the application for reconsideration was filed.
If the AOGCC grants an application for reconsideration, this order or decision does not become final. Rather, the order or
decision on reconsideration will be the FINAL order or decision of the AOGCC, and it may be appealed to superior court. That
appeal MUST be filed within 33 days after the date on which the AOGCC mails, OR 30 days if the AOGCC otherwise
distributes, the order or decision on reconsideration.
In computing a period of time above, the date of the event or default after which the designated period begins to run is not
included in the period; the last day of the period is included, unless it falls on a weekend or state holiday, in which event the
period runs until 5:00 p.m. on the next day that does not fall on a weekend or state holiday.
Bernie Karl
K&K Recycling Inc.
P.O. Box 58055
Fairbanks, AK 99711
George Vaught, Jr.
P.O. Box 13557
Denver, CO 80201-3557
Gordon Severson
3201 Westmar Cir.
Anchorage, AK 99508-4336
Darwin Waldsmith
P.O. Box 39309
Ninilchik, AK 99639
Penny Vadla
399 W. Riverview Ave.
Soldotna, AK 99669-7714
Richard Wagner
P.O. Box 60868
Fairbanks, AK 99706
I'HE STATE
0fALASKA
1 IL
GOVERNOR MIKL DUNLLAVY
Alaska Oil and Gas
Conservation Commission
ADMINISTRATIVE APPROVALS
CONSERVATION ORDER NO. 83A.001
CONSERVATION ORDER NO. 207D.002
CONSERVATION ORDER NO. 311B.004
CONSERVATION ORDER NO. 317B.004
CONSERVATION ORDER NO. 329A.002
CONSERVATION ORDER NO. 3411.002
CONSERVATION ORDER NO. 345.003
CONSERVATION ORDER NO. 452.005
CONSERVATION ORDER NO. 457B.007
CONSERVATION ORDER NO. 471.010
CONSERVATION ORDER NO. 484A.005
CONSERVATION ORDER NO. 505B.003
CONSERVATION ORDER NO. 559A.002
CONSERVATION ORDER NO. 570.011
Mr. Oliver Stemicki
Well Integrity Engineer
Hilcorp North Slope LLC
P. O. Box 196612
Anchorage, AK 99519-6612
Re: Docket Numbers: CO -20-004 and CO -20-008
333 West Seventh Avenue
Anchorage, Alaska 99501-3572
Main: 907.279.1433
Fax: 907.276.7542
www.00gcc.olaska.gov
Request to amend normal operating limit for inner annulus pressure for non Lisburne
development area wells from 2,000 psig to 2,100 psig and to add an administrative approval
clause to Conservation Order No. 492
Prudhoe Bay Unit
All Oil Pools
Dear Mr. Stemicki:
By application dated February 24, 2020, Hilcorp North Slope, LLC' (HNS) applied to modify
Conservation Order No. 492 (CO 492) to raise the inner annulus (IA) normal operating limit (NOL)
reporting threshold from 2,000 psig to 2,100 psig for all wells not processed through the Lisburne
Processing Center (LPC)2. CO 492 was issued on June 26, 2003 and applied to all pools in the
' The February 24, 2020, application was submitted by BP Exploration (Alaska) Inc. (BPXA) as operator of the
Prudhoe Bay Unit (PBU) but effective on July 1, 2020, BPXA came under new ownership and was renamed HNS.
HNS is currently the operator of the PBU.
s The IA NOL for wells processed through the LPC is currently set at 2,500 prig. HNS is not seeking to modify this
at this time.
COs 83A.001, 207D.002, 311B.004, 317B.003, 329A.002,3411.002, 345.003, 452.005, 457B.006, 471.009,
484A.005,50513.003,559A.002, & 570.011
October 1, 2020
Page 2 of 4
Prudhoe Bay Unit (PBU). The order established rules for dealing with sustained casing pressure
for all producers in the PBU. Some, but not all, of the pools in the PBU area have incorporated
the rules found in CO 492 directly into its pool rules. CO 492 itself did not contain provisions to
allow it the be administratively amended, so providing public notice and opportunity to comment
was required in order to amend the order. As such CO 492 will be amended separately and this
letter will amend the individual pool rules for the PBU area oil pools.
Due to operational changes over time in the PBU, namely increases in the gas lift header pressures,
the 2,000 psig NOL for the IA that requires notification to the Alaska Oil and Gas Conservation
Commission (AOGCC) when it is exceeded is triggering numerous notifications. These
notifications do not on their own require any corrective action to be taken, but simply are a
reporting burden on the operator and the AOGCC. Increasing the NOL from 2,000 to 2,100 would
decrease the frequency of these notifications. Currently, the NOL for the IA for wells processed
through the LPC is 2,500 psig. Exceeding the 2,500 psig NOL triggers a reporting requirement,
but does not, standing alone, require corrective action. Another limit that is currently in place, and
is not being changed by this action, is a pressure limitation of 45% of the casing's burst pressure
rating. Exceeding the 45% pressure limitation requires that corrective action to be taken.
Increasing the reporting threshold from 2,000 psig to 2,100 psig for the wells that are not processed
at the LPC will eliminate many unnecessary notifications for wells where notification was
triggered by the gas lift system pressure instead of an actual problem with the well that might
indicate loss of containment.
Increasing the IA NOL from 2,000 psig to 2,100 psig for production wells that are not processed
at the LPC is based on sound engineering and geoscience principles.
Now therefore it is ordered that the text below shall replace the text in the specified rules in the
following orders:
Conservation Order
Oil Pool
Rules being replaced
207D
Lisburne
15
457B
Aurora
11 and 123
484A
Polaris
11
505B
Schrader Bluff
11
559A
Put River
10
570
Raven
12
In the current CO 457B, the pool rules for the Aurora Oil Pool, Rule 11 contains paragraphs a. through f. of the
annular pressure rules and Rule 12 contains the definitions in paragraph g. of the annular pressure rules. Paragraph g.
is a part of the revised Annular Pressure of Production Wells shown here and thus Rule 12 in CO 457B is being
eliminated.
COs 83A.001, 207D.002, 311B.004, 317B.003, 329A.002, 3411,002, 345.003, 452.005, 457B.006, 471.009,
484A.005, 505B.003, 559A.002, & 570.011
October 1, 2020
Page 3 of 4
And be added as the new rule indicated in the following orders:
Conservation Order
Oil Pool
Added rule
83A
Kuparuk River
9
311B
West Beach
14
317B
Pt McIntyre and Stump Island
17
329A
Niakuk
13
341I
Prudhoe Oil Pool
22
345
North Prudhoe Bay
12
452
Midnight Sun
15
471
Borealis
11
Annular Pressure of Production Wells
a. At the time of installation or replacement, the operator shall conduct and document a
pressure test of tubulars and completion equipment in each production well that is sufficient
to demonstrate that planned well operations will not result in failure of well integrity,
uncontrolled release of fluid or pressure, or threat to human safety.
b. The operator shall monitor each production well daily to check for sustained pressure,
except if prevented by extreme weather conditions, emergency situations, or similar
unavoidable circumstances. Monitoring results shall be made available for Commission
inspection.
c. The operator shall notify the Commission within three working days after the operator
identifies a well as having (1) sustained inner annulus pressure that exceeds 2500 psig for
wells processed through the Lisburne Processing Center and 2100 psig for all other
production wells, or (2) sustained outer annulus pressure that exceeds 1000 psig.
d. The Commission may require the operator to submit in an Application for Sundry
Approvals (Form 10-403) a proposal for corrective action or increased surveillance for any
production well having sustained pressure that exceeds a limit set out in paragraph (c) of
this rule. The operator shall give the Commission notice consistent with the requirements
of Industry Guidance Bulleting 10-OIA of the testing schedule to allow the Commission to
witness the tests.
e. If the operator identifies sustained pressure in the inner annulus of a production well that
exceeds 45% of the burst pressure rating of the well's production casing for inner annulus
pressure, or sustained pressure in the outer annulus that exceeds 45% of the burst pressure
rating of the well's surface casing for outer annulus pressure, the operator shall notify the
Commission within three working days and take corrective action. Unless well conditions
require the operator to take emergency corrective action before Commission approval can
be obtained, the operator shall submit in an Application for Sundry Approvals (Form 10-
403) a proposal for corrective action. The operator shall give the Commission sufficient
notice of the testing schedule to allow the Commission to witness the tests.
COs 83A.001, 207D.002, 31 16.004, 317B.003, 329A.002, 3411.002, 345.003, 452.005, 457B.006, 471.009,
484A.005, 505B.003, 559A.002, & 570.011
October 1, 2020
Page 4 of 4
f. Except as otherwise approved by the Commission under (d) or (e) of this rule, before a
shut-in well is placed in service, any annulus pressure must be relieved to a sufficient
degree (1) that the inner annulus pressure at operating temperature will be below 2000 psig,
and (2) that the outer annulus pressure at operating temperature will be below 1000 psig.
However, a well that is subject to (c) but not (e) of this rule may reach an annulus pressure
at operating temperature that is described in the operator's notification to the Commission
under (c) of this rule, unless the Commission prescribes a different limit.
g. For purposes of this rule,
1. "inner annulus" means the space in a well between tubing and production casing;
2. "outer annulus" means the space in a well between production casing and surface
casing;
3. "sustained pressure" means pressure that (A) is measurable at the casing head of an
annulus, (B) is not caused solely by temperature fluctuations, and (C) is not pressure
that has been applied intentionally.
DONE at Anchorage, Alaska and dated October 1, 2020.
Jeremy D51mY ned by
JeleDate 10201 ODI
M. Price 135g]9-0a'Do'
Jeremy M. Price
Chair, Commissioner
Daniel T.Digitally signed by
Wini xamoem,J,.
Searnount, Jr. 11`'20101 o01
12 Deals -0e 00'
Daniel T. Seamount, Jr
Commissioner
Digitally signed by
Jessie L. Jessie L. Chmielowski
Chmielowski 1`2020.10.01
;2:12:07-09.00'
Jessie L. Chmielowski
Commissioner
As provided in AS 31.05.080(x), within 20 days after written notice of the entry of this order or decision, or such further time
as the AOGCC grants for good cause shown, a person affected by it may file with the AOGCC an application for reconsideration
of the matter determined by it. If the notice was mailed then the period of time shall be 23 days. An application for
reconsideration must set out the respect in which the order or decision is believed to be erroneous.
The AOGCC shall grant or refuse the application for reconsideration in whole or in part within 10 days after it is filed. Failure
to act on h within 10 -days is a denial of reconsideration. If the AOGCC denies reconsideration, upon denial, this order or
decision and the denial of reconsideration are FINAL and may be appealed to superior court. The appeal MUST be filed within
33 days after the date on which the AOGCC mails, OR 30 days if the AOGCC otherwise distributes, the order or decision
denying reconsideration, UNLESS the denial is by inaction, in which case the appeal MUST be filed within 40 days after the
date on which the application for reconsideration was filed.
If the AOGCC grants an application for reconsideration, this order or decision does not become final. Rather, the order or
decision on reconsideration will be the FINAL order or decision of the AOGCC, and it may be appealed to superior court. That
appeal MUST be filed within 33 days after the date on which the AOGCC mails, OR 30 days if the AOGCC otherwise
distributes, the order or decision on reconsideration.
In computing a period of time above, the date of the event or default after which the designated period begins to run is not
included in the period; the last day of the period is included, unless it falls on a weekend or state holiday, in which event the
period runs until 5:00 p.m. on the neat day that does not fall on a weekend or state holiday.
Bernie Karl Gordon Severson Richard Wagner
K&K Recycling Inc. 3201 Westmar Cir. P.O. Box 60868
P.O. Box 58055 Anchorage, AK 99508-4336 Fairbanks, AK 99706
Fairbanks, AK 99711
George Vaught, Jr. Darwin Waldsmith
P.O. Box 13557 P.O. Box 39309
Denver, CO 80201-3557 Ninilchik, AK 99639
16
J(ombie, Jody J (cED)
From:
Rixse, Melvin G (CED)
Sent:
Wednesday, June 10, 2020 2:27 PM
To:
Sternicki, Oliver R
Cc:
Colombie, Jody 1 (CED)
Subject:
FW: June 25 hearing to amend 4 CO's
Attachments:
CO -20-008 Public Hearing Notice.pdf, RE: CO -20-008
This is a clarification email to BPXA, Oliver Sternicki, that the AOGCC interpretation of any development well going
through Lisburne Production Center, whether on gas lift or noturalflow, will be allowed 2500 psig sustained inner
annulus pressure before reporting is required.
CO -20-008 as written should be fine. We will then administratively amend the COs per the notice.
Mel Rixse
Senior Petroleum Engineer (PE)
Alaska Oil and Gas Conservation Commission
907-793-1231 Office
907-223-3605 Cell
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 area n unintended recipient of this a -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 Mel Rixse at (907-793-1231) or ( Melvin. Rixsepa Iask a govl.
cc. Jody Colombie
From: Colombie, Jody J (CED)
Sent: Wednesday, June 10, 2020 8:59 AM
To: Chmielowski, Jessie L C (CED) <jessie.chmielowskiPalaska eov>
Cc: Rixse, Melvin G (CED) <melvin.rixsePalaska eov>
Subject: RE: June 25 hearing to amend 4 CO's
No one has requested a hearing.
Mel: Do you vote to vacate?
Jody
From: Chmielowski, Jessie L C (CED) <iessie.chmielowski(caalaska gov>
Sent: Wednesday, June 10, 2020 8:57 AM
To: Colombie, JodyJ (CED) <jody.colombieRaalaska ftov>
Cc: Rixse, Melvin G (CED) <melvin.rixse @alaska Rov>
Subject: June 25 hearing to amend 4 CO's
Hi Jody,
Were there any requests to hold the hearing that's scheduled for June 25? Wondering if we can vacate and
administratively amend the CO's?
Co amble, Jody J (CED)
From:
Sternicki, Oliver R <Oliver.Sternicki@bp.com>
Sent:
Tuesday, June 2, 2020 3:43 PM
To:
Rixse, Melvin G (CED)
Cc:
Lau, Jack
Subject:
RE: CO -20-008
Mel,
I was doing some work on the NOL increase and noticed something that might need slightly more clarification.
The operator shall notify the AOGCC within three working days after the operator
identifies a development well as having (a) sustained inner annulus pressure that exceeds
2500 psig for wells with supplied gas lift pressure from the Lisburne Processing Center
and 2100 psig for all other development wells, or (b) sustained outer annulus pressure that
exceeds 1000 psig.
The issue is that this wording could be interpreted as just applying to the gas lifted produces at LPC and excludes the
natural flow producers at that facility and in the GPMA area. There are currently 69 wells this applies to. This part
should read:
...for wells with supplied gas lift pressure from the Lisburne Processing Center or wells processed through the Lisburne
Processing Center...
Let me know what you think,
Oliver Sternicki
YY
p)ubal rw16a ory�rJ,al3on
Sr. Well Integrity Engineer
BP Exploration Alaska
Cell: 1 (907) 350 0759
oliver.stemicki(@bP.com
From: Rixse, Melvin G (CED) <melvin.rixse@alaska.gov>
Sent: Friday, May 15, 2020 4:31 PM
To: Sternicki, Oliver R <Oliver.Sternicki@bp.com>
Subject: FW: CO -20-008
From: Colombie, Jody 1 (CED) <jodv.colombieCcDalaska.gov>
Sent: Friday, May 15, 2020 3:16 PM
To: AOGCC_Public_Notices <AOGCC Public Notices @list state ak us>
Subject: [AOGCC_Public_Notices] CO -20-008
Docket Number: CO -20-008
Prudhoe Bay Field, All Pools
Jodv.L Colonbie
Special Assistant
Alaska Oil and Lias Conservation Commission
333 West 7h Avenue
Anchorage, AK 99501
(907) 793-1221 Direct
(907) 2 76- 7542 Far
List Name: AOGCC Public NoticesCa list.state ak.us
You subscribed as: rvan.danielPbp.com
Unsubscribe at: http://list.state.ak.us/mailman/options/aogcc public notices/rvan.daniel*/`40bp.com
STATE OF ALASKA
ADVERTISINGNOTICE
ORDER
TO PUBLISHER
SUBMITINVOICE SHOWING ADVERTISING ORDER NO., CERTIFIED
APFIDAVITOFPUBLTT�
AGTDCOPYOF
ADVERTISMENT
ADVERTISING ORDER NUMBER
AO-08-20-024
FROM: AGENCY CONTACT:
Jody Colombie/Samantha Carlisle
Alaska Oil and Gas Conservation Commission DATE OF A.O.AGENCY PHONE:
333 West 7th Avenue 5/15/2020 907 279-1433
Anchorage, Alaska 99501
DATES ADVERTISEMENT REQUIRED:
COMPANY CONTACT NAME:
PHONE NUMBER: ASAP
FAX NUMBER:
907 276-7542
TO PUBLISHER:
Anchorage Daily News LLC
SPECIAL INSTRUCTIONS:
PO Box 140147
Anchorage, Alaska 99514-0174
TYPE OF ADVERTISEMENT:
(✓ LEGAL f- DISPLAY r CLASSIFIED f- OTHER (Specify below) i.
DESCRIPTION PRICE
CO-20-008
Initials of who prepared AO:
Alaska Non -Taxable 92-600185
SUBMIT INVOICE SHOWING ADVERTTs"r
ORDER NO., CERTIFIED AFFIDAVITOF
PUBLICATION WI'rHATTACHED COPV OF
ADVERnsMENr To:
AOGCC
333 West 7th Avenue
Anchorage, Alaska 99501
Pae 1 of I
Total of
All Pages $
REF Tye Number
Amount Date Comments
I PVN IVCO21795
z Ao AO-08-20-024
3
4
FIN AMOUNT SY Act. Template PGM LGR Object FY DIST LIQ
1 20 AOGCC 3046 20
2
3-
4
5
Purch n u ri Title: Pnrchming
nn A
Authority's Signature Telephone Number
.O. a and receiving agency name must appear mall invoices and documents relating to this purchase.
e stale is registered for tax free transactions under Chapter 32, IRScode. Registration number 92-73-0006 K. Items are for the exclusive use of the slate and
of for resale.
DISTRIBUTION:
Division FircaVOriginal AO
Copies: Publisher (taxed), Division Fiscal, Receiving
Form: 02-901
Revised: 5/21/2020
Notice of Public Hearing
STATE OF ALASKA
ALASKA OIL AND GAS CONSERVATION COMMISSION
Re: Docket Number: CO -20-008
Prudhoe Bay Field, All Pools
BP Exploration Alaska, Inc., by application received February 24, 2020, requests the Alaska Oil and Gas
Conservation Commission (AOGCC) revise Rule 3 of Conservation Orders 317, 505, 559 and 570 to
include the following language:
The operator shall notify the AOGCC within three working days after the operator
identifies a development well as having (a) sustained inner annulus pressure that exceeds
2500 psig for wells with supplied gas lift pressure from the Lisburne Processing Center
and 2100 psig for all other development wells, or (b) sustained outer annulus pressure that
exceeds 1000 psig.
In addition, on its own motion AOGCC proposes to add the language that "unless notice
and public hearing are otherwise required, upon proper application the AOGCC may
administratively amend this order as long as the change does not promote waste or
jeopardize correlative rights, is based on sound engineering and geoscience principles, and
will not result in an increased risk of fluid movement into freshwater."
The AOGCC has tentatively scheduled a public hearing on this application for June 25, 2020, at 10:00 a.m.
at 333 West 7°i Avenue, Anchorage, Alaska 99501. To request that the tentatively scheduled hearing be
held, a written request must be filed with the AOGCC no later than 4:30 p.m. on June 5, 2020.
Due to health mandates issued as a result of the covid-19 virus, if a hearing is requested, the hearing will
be held telephonically. Those desiring to participate or be present at the hearing should call 1-800-315-6338
and, when instructed to do so, enter the code 14331. Because the hearing will start at 10:00 a.m., the phone
lines will be available starting at 9:45 am. Depending on call volume, those calling in may need to make
repeated attempts before getting through.
If a request for a hearing is not timely filed, the AOGCC may consider the issuance of an order without a
hearing. To learn if the AOGCC will hold the hearing, call (907) 793-1221 after June 7, 2020.
In addition, written comments regarding this application may be submitted to the AOGCC, at 333 West 7's
Avenue, Anchorage, Alaska 99501. Comments must be received no later than 4:30 p.m. on June 22, 2020,
except that, if a hearing is held, comments must be received no later than the conclusion of the June 25,
2020 hearing.
If, because of a disability, special accommodations may be needed to comment or attend the hearing, contact
the AOGCC's Special Assistant, Jody Colombie, at (907) 793-1221, no later than June 20, 2020.
Jeremy M. Price
Chair, Commissioner
Bernie Karl
K&K, Recycling Inc.
P.O. Box 58055
Fairbanks, AK 99711
George Vaught, Jr.
P.O. Box 13557
Denver, CO 80201-3557
Gordon Severson
3201 Westmar Cir.
Anchorage, AK 99508-4336
Darwin Waldsmith
P.O. Box 39309
Ninilchik, AK 99639
Richard Wagner
P.O. Box 60868
Fairbanks, AK 99706
14
n
BP Exploration (Alaska) Inc. W�44p
Attn: Well Integrity Coordinator, PRB-20.
Post Office Box 196612tt
.
Anchorage, Alaska 99519-6612
February 24, 2020
Mr. Jeremy Price
Alaska Oil and Gas Conservation Commission
333 West 7th Avenue
Anchorage, Alaska 99501
Subject: Request to amend Conservation Order No. 492 rule 3(a) and 6(a).
Dear Mr. Price,
BP Exploration (Alaska) Inc. requests an amendment to Conservation Order No. 492 rule
3(a) and 6(a) such that current notification and pressure limits are changed from 2000psi
to 2100 psi for wells not processed through the Lisburne Processing Center.
Current maximum gas lift header pressure in the Prudhoe Bay field for wells not
processed through the Lisburne Processing Center regularly exceeds 2000psi. The field -
wide IA (Inner Annulus) NOL (Normal Operating Limit) is set at 2000 psi for non -Lisburne
development wells, excluding jet pump wells. Beginning in 2015 BPXA began installation
of wireless digital annulus pressure gauges on all wells, this was completed in late 2019.
Due to the increased accuracy of the annulus pressure readings and realtime
monitoring/alerting capability, board operators are now very frequently responding to false
alerts of IA NOL excursions on gas lifted wells due to gas lift header pressure exceeding
2000 psi, not sustained casing pressure as intended. BPXA requests that rule 3(a) and
6(a) be changed from 2000psi to 2100 psi (excluding jet pumps) for wells not processed
through the Lisburne Processing Center to help minimize bo�rd and well pad operators
responding to false alerts.
If you have any questions, please call me at 564-5430.
Sincerely,
Ryan Daniel
BPXA Well Integrity Team Lead
Attachments:
Technical Justification
Technical Justification for Conservation Order No. 492 Amendment
February 24, 2020
History and Status:
Gas lift header pressure at many of the drill sites and pads in the Prudhoe Bay field
(excluding wells processed through the Lisburne Process Center) regularly exceeds the
2000 psi IA NOL set for development wells. Gas lift compressor outlet pressures are
commonly set at 2100 psi. Historical gas lift pressures can be seen in Figure 1 & 2 for
reference. The legacy IA NOL value of 2000 psi was set to remain compliant with
Conservation Order No. 492 rule 3(a) and 6(a).
Prior to the installation and monitoring of wireless annulus pressure gauges this was not
as large of a problem due to one IA pressure read being recorded via mechanical
gauge daily per well. If a pressure read exceeded the 2000 psi NOL it was reported to
Well Integrity and evaluated to determine if the excursion was SCP or not.
Currently all wells in the Prudhoe Bay field have the inner annulus pressures monitored
in real-time by either the EOA or WOA production center board operators. The board
operators are notified with an alert when the IA pressure of a well exceeds the set NOL
value of 2000 psi. This ensures a timely notification and response to any potential
excursion event. With the utilization of the wireless annulus pressure gauge alerting it
has become an ongoing problem where wells supplied with gas lift pressure are
regularly setting off alerts due to the gas lift supply pressure exceeding the 2000 psi
NOL and not due to SCP as intended. This excessive alerting has the potential to
desensitize workers to possible hazardous occurrences.
Increasing IA NOL from 2000 psi to 2100 psi for development wells would eliminate the
majority of these false NOL excursion alerts and allow resources to be more focused on
response and evaluation of probable SCP events. This increase of 100 psi to the IA
NOL is well within the design parameters of development wells across the Prudhoe Bay
field.
All development wells are included in this request in an effort to reduce the complexity
of the IA NOL change. While non gas lifted wells are not subject to the same false
alerts there is an increased risk of operating the field with IA NOLs varying for different
types of wells. The use of gas lift on development wells, including natural flow
producers, is continually changing, some require gas lift for kick off purposes only while
others need constant gas lift. Gas lift usage may also change as a well ages depending
on depletion or may change due to well work such as add pert/ reperf interventions.
The tracking of these dynamic changes would be very difficult and the continual
changing of NOL between 2000 psi and 2100 psi for individual wells in multiple data
and control systems would greatly increase the complexity and management of NOLs
across the field. This inconsistency in IA NOLs would be difficult for field personnel to
continually keep track of and would reduce their effectiveness in identification of
potential SCP events and would potentially result in misreporting of excursions. The IA
NOL increase would not reduce the ability to identify SCP excursions in non -gas lifted
wells. BPXA currently monitors development wells for minimum tubing by IA differential
pressure thresholds as an indicator of communication. In addition to this SITP of non -
gas lifted wells is in excess of 2100 psi, which if seen on the IA would indicate a loss of
tubing integrity and would flag as SCP. Based on this it is requested to increase the IA
NOL for all development wells (excluding jet pump wells and those processed through
the Lisburn Processing Center) to 2100 psi.
Figure 1- EOA DS Gas Lift Header Pressure
EOA Gas Lift Pressure
I..
3/1L]J13 5/1/3.3 fi/}MIDIS B/9/ZOIS 9/EUW35 !!Ilt/ZOIS 1/6/.016
Figure 2 WOA Pad Gas Lift Header Pressure
WOA Gas Lift Pressure.
I,aoom
3/ll/M13
3/t/3035 6/}Ulm3 8/9/1013 9RbID13 11/ll/$ms 1/6/l.6 l/}yIDl6
Ogle
B? Exploration (Alaska) Inc.
900 East Benson Boulevard
P.O. Box 196612
Anchorage, Alaska 99519-6612
(907) 561 -511 1
February 20, 2020
Via USPS and Electronic Delivery
Jeremy Price
Commission Chair
Alaska Oil and Gas Conservation Commission
333 West 7`s Avenue, Suite 100
Anchorage, AK 99501
0
Re: Application for Administrative Approval
Conforming PBU GPMA Pool Rules for Consistency
Amendments to Conservation Orders: 207C, Rules 3, 9c, IOa-f,16c; CO 317B Rules 4,
1Ob,d, IOg, IOh, IOi, l Oj, 12a -f, 16b; CO 329A Rules 3, 6b,d, f -j, 8a -f, e; CO 311B
Rules 3, 7b, d, f -k; 9a -f; CO 345 Rules 5b,d,f-i, 7a -f; CO 362A.005 Rule 1; CO 570
(Corrected) Rule 3; AA No. 570.002; CO 570.004 Rule 6 b, d, f -i; , I Of governing the
development and operation of the Lisburne, Pt. McIntyre, Niakuk, West Beach, North
Prudhoe, and Raven Oil Pools
Dear Chair Price,
BP Exploration (Alaska) Inc. (BPXA), as the operator of the Prudhoe Bay Unit (PBU),
respectfully requests that the commission administratively approve amendments described in
this application to the referenced Conservation Orders. Each of these pools is in the Greater Pt.
McIntyre Area (GPMA) in the PBU. This administrative relief is sought under Rule 17 of CO
207C and its equivalents in the other referenced Conservation Orders.
The amendments are proposed with the goal of bringing more efficiency to the management of
these reservoirs through achieving as much rule consistency as possible, while still honoring the
unique aspects of each pool. More consistent rules will also result in easier monitoring of
compliance for the Commission. The proposed changes are in line with recent Commission -
approved changes to CO 341F (January, 2018) for the Prudhoe Oil Pool and for changes made to
COs 452, 457B, 471, 484A, 505B for the Aurora, Borealis, Orion, Polaris and Midnight Sun Oil
Pools (May 29, 2019). With the GPMA Plan Year running April 1 — March 31, BPXA
RECEIVED
FEB 21 2020
AOGCC
respectfully requests adjudication by April 1, 2020 in order that the entire next plan year may be
under the new regulations.
In overview*, BPXA seeks simplification and consistency for the following:
• Well Spacing. BPXA proposes there should be no restrictions as to well spacing except that no
pay shall be opened in a well closer than 500 feet to the boundary of the affected area, unless the
owner and landowner are the same on both sides of the line. This is consistent with the
language for the Prudhoe Oil Pool except for the "same landowner" clause which represents an
improvement to the POP rule.
• Pressure Data 10-412 Report. BPXA proposes to eliminate the monthly (Lisburne) to
quarterly (Pt. McIntrye, Niakuk, West Beach) to unspecified (N Prudhoe and Raven)
reporting requirement by allowing the operator to annually nominate in the ASR (or if no
ASR is required to annually report) the number and approximate locations of pressure
surveys, with the AOGCC having 30 days to register an issue; if none is raised the
proposed number will take effect. The pressure data report would be included in the
ASR with that report replacing Lisburne's requirement for an annual meeting to review
pressure monitoring requirements and to discuss plans for reservoir management. All
data necessary for analysis of each survey need not be submitted with the report but must
be available to the commission upon request. This is the current regulation for the POP.
• It is proposed to remove the requirement to determine water volumes, annual API gravity,
and annual gas samples from each non -gas lifted producing well in the Surface
Commingling and Common Facilities rules as our reservoir recovery mechanisms are not
changing. The need for data of this kind on such a frequency is not justified. If the
operator were to change the recovery mechanism then it might be prudent to monitor
each well in such a manner but barring that, BPXA does not see this data guiding
reservoir management decisions.
• Allocation Process Reviews. BPXA proposes to formally eliminate this requirement.
Instead, this requirement can be replaced with an Allocation Factor report in the Annual
Surveillance Report (ASR).
• Well Test data Report. BPXA proposes to formally eliminate this requirement for all
GPMA pools that currently have it and replace it with the Allocation Factor report in the
ASR, as provided for other BP operated pools in AOGCC Administrative Approval (AA)
(Docket # CO -15-013) dated 1/7/16. That AA waived the requirement to submit monthly
reports of daily allocation and test data for a number of PBU pools. It covered some but
not all of the GPMA Pools.
• Well Test Frequency. BPXA proposes to go from two to one per month for the GPMA
pools. This will be in alignment with the other PBU pools.
*Items that pertain solely to individual pools are: proposed elimination of the Lisburne Oil Pool
Gas -Oil Ratio Test requirement, proposed upward revision of Injection Gradient and elimination
of injection rate limit for the Lisburne Gas Cap Water Injection Project, and proposed
elimination of the Pt. McIntyre Oil Pool EOR Project performance report. Rationale behind
these "one-off' items is provided in Table 1, a spreadsheet containing all the proposed changes
across the six GPMA pools.
2
The specific requests are detailed on an individual pool basis below using the convention of
brackets [ ] for deletions of existing order words; use of underline denotes proposed new text.
Only those rules and paragraphs within rules that have proposed changes are included below.
Lisburne Oil Pool Conservation Order 207C
There shall be no restrictions as to well spacing except that no fThe well spacing unit shall be
one producing well per governmental quarter section. No] pay shall be opened [in a well closer
than 1,000 feet to the pay opened in another well or opened] in a well which is closer than 500
feet to the boundary of the affected area.
a) Between 90 and 120 days after regular production commences and each six
months thereafter a gas -oil ratio test will be taken on each well for as long as it
produces oil;
b) The gas -oil ratio tests will be for a minimum of four hours and shall be taken at
the normal producing rate of the well; and
c) The results of the gas -oil ratio tests will be reported on Form 10-409, Gas -Oil
Ratio Test and will be submitted in January and July of each year.]
�S =1129M. . t
a) [All new wells shall have an acceptable pressure survey, as defined in part (c),
taken prior to regular production or injection.
b) One pressure survey per producing drillsite per year shall be taken. Pressure
surveys from producing or water and gas injection wells may be used for this
pressure requirement. Pressure surveys covered in section (a) may be substituted
for a drillsite pressure.
c) Acceptable pressure surveys include static surveys, RFT/FMT, pressure buildup
and falloff tests, and multi -rate pressure transient tests in production or injection
wells. Other quantitative methods may be administratively approved by the
Commission.
d) The pressure datum for the Lisburne Oil Pool is 8900 feet subsea. The
Commission may administratively amend this datum or create an additional
datum when more information is available on the reservoir.
e) Data from the pressure surveys, along with additional pressure data obtained
through proper management of the reservoir, shall be filed on form 10-412 by the
last day of the month following the month that the pressure survey was obtained.
Submitted pressure data shall include other information as necessary such as rate,
time, depth, temperature, and well conditions to allow for a complete analysis of
the pressure survey.
f) The operator shall schedule an annual meeting with the Commission to review
the pressure monitoring program and discuss future plans for reservoir
management.]
3
a. An Annual Pressure Surveillance Plan shall be submitted to the AOGCC in conjunction
with the Annual Lisburne Oil Pool Reservoir Surveillance Report by June 15`h of each
year. This plan will contain the number and approximate location of pressure surveys
anticipated for the next calendar year, and it will be subject to approval by the AOGCC
by July 15 of that year.
b. Data from the surveys required in (a) of this rule shall be submitted with the Annual
Lisburne Oil Pool Reservoir Surveillance Report by June 15 of each year on form
10-412. Data submitted shall include rate pressure time depths temperature and
any well condition necessary for the complete analysis of each survey. The datum for
the pressure surveys is 8,900 true vertical feet subsea Transient pressure surveys
obtained by a shut-in buildup test an injection well pressure fall-off test a multirate
test, or an interference test are acceptable. Calculation of bottom -hole pressures from
surface data will be permitted for water injection wells Other quantitative methods
may be administratively approved by the AOGCC
c. Results and data from any special reservoir pressure monitoring techniques tests or
surveys shall also be submitted as prescribed in (b) of this rule
Rule 16, GAS -CAP WATER INJECTION PROJECT
[b The Well L5-29 injection rate is limited to 20,000 barrels of water injected per day;]
c.Injection pressures must be maintained below 0.85 psi/ft.
Pt. McIntyre Oil Pool Conservation Order 317B
Rule 4 Well Soacine
There shall be no restrictions as to well spacing except that no [The spacing unit
shall be one producing well per 40 acres or quarter -quarter governmental
section. No] pay shall be opened in a well closer than 500 feet to the boundary
of the affected area.
Rule 10 Surface Commineline and Common Facilities
b. Production from each well will be determined by the following well test allocation methodology.
Allocation data and well test data will be supplied to the Commission [quarterly in both computer file
and report formats.] via the Annual Reservoir Surveillance Report.
No changes to the remainder of b (sub paragraphs).
d. Each producing well will be tested at least [twice] once each month. Wells that have been shut
in and cannot meet the [twice] once monthly test frequency must be tested within five days of
startup. All available test separator capacity within the constraints imposed by operating conditions
must be utilized for well testing.
e. The operator shall submit a review of pool production allocation factors and
0
issues over the prior year with the annual reservoir surveillance report and
retain electronic file(s) containing daily allocation data and daily test data for a
minimum of five years. Data shall be presented on a monthly basis reported
annually in the ASR.
[1 Of) API gravity will be determined for each producing well annually by an API/MPMS
approved method.
I Og) Gas samples will be taken and analyzed for composition from each non -gas lifted producing
well yearly.
10h) Quarterly allocation process reviews will be held with the Commission.
10i) This rule may be revised or rewritten after an evaluation period of at least one year.]
Ia. Prior to regular production, a pressure survey shall be taken on each well to determine
the reservoir pressure.
b. A minimum of one bottom hole pressure survey per producing governmental section
shall be run annually. The surveys in part a. of this rule may be used to fulfill the
minimum requirements
c. The datum for all surveys is 8800' TVDss.
d. Pressure surveys will be either a pressure buildup, pressure falloff, RFT, or
static bottom hole pressure after the well has been shut in for an extended period.
e. The pressure surveys will be reported to the Commission quarterly. Commission
form 10-412, Reservoir Pressure Report, shall be used to report results from these
surveys. All data necessary for complete analysis of each survey need not be submitted
with the form 10-412 but must be submitted upon request.
f. Results and data from any special reservoir pressure monitoring techniques,
tests, or surveys also shall be submitted in accordance with part e. of this rule.]
year. This plan will contain the number and approximate location of pressure surveys
anticipated for the next calendar year, and it will be subject to approval by the AOGCC by
July 15 of that year.
b.Data from the surveys required in (a) of this rule shall be submitted with the Annual Pt
McIntyre Oil Pool Reservoir Surveillance Report by June 15 of each year on forth 10-
412. Data submitted shall include rate, pressure, time depths, temperature and any well
condition necessary for the complete analysis of each survey. The datum for the pressure
surveys is 8,800 true vertical feet subsea. Transient pressure surveys obtained by a shut-
in buildup test, an injection well pressure fall-off test, a multirate test, or an interference
5
test are acceptable. Calculation of bottom -hole pressures from surface data will be
Permitted for water injection wells Other quantitative methods may be administratively
approved by the AOGCC.
c.Results and data from any special reservoir pressure monitoring techniques tests or
surveys shall also be submitted as prescribed in (b) of this rule
Rule 16 Pt McIntyre Oil Pool Enhanced Oil Recovery Project
[b. An annual report must be submitted to the Commission detailing performance of the PMOP
Enhanced Oil Recovery Project and outlining compositional information for the current miscible
injectant necessary to maintain miscibility under anticipated reservoir conditions. The report
should be submitted in conjunction with the PMOP Annual Reservoir Report.]
Niakuk Oil Pool Conservation Order 329
[Upon application ofthe operator, the Commission may administratively approve the drilling of
any well to a bottom hole location greater than 500 lineal feet from the external boundary of the
affected area. No well bore may be open to the Niakuk oil pool within 500 feet of the external
boundary of the affected area nor within 1000 feet of another well capable of producing from
thesamepool.]
There shall be no restrictions as to well spacing except that no pay shall be opened in a well
closer than 500 feet to the boundary of the affected area.
Rule 6 Surface Commingling and Common Facilities
b. Production from each well will be determined by the following well test allocation methodology.
Allocation data and well test data will be supplied to the Commission [monthly in both computer
file and report formats.] via the Annual Reservoir Surveillance Report.
No changes to the remainder of b (sub paragraphs).
d.Each producing well will be tested at least [twice] once each month. Wells that have been
shut in and cannot meet the [twice] once monthly test frequency must be tested within five
days of startup. All available test separator capacity within the constraints imposed by operating
conditions must be utilized for well testing.
[f.Water volumes will be determined by API/MPMS approved methods, or the use of industry
proven, on-line water cut measurement devices approved by the Commission.
g.API gravity will be determined for each producing well annually by an API/MPMS
approved method.
h.Gas samples will be taken and analyzed for composition from each non gas lifted
F
producing well yearly.
j.Quarterly allocation process reviews will be held with the Commission.
j.This rule may be revised or rewritten after an evaluation period of at least one year.]
Rule 8 Reservoir Pressure Monitoring
a. [Prior to regular production, a pressure survey shall be taken on each well to determine
the reservoir pressure.
b. A minimum of one bottom hole pressure survey per producing governmental section shall
be obtained annually. The surveys in part'a' of this rule may be used to fulfill the
minimum requirements.
c. The datum for all surveys is 9200' TVDss.
d. Pressure surveys will be either a pressure buildup, pressure falloff, RFT, or static bottom hole
pressure after the well has been shut in for an extended period.
e. The pressure surveys will be reported to the Commission quarterly on form 10412, Reservoir
Pressure Report. All data necessary for complete analysis of each survey need not be
submitted with the form 10-412 but must be submitted upon request.
f Results and data from any additional reservoir pressure tests, surveys or
special monitoring techniques shall be submitted in accordance with part'e'
ofthis rule.]
This plan will contain the number and approximate location of pressure surveys anticipated
for the next calendar year, and it will be subject to approval by the AOGCC by July 15 of
that year.
b. Data from the surveys required in (a) of this rule shall be submitted with the Annual
Niakuk Oil Pool Reservoir Surveillance Report by June 15 of each year on form 10-412.
Data submitted shall include rate, pressure, time depths, temperature, and any well
condition necessary for the complete analysis of each survey. The datum for the pressure
surveys is 8,800 true vertical feet subsea. Transient pressure surveys obtained by a shut-
in buildup test, an injection well pressure fall-off test, a multirate test, or an interference
test are acceptable. Calculation of bottom -hole pressures from surface data will be
permitted for water injection wells. Other quantitative methods may be administratively
approved by the AOGCC.
7
c. Results and data from any special reservoir pressure monitoring techniques tests or
surveys shall also be submitted as prescribed in (b) of this rule
West Beach Oil Pool Conservation Order 311B
Rule 3 Well Spacin¢
There shall be no restrictions as to well spacing except that no nay shall be opened in a well
closer than 500 feet to the boundary of the affected area
[Statewide 160 -acre drilling units are in effect until such time as data or circumstances
warrant the Commission to approve a change.]
Rule 7 Common Facilities and Surface Commin lin¢
[(b) Production from each pool will be determined by the following well test allocation method.
Allocation data and well test data will be supplied to the Commission monthly in both computer file
and report formats.]
(d) Each producing well will be tested at least [twice] once each month. Wells that have been shut-in
and cannot meet the [twice]once-monthly test frequency must be tested within five days of startup.
All available test separator capacity within the constraints imposed by operating conditions must be
utilized for well testing.
[(t) Water volumes will be determined by API/MPMS approved methods, or the use of industry proven
on-line water cut measurement devices.
(g) API gravity will be determined for each producing West Beach well monthly.
(h) Gas samples will be taken for each non -gas lifted producing well yearly.
(i) Quarterly allocation process reviews will be held with the Commission.
0) Prior to installing separate test facilities (if required by future development) at West Beach,
Commission approval of the facilities must be obtained.
(k) This rule may be revised or rewritten after an evaluation period of at least one year.]
Rule 9 Reservoir Pressure Monitoring
[(a) Prior to regular production, a pressure survey shall be taken on each well to determine the reservoir
pressure.
(b)A minimum of one bottom -hole pressure survey per producing governmental section shall be run
annually. The surveys in part (a) of this rule may be used to fulfill the minimum requirements.
(c)The datum for all surveys is 8,800' TVD SS.
(d)Pressure survey will be a pressure buildup, pressure falloff, RFT, or static bottom -hole pressure
after the well has been shut in for an extended period.
(e)The pressure surveys will be reported to the Commission quarterly. Commission form 10-412,
Reservoir Pressure Report, shall be used to report results from these surveys. All data necessary for
complete analysis of each survey need not be submitted with the form 10-412 but must be submitted
1*1
on request.
(f)Results and data from any special reservoir pressure monitoring techniques, tests, or surveys also
shall be submitted in accordance with part (e) of this rule.]
a. An Annual Pressure Surveillance Plan shall he suhmitted to rhe AnOC in rnninnrtinn
This plan will contain the number and approximate location of pressure surveys anticipated
for the next calendar year, and it will be subject to approval by the AOGCC by 15 of
that year.
b. Data from the surveys required in (a) of this rule shall be submitted with the Annual
West Beach Oil Pool Reservoir Surveillance Report by June 15 of each year on form 10-
412. Data submitted shall include rate pressure time depths temperature and any well
condition necessary for the complete analysis of each survey. The datum for the pressure
surveys is 8,800 true vertical feet subsea. Transient pressure surveys obtained by a shut-
in buildup test, an injection well pressure fall-off test a multirate test or an interference
test are acceptable. Calculation of bottom -hole pressures from surface data will be
permitted for water injection wells. Other quantitative methods may be administratively
Approved by the AOGCC.
c. Results and data from gny special reservoir pressure monitoring techniques, tests or surveys
shall also be submitted as prescribed in (b) of this rule
North Prudhoe Bay Oil Pool Conservation Order 345
Rule 5 Surface Commingling and Common Facilities
(b) Production from each well will be determined by the following well
test allocation methodology. Allocation data and well test datawill be
supplied to the Commission via the Annual Reservoir Surveillance Report
[monthly in both computer file and report formats.]
No changes to the remainder of b (sub paragraphs).
(d) At a minimum, each producing well will be tested at least once [twice] each month. Wells that have
been shut in and cannot meet the once [twice] monthly test frequency must be tested within five days of
startup.
[(f) Water volumes will be determined by APUMPMS approved methods, or the use of industry
proven, on-line water cut measurement devices approved by the Commission.
(g) API gravity will be determined for each producing well annually by an APUMPMS approved
method.
(h) Gas samples will be taken and analyzed for composition from each non -gas lifted producing well
yearly.
(i) The allocation process for the North Prudhoe Bay Oil Pool will be reviewed with the
Commission in conjunction with scheduled LPC allocation review.]
Rule 7 Reservoir Pressure Monitoring
[7a) Prior to regular production, a pressure survey shall be taken on each well to determine the
reserv0l r pressure.
7b) Until a secondary recovery project is approved and implemented, a minimum of one bottom- hole
pressure survey per producing governmental section shall be obtained annually.
7c) The datum for all surveys is 9245' TVDss.
7d) Pressure surveys will be either a pressure buildup, pressure falloff, RFT,
or static bottom- hole pressure after the well has been shut in for an extended
period.
7e) The pressure surveys will be reported to the Commission on form 10-412,
Reservoir Pressure Report. All data necessary for complete analysis of each survey
need not be submitted with the form 10-412, but must be submitted upon
request.
7f) Results and data from any additional reservoir pressure tests, surveys or
special monitoring techniques shall be submitted in accordance with part'e' of
this rule.]
year. This plan will contain the number and avoroximate location of pressure surveys
anticipated for the next calendar year, and it will be subject to approval by the AOGCC by
July 15 of that year.
b.Data from the surveys required in (a) of this rule shall be submitted with the Annual
North Prudhoe Bay Oil Pool Reservoir Surveillance Report by June 15 of each year on
form 10-412. Data submitted shall include rate pressuretime depths temperature and
M well condition necessary for the complete analysis of each survey. The datum for the
Pressure surveys is 9245 true vertical feet subsea. Transient pressure surveys obtained by
a shut-in buildup test, an injection well pressure fall-off test a multirate test or an
interference test are acceptable. Calculation of bottom -hole pressures from surface data
will be permitted for water injection wells. Other quantitative methods may be
administratively approved by the AOGCC
c. Results and data from any special reservoir pressure monitorintz techniques tests or
surveys shall also be submitted as prescribed in (b) of this rule
Raven Oil Pool Conservation Order 570
Rule 3: Well Spacing
[To allow for close proximity of wells in separate fault blocks, spacing within the pool
will be a minimum of 20 acres. The ROP shall not be opened in any well closer than 500
feet to the external property lines where ownership or landownership changes.]
10
There shall be no restrictions as to well spacing except that no pay shall be opened in a
well closer than 500 feet to the boundary of the affected area
Rule 10: Annual Reservoir Surveillance Report
[f. By August 1 of each year, the Operator shall schedule and conduct a technical review
meeting with the AOGCC to discuss the report contents and to review items that may
require action within the coming year by the AOGCC. The AOGCC may conduct audits
of technical data and analyses used in support of the surveillance conclusions and
reservoir depletion plans.]
Rule 6: Common Production Facilities and Surface Commingling
c. All wells must be tested a minimum of [twice] once per month. The AOGCC may
require more frequent or longer tests if the allocation quality deteriorates. Wells that have
been shut in and cannot meet the [twice] once monthly test frequency must be tested
within five days of startup. All available test separator capacity within the constraints
imposed by operating conditions must be utilized for well testing.
d. [The operator shall submit a monthly report and file(s) containing daily allocation data
and daily test data for agency surveillance and evaluation.] Allocation data and well test
data will be supplied to the Commission via the Annual Reservoir Surveillance Report
[f.Water volumes will be determined by API/MPMS approved methods, or the use of
industry proven, on-line water cut measurement devices approved by the Commission.
g.API gravity will be determined for each producing well annually by an API/MPMS
approved method.
h.Gas samples will be taken and analyzed for composition from each non gas lifted
producing well yearly.
i.Quarterly allocation process reviews will be held with the Commission.]
Rule 7: Reservoir Pressure Monitoring
a. [Prior to regular production or injection, an initial pressure survey must be taken
in each well.
b. A minimum of one pressure survey will be taken annually in each of the ROP
reservoir compartments where production wells exist.
C. The reservoir pressure datum will be 9,850' feet true vertical depth subsea.
d. Pressure surveys may consist of stabilized static pressure measurements (bottom -
hole or extrapolated from surface), pressure fall-off tests, pressure build-up tests,
multirate tests, drill stem tests, and open -hole formation tests.
e. Data and results from pressure surveys shall be submitted with the annual
reservoir surveillance report. All data necessary for analysis of each survey need not be
submitted with the report but must be available to the AOGCC upon request.
f. Results and data from special reservoir pressure monitoring tests shall also be
submitted in accordance with part (e) of this rule.]
11
a.An Annual Pressure Surveillance Plan shall be submitted to the AOGCC in conjunction
with the Annual Raven Oil Pool Reservoir Surveillance Report by June 15th of each
Year. This plan will contain the number and approximate location of pressure surveys
anticipated for the next calendar year, and it will be subject to approval by the AOGCC
by July 15 of that year.
b.Data from the surveys required in (a) of this rule shall be submitted with the Annual
Raven Oil Pool Reservoir Surveillance Report by June 15 of each year on form 10-412
Data submitted shall include rate pressure time depths temperature and any well
condition necessary for the complete analysis of each survey. The datum for the pressure
surveys is 9,850' true vertical feet subsea Transient pressure surveys obtained by a shut-
in buildup test, an injection well pressure fall-off test a multirate test or an interference
test are acceptable. Calculation of bottom -hole pressures from surface data will be
permitted for water injection wells. Other quantitative methods may be administrative
approved by the AOGCC.
c.Results and data from any special reservoir pressure monitoring techniques tests or
surveys shall also be submitted as prescribed in (b) of this rule.
If you have any questions regarding this request, please contact Bill Bredar at 564-5348
or through email at William.bredar@bp.com.
Si�nJcerreely, �j
/ �+e-C/.civ� .+
Katrina Garner
PBU Area Manager
Cc: J. Schultz, CPAI
J. Farr, ExxonMobil Alaska, Production Inc.
D. White, Chevron USA
D. Sturgis, ExxonMobil Alaska, Production Inc.
E. Reinbold, CPAI
D. Roby, AOGCC
12
Y —__
Table 1. GPMA Current vs. Proposed Conservation Order Changes (part of Application for Administrative Approval Conforming PBU GPMA Pool Rules for Consisting(
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-412
Prudhoe Bay Field - Annual Surveillance Reporting Requirements to AOGCC
Amends Order/Rule Order Date Comment
Group 1 IPA
Group 2 GPMA
Group 3 Satellites
Annual Surveillance Report
Annual Overview Presentation
Production Period to be Covered
C0341 D Rule 11
11/30/2001
Note C0341 E (modified Pool Definition to
include a portion of Put River Sandstone)
15 -Mar
15 -Jun
15 -Sep
Group 2 - GPMA Oil Pools
22 -Jun
22 -Sep
CO207, 207A
Rule 9
C0345 Rule 8 12/16/1994
No rule on Surveillance reports
C0317B Rule 15 4/19/2000
Jan 1 -Dec 31
Apr 1 -Mar 31
Jul 1 -Jun 30
Amends Order/Rule Order Date Comment
Group I - IPA Oil Pools
Prudhoe Oil Pool
Put River Oil Pool
C0341 D Rule 11
11/30/2001
Note C0341 E (modified Pool Definition to
include a portion of Put River Sandstone)
C0559
11/22/2006
Corrected 2/14/2006
Group 2 - GPMA Oil Pools
— ---------
Lisburne
Niakuk..--00329A
____,__North_Prudhoe Bay
Pt. McIntyre
Raven Oil Pool
CO207, 207A
Rule 9
C0345 Rule 8 12/16/1994
No rule on Surveillance reports
C0317B Rule 15 4/19/2000
C0570 Rule 10 8/-9/2006
West Beach Oil Pool
C031 I B Rule 13 8/1/2000
Group 3 - Prudhoe Satellite Oil Pools
Aurora
Boreallis
Midnight Sun
Orion
Polaris,
C-0457BRule 8
6/25/2004
(corrected EV9!2
C0471 Rule 4
C0452 Rule 11
11/15/2000
C0505A Rule 9
C0484A Rule 9
4/28/2006
11/3/2005
Subject: [Fwd: [Fwd: Re: surveillance report dates]]
From: Jane Williamson<jane_williamson@admin.state.ak.us>
Date: Fri, 20 Apr 2007 13:03:59 -0800
To: Jody J Colombie <jody_colombie@admin. state.ak.us>, Dave Roby <dave_roby@admin. state.ak.us>,
Cathy P Foerster <cathy_foerster@admin.state.ak.us>, Alan J Birnbaum
<alan_birnbaum@law. state. ak.us>
CC: Stephen E Mcmains <steve_mcmains@admin. state.ak.us>, art Saltmarsh
<artsaltmarsh@admin.state.ak.us>, Thomas E Maunder <tom maunder@admin.state.ak.us>
There is something I didn't get around to before I left and that was to administratively amend the COs for
PBU to include reporting dates agreed to verbally with BP (and DNR). Really, only Pt. McIntyre and Borealis
have the wrong dates in the CO's. The others are either ok, or not explicit. Attached are the COs affected.
I'm not sure how you want to handle. Jody. Please put this in the following CO files along with the
attachment.
Group 1 - IPA Oil Pools
Prudhoe Oil Pool C0341D
Put River Oil Pool C0559
Group 2 - GPMA Oil Pools
Lisburne CO207, 207A
Niakuk C0329A Rule 9
North Prudhoe Bay C0345
Pt. McIntyre C0317B
Raven Oil Pool C0570
West Beach Oil Pool C0311 B
Group 3 - Prudhoe Satellite Oil Pools
Aurora C0457B
Boreallis C0471
Midnight Sun C0452
Orion C0505A
Polaris C0484A
Original Message--------
Subject:Re: surveillance report dates
Date:Thu, 31 Aug 2006 17:27:45 -0800
From:Jane Williamson < ane wiiiiarnson(ii,)admin.state. ak.us>
Organization: State of Alaska
To:Lenig, David C <David.Lenig;(),bp.com>
References: <CBF4D 8 E92B 5 A7 04 79F64416 5 8 2 FU'A i 7CB81 AvOgbp 1 ancex005.bpi. ad.bo.com>
Oops
Lenig, David C wrote:
Hi Jane,
of 3
4/23/2007 9:50 AM
From: Jane Williamson [ : , v :v R -
Sent: Thursday, August 31, 2006 5:14 PM
To: Lenig, David C
Subject: Re: surveillance report dates
E-mail is fine.
Attached is a list of the pools and orders/rules that will be amended with the Admin approval. Take a look and
see if this looks right to you. (Note, I'm only listing the rules that are affected by the new dates - there may be
additional amendments unrelated to the surveillance requirements that I've not listed.)
I'm flexible on the date for the Overview presentation. I'd be fine with specifying it to be within one or two months
of the report date rather than the POD overview that you've noted. What would you prefer?
I
Lenig, David C wrote:
Jane,
Here is a table showing the dates for the various Reports and
Presentations. I've added the production period as well. The IPA review
date remains problematic due to the proximity to spring break but we
seem to work around it each year.
Would you prefer that I put this in a letter requesting the changes? I
know we talked about this a little while ago I just haven't found the
time.
Thanks,
David
IPA GPMA
Satellites
Annual Surveillance Report March 15 June 15 September 15
Annual Overview Presentation March 22 June 22 September 22
Plan of Development March 30 June 30 September 30
Production Period Janl-Dec31 Aprl-Mar31
Jull-Jun30
-----Original Message -----
From: Jane Williamson [mailto:jane williamson@admin.state.ak.us]
Sent: Thursday, August 31, 2006 2:30 PM
To: Lenig, David C
Subject: surveillance report dates
Hi David.
When you get a second, could you please send back an e-mail that lists
all the surveillance report dates that we've agreed to for all PBU pools
(including GPMA)? Also, do you have dates for surveillance reviews?
I'll go through the list and make sure the Conservation orders are
correctly worded, then put out administrative amendments as necessary.
I checked with Cammy and she said an e-mail is fine for starting the
2 of 3 4/23/2007 9:50 AM
administrative action process.
Thanks.
Jane
Senior Reservoir Engineer (907) 793-1226
Alaska Oil and Gas Conservation Commission
surveillance report.gls Content -Type: application/vnd.ms-excel
Content -Encoding: base64
3 of 3 4/23/2007 9:50 AM
411
DEPARTMENT OF NATURAL RESOURCES
DIVISION OF OIL AND GAS
CERTIFIED MAIL
RERURN RECEIPT REQUESTED
January 27, 2004
Francis Sommer
Prudhoe Bay Asset Manager, Greater Prudhoe Bay
BP Exploration (Alaska), Inc.
900 East Benson Boulevard
P.O. Box 196612
Anchorage, Alaska 99519-6612
K MURKOWSKI, GOVERNOR
550 WEST 7' AVENUE, SUITE 800
ANCHORAGE, ALASKA 99501-3560
PHONE: (907) 269-8800
FAX (907) 269-8938
_^
— 'N -7AVEJ
JV 2 8 2004
Alaska Cil &Gas Cons. Commiss"
Anchorage
Re: Revised Request to Commingle Pt. McIntyre Participating Area Production with IPA Production
and Amendments to the Greater Pt. McIntyre Area Production Allocation Procedures
Dear Mr. Sommer:
By a letter dated September 9, 2003, BP Exploration (Alaska) Inc. (BPXA), as Prudhoe Bay Unit
(PBU) Operator, submitted a request for authorization to commingle Prudhoe Bay Unit (PBU) Pt.
McIntyre Participating Area (PMPA) production from the PM2 drillsite with production from the
PBU Initial Participating Areas (IPA) through surface facilities at Gathering Center 1 (GC -1). The
Department of Revenue Tax Division (DOR) and the Division of Oil and Gas (Division) responded to
BPXA's request by letters dated October 16 and 27, 2003, respectively. DOR objected to treating the
NGLs recovered from the PM2 to GCl gas stream as IPA fluids and proposed a simplified method of
allocating those NGLs to the PMPA. Its proposal was to take the percentage of total separator off -gas
that is attributable to PMPA wells producing into GCI, with the gas lift gas netted out, multiplied by
the total NGL recovery at the CGF. The Division expressed the same concerns and proposed a
similar methodology, but with the PMPA separator off -gas debited for fuel and flare uses at GC 1 in
addition to netting out the gas lift gas component. Both agencies supported treating PMPA gas, other
than that gas turned into NGLs, as indigenous IPA natural gas.
In response to the agency letters, BPXA, on November 11, 2003, amended its original request to
commingle PBU and PMPA production to use the simplified NGL allocation method proposed by the
DOR. It also requested approval to change production allocation within the Greater Pt. McIntyre
Area (GPMA) to a rate table allocation methodology, and provided additional clarification regarding
the allocation procedures for PMPA production. The November 11, 2003, letter sets forth the details
of BPXA's revised proposal on these issues.
"Develop, Conserve, and Enhance Natural Resources for Present and Future Alaskans."
ti
Mr. Francis Sommer
PM2 to GC -1 Project and
GPMA Allocation Procedures
January 27, 2004
Page 2
Based on our review of BPXA's revised request, meetings with BPXA regarding the PBU Western
Satellite Production Metering Plan (WSPMP) and the proposed modifications to the Plan, and
conversations with the DOR and the Alaska Oil and Gas Conservation Commission, which has
already approved the commingling request in Administrative Approval No. 317.001, the Division
issues the following decision on BPXA's revised request.
(1) The Division approves BPXA's request to commingle PMPA production with IPA production
using the simplified NGL allocation method proposed by the DOR, subject to the following
conditions: (a) BPXA shall submit to the Division, within five working days of their
execution, any amendments to the Special, Supplemental Provisions to the PBU Operating
Agreement for the PMPA, or the Pt. McIntyre Facility Sharing Agreement (collectively
referred to as the Agreements) authorizing the use of IPA production equipment and services
for Pt. McIntyre operations. If the PBU Owners decide against amending these Agreements as
a result of either the PM2 to GC Project or the "Waterwheel" Project, BPXA shall notify the
Division in writing about the decision within five working days of making it; and (b) BPXA
shall submit the final list of wells whose production BPXA will send to GC -1 from PM2.
Subject to the foregoing, any PMPA gas sent to GC -1, other than that gas turned into NGLs,
may be treated as indigenous IPA natural gas.
(2) The Division approves BPXA's request to change the allocation procedures for all the
participating areas within GPMA from the currently approved well test methodology to the
rate table methodology outlined on page three of BPXA's November 11, 2003, letter. The
following sections of the Division's Findings and Decisions regarding GPMA participating
areas are amended to refer to the rate table methodology: (a) Findings and Condition #12 of
the Decision and Findings of the Director of the Division of Oil and Gas regarding the
Amended Application for the Third Expansion of the Unit Area and Formation of the Pt.
McIntyre Participating Area, dated December 30, 1993; (b) Section VI. 9. of the Decision and
Findings of the Commissioner Alaska Department of Natural Resources regarding the
Application for the Formation of the West Beach Participating Area, dated April 4, 1993; (c)
Section VI. S. of the Decision and Findings of the Commissioner Alaska Department of
Natural Resources regarding the Application for the Formation of the North Prudhoe Bay
Participating Area, dated December 30, 1994; (d) Section VI. 7. of the Decision and Findings
of the Commissioner Alaska Department of Natural Resources regarding the Application for
the Formation of the Niakuk Participating Area, dated March 2, 1994; and (e) Section VI. 10.
of the Decision and Findings of the Commissioner Alaska Department of Natural Resources
regarding the Application for the Fourth Expansion of the Unit Area, First Expansion of the
Niakuk Participating Area and Formation of the West Niakuk Participating Area dated
November 17, 1997:
Mr. Francis Sommer
PM2 to GC -1 Project and
GPMA Allocation Procedures
January 27, 2004
Page 3
A person affected by this decision may appeal it, in accordance with 11 AAC 02. Any appeal must be
received within 20 calendar days after the date of "issuance" of this decision, as defined in 11 AAC
02.040(c) and (d) and may be mailed or delivered to Tom Irwin, Commissioner, Department of
Natural Resources, 550 W. 7th Avenue, Suite 1400, Anchorage, Alaska 99501; faxed to 1-907-269-
8918, or sent by electronic mail to dnr_appeals@dnr.state.ak.us. This decision takes effect
immediately. An eligible person must first appeal this decision in accordance with 11 AAC 02 before
appealing this decision to Superior Court. A copy of 11 AAC 02 may be obtained from any regional
information office of the Department of Natural Resources.
Sincerely,
Mark D. Myers
Director
cc: Commissioners, AOGCC
Greg Bidwell, DOR
Ken Rupp, BPXA
Leslie Senden, BPXA
410
November 11, 2003
0 0 0
BP Exploration (Alaska) Inc.
. 900 East Benson Boulevard
P. O. Box 196612
Anchorage, Alaska 99519-6612
(907) 561-5111
Dr. Mark Myers, Director
Division of Oil and Gas
Department of Natural Resources
550 West 7h Avenue, Suite 800
Anchorage, AK 99501
Ms. Sarah Palin, Chair
Alaska Oil and Gas Conservation Commission
333 West 7`h Ave, Suite 100
Anchorage, AK 99501
Re: Revised Request to Commingle Prudhoe Bay Unit (PBU) and Pt. McIntyre Participating
Area (PMPA) Production
Dear Chair Palin and Dr. Myers:
The intent of this letter is fourfold: 1) to respond to the Division of Oil and Gas letter, dated
October 27, 2003, that rejected our initial request to commingle PBU and PMPA production and
treat all gas from the PM2 to GC 1 stream as IPA gas, 2) to revise our original request to
commingle PBU and PMPA production, 3) to request approval to change GPMA to rate table
allocation methodology, and 4) to provide additional clarification regarding the allocation
procedures for Pt. McIntyre production.
BPXA, as operator of the Pt. McIntyre Participating Area (PMPA) within the Prudhoe Bay Unit,
has received both the Department of Revenue Tax Division (DOR) letter dated October 16, 2003
and the Division of Oil and Gas letter dated October 27, 2003 regarding our previous request to
commingle PBU and PMPA production, dated September 9, 2003. The DOR letter presented its
objection to treating the NGLs recovered from the PM2 to GCl gas stream as IPA fluids and
proposed a simplified method of allocating those NGLs to Pt. McIntyre. The proposed method
consisted of taking the percentage of total separator off -gas that is attributable to Pt. McIntyre
wells producing into GCI, with the gas lift gas netted out (gas lift gas from GPMA does not
contain NGLs), multiplied by the total NGL recovery at the CGF. The DOG letter echoed the
same concerns and proposed a similar methodology, but with the Pt. McIntyre separator off -gas
debited for fuel and flare uses at GCI in addition to netting out the gas lift gas component. Both
agencies supported our request to treat all injected gas as indigenous to the IPA.
The PBU Working Interest Owners appreciate the DOG's allowance for fuel and flare uses and
the recognition of the fact that we are not required to pay tax and royalty on produced gas used
Page 1 of 4
for fuel and flare. However, while we would benefit from this change, the benefits do not
warrant the cost and complexity of accounting for fuel gas and flare. Ignoring the fuel and flare
factor is also consistent with the fact that the allocation of Pt. McIntyre NGLs is itself purposely
simplified. A precise measure of the NGLs attributable to Pt. McIntyre gas would require costly
and time-consuming process simulations on an ongoing basis. We therefore prefer to keep the
NGL allocation as simple and streamlined as possible and are revising our original request to
employ the simplified NGL allocation scheme proposed by the DOR.
With this change in NGL allocations, we must now also revise our original request to commingle
PBU and PMPA production on the surface at GC 1 and respectfully suggest the following change
to Rule 10 of AOGCC Conservation Order 31713:
a. Production from the Pt. McIntyre and Stump Island oil pools may be
commingled on the surface with production from other pools for processing at the
LPC and GCI prior to custody transfer.
b. Production from each well will be determined by the rate table methodology set
forth in the WSPMP. Allocation data and well test data will be supplied to the
Commission monthly in both computer file and report formats.
c. NGLs recovered at the LPC will be allocated to each pool based on actual gas
production volumes and NGL process simulations. Process simulations will be
updated at least once per year based on NGL samples and results reported to the
Commission.
NGLs attributable to the PM2 to GCI gas stream and recovered at the CGF will
be allocated by calculating the amount of separator off -gas attributable to Pt.
McIntyre wells producing into GCL The Pt. McIntyre separator off -gas will be
determined according to Section 10 b. above, and will not include the metered Pt.
McIntyre gas lift gas supplied to wells flowing to GCL The percentage of total
separator off -gas delivered to the CGF that is Pt. McIntyre formation gas
multiplied by the total NGL recovery at CGF yields the amount of NGLs to be
allocated to Pt. McIntyre.
We believe that the changes to Rule 10 can be handled administratively if DOG and DOR are in
agreement with the simplified approach.
The "Request to Commingle Production from the PMPA with IPA Production" submitted to
your agencies on September 9, 2003 stated that "production from PMPA wells that is
commingled with IPA production at GC 1 will be determined and allocated in accordance with
the PBU Western Satellite Production Metering Plan' (WSPMP). To more clearly establish how
we propose allocating PMPA production flowing to either the LPC or GC 1, we are providing the
following description of our proposal as it applies to each "Key Provision' of the WSPMP.
Page 2 of 4
1&2) The EOA allocation technique will be used for all GPMA wells (gas lifted and flowing)
in place of the current well test allocation procedure. Daily production from all wells
will be based on empirical well performance curves derived from 3-phase flow equations
and production well test data, and will be a function of flowing tubing pressure and gas -
lift rate. This is a modification of the WSPMP, which uses the WOA allocation
technique for flowing wells and the EOA allocation technique for gas lifted wells.
3) A minimum of two well tests per month will be performed on each GPMA well, when
operational conditions allow. This is a modification of the WSPMP, which calls for one
test per month per well.
4) All PM2 wells flowing exclusively to Gathering Center I (GCI) will use GCI's well
allocation factor for oil, gas, and water. All PM2 wells flowing exclusively to the
Lisburne Production Center (LPC) will use LPC's well allocation factor for oil, gas,
and water. PM2 wells that flow to both GCI and LPC in the same month will use a
prorated (GCI and LPC) well allocation factor for oil, gas, and water.
5) Within the GPMA, test separators will continue to have Micromotion meters for mass
flow measurement and Phase Dynamics meters for water cut measurements.
6) Zero -rate tests will be performed at PM2 once a quarter (every three months). If leak
rates are not within acceptable tolerances, corrective measures will be taken. Leak rates
from the zero -rate test will be used to correct test rates as necessary. This procedure is
consistent with the WSPMP.
7) Reservoir specific shrinkage factors will be used to correct metered fluids to stock tank
barrels. This is consistent with both our current operations and the WSPMP.
We also hereby request approval to change the allocation procedures for all participating areas
within GPMA from the current well test methodology that was approved in the decisions and
findings for the PMPA to the rate table methodology outlined above. In accordance with the
testimony provided in support of the WSPMP, allocation through the use of rate tables is
expected to provide a more consistent, accurate, and efficient determination of fluid flow.
Changing to the rate table methodology is included in the work scope to upgrade the GPMA
automation system from Setcim to IP21. Work on this upgrade is in progress and is expected to
be completed during 1Q 2004. Until completion, we will continue to allocate production
according to the current well test methodology.
To assist the agencies in evaluating the allocation procedures related to the PM2-GCI project,
we have attached a summary of the overall project benefits. Also attached is the current
expected well lineup for the PM2 wells. This chart shows where (GCI or LPC) each well will be
Page 3 of 4
capable of flowing. Please note that this is preliminary and the final well lineup may change
based on operational considerations.
Please let me know if you need any clarification of this information.
Respectfully,
Francis Sommer
Prudhoe Bay Asset Manager
Greater Prudhoe Bay
BP Exploration (Alaska) Inc.
cc: Mr. Dan Kruse, ConocoPhillips Alaska, Inc.
Mr. Marc Vela, ExxonMobil
Mr. Dan Dickinson, Department of Revenue, Tax Division
Mr. Mike Kotowski, Division of Oil and Gas
Ms. Jane Williamson, Alaska Oil and Gas Conservation Commission
Page 4 of 4
• 0
PM2 to GC1 Project
Supplemental Project Information
PM -2 to GC -1 Proiect Benefits
This project is estimated to increase recoveries by 20-25 MMBO. The primary benefits
are from debottlenecking production at Pt. McIntyre, improved efficiency of the Pt
McIntyre base EOR and Supplemental MI projects and the supply of water to support
waterflood operations in the GC -2 area.
Waterflood (WF) Benefit
Upgrading GC -1 to handle production from PM2 debottlenecks the Pt. McIntyre water
production constraint that exists today at the Lisburne Production Center (LPC). This
allows PM high water cut wells that are currently shut-in due to LPC facility constraints
to be brought back on production and to stay on production longer.
Low Permeability (kh) Production Benefit
The low kh production benefit results from low kh PM2 wells, which cannot produce into
the high pressure LPC system being able to produce into the lower pressure GC -1 system.
EOR Response Benefit
In addition to the waterflood benefit, increased enhanced oil recovery from MI injection
will be realized from Pt McIntyre producers staying on production longer. This helps to
maintain the integrity of the 9 -spot patterns and improves areal conformance of the WAG
flood.
MI Recovery Benefit
Directing part of PM2 production to GC 1 will result in a higher amount of MI being
recovered for use in enhanced oil recovery. The miscible injectant process at the CGF is
more efficient than the recovery process at the Lisburne Production Center, with more
return MI captured at the CGF than would occur at the LPC.
Gas Constraint Benefits
PM -2 to GC -1 project debottlenecks gas production as well as water production. Because
Pt McIntyre is gas rate constrained, returned MI (RMI) entering the system from ongoing
EOR operations would otherwise impact high GOR oil production. Producing a portion
of PM2 to GC 1 reduces the impact since the marginal GOR at GC 1 are higher than at the
LPC.
GC -2 Water Benefit
There is a need for additional injection water at GC -2 with the start-up of water injection
projects in the Satellites and EWE. PM2 to GCI will facilitate meeting this demand by
allowing PM water recovered at GC1 to be directed to the GC2 area via the recently
connected GC1 — GC2 water tie -line. Based on water forecasts, the additional water from
PM -2 wells producing into GC -1 should meet most of the anticipated demand.
. �t
PM2 to GC1 Projec
Initial Well Lineup
Well #
Service After Startup
LP&HP 1
HP Only (2)
Infector
NIS 3
LP Conversion (4)
1
LP&HP
X
2
NIS
X
3
LP&HP
X
4
LP&HP
X
5
NIS
X
6
LP&HP
X
7
LP&HP
X
8
LP&HP
X
9
Injector
X
10
HP Only
X
High
11
LP&HP
X
12
LP&HP
X
13
LP&HP
X
14
HP Only
X
High
15
Injector
X
16
Injector
X
17
LP&HP
X
18
LP&HP
X
19
LP&HP
X
20
LP&HP
X
21
LP&HP
X
22
LP&HP
X
23
Injector
X
24
LP&HP
X
25
LP&HP
X
26
NIS
X
27
LP&HP
X
28
Injector
X
29
Injector
X
30
LP&HP
X
31
LP&HP
X
32
LP&HP
X
33
LP&HP
X
34
Injector
X
35
LP&HP
X
36
LP&H P
X
37
LP&HP
X
38
NIS
X
39
NIS
X
40
LP&HP
X
41
LP&HP
X
42
Injector
X
43
NIS
X
44
LP&HP
X
45
HP Only
X
Medium
46
Injector
X
September 22, 2003
` PM2 toGC 1 Project
�
Initial Well Lineup
Well # Service After Startup LP&HP 1 HP Only (2) Infector
47
Injector
X
48
HP Only
X
49
LP&HP
X
50
HP Only
X
51
LP&HP
X
52
LP&HP
X
53
HP Only
X
54
LP&HP
X
55
NIS
56
HP Only
X
57
HP Only
X
58
HP Only
X
59
LP&H P
X
60
LP&HP
X
34
9 10
NIS (3) LP Conversion (4)
Medium
Medium
Low
X
Low
Low
High
7
Notes:
1) LP&HP wells can flow to either LPC or GC1
2) HP Only wells can only flow to LPC
3) NIS are not in service
4) HP Only wells are being scheduled for connection to LP system ranked high, medium,
low for implementation. Some high ranked wells may be available for LP service at startup.
September 22, 2003
DEPARTMENT OF NATURAL RESOURCES
DIVISION OF OIL AND GAS
CERTIFIED MAIL
RERURN RECEIPT REQUESTED
October 27, 2003
Francis Sommer
Prudhoe Bay Asset Manager, Greater Prudhoe Bay
BP Exploration (Alaska), Inc.
900 East Benson Boulevard
P.O. Box 196612
Anchorage, Alaska 99519-6612
FRANKH. MURKOWSKI, GOVERNOR
550 WEST 7TH AVENUE, SUITE 800
ANCHORAGE, ALASKA 99501-3560
PHONE. (907) 269-8800
FAX (907) 269-8936
,I q
Re: Request to Commingle Pt. McIntyre Participating Area Production with IPA Production
Dear Mr. Sommer:
I am responding to your September 9, 2003 request for authorization to commingle Prudhoe Bay Unit
(PBU) Pt. McIntyre Participating Area (PMPA) production from the PM2 drillsite with production
from the PBU Initial Participating Areas (IPA) through surface facilities at Gathering Center 1 (GC -
1). The letter states, in part, that NGLs removed from PM2 gas produced through GC -1 facilities will
be accounted for and reported as IPA fluids and any gas produced into GC -1 facilities from PMPA
wells will be deemed "lost or consumed in operations" and any PMPA gas injected into the Prudhoe
Bay Reservoir will be treated as indigenous IPA natural gas.
After review of the supplemental materials submitted in support of this request and further analysis by
staff, the Division of Oil and Gas (Division) is denying your request. The Division believes that
NGLs removed from the production of PMPA wells through IPA facilities should be accounted for
and reported as PMPA fluids, not IPA fluids. While we recognize the overall benefits of the PM2 to
GC -1 Project, we disagree that commingling PMPA production with IPA production at GC -1 should
transform PMPA fluids, whether oil or gas liquids, into IPA fluids.
The Division also recognizes that a precise measure of the NGLs attributable to Pt. McIntyre gas
would require costly and time-consuming process simulations on an ongoing basis. However, we
agree with the Department of Revenue's view, as set out in its October 16, 2003 letter to you, that a
simple formula can be used to approximate the quantity of Pt. McIntyre NGLs recovered at the
Central Gas Facility (CGF).
"Develop, Conserve, and Enhance Natural Resources for Present and Future Alaskans. "
Mr. Francis Sommer
PM2 to GC -1 Project
October 27, 2003
Page 2
NGLs are recovered at the CGF from separator off -gas from the IPA, Prudhoe Bay satellites, or, after
commingling, the PMPA. The gross amount of gas attributable to Pt. McIntyre wells*producing into
GC -1 can be calculated using the current test separators at Pt. McIntyre. The PMPA apportioned
share of fuel gas utilized in GC -1 and flare gas in any month can be based on its apportioned share of
the total produced gas through GC -1. The Point McIntyre gas lift gas and the apportioned share of
fuel and flare gas can be netted out to arrive at an estimate of the Pt. McIntyre gas that becomes
separator off -gas at GC -1. After similarly accounting for gas lift and fuel and flare gas from the rest
of the gathering centers and flow stations, the percentage of total PM 2 and IPA separator off -gas that
is PM 2 Pt. McIntyre formation gas multiplied by total NGL recovery at the CGF provides a simple -
to -calculate way of approximating NGL recovery from Pt. McIntyre production at the CGF.
After taking into account the PMPA NGLs, the Division has no objection to treating Pt. McIntyre gas,
other than that gas turned into NGLs, as indigenous IPA natural gas.
A person affected by this decision may appeal it, in accordance with 11 AAC 02. Any appeal must be
received within 20 calendar days after the date of "issuance" of this decision, as defined in 11 AAC
02.040(c) and (d) and may be mailed or delivered to Tom Irwin, Commissioner, Department of
Natural Resources, 550 W. 7th Avenue, Suite 1400, Anchorage, Alaska 99501; faxed to 1-907-269-
8918, or sent by electronic mail to dnr_appeals@dnr.state.ak.us. This decision takes effect
immediately. An eligible person must first appeal this decision in accordance with 11 AAC 02 before
appealing this decision to Superior Court. A copy of 11 AAC 02 may be obtained from any regional
information office of the Department of Natural Resources.
Sincerely,
_�Mark D. Myers
P'-/Director
cc: AOGCC Chair
Greg Bidwell, ADOR
Ken Rupp, BP
Leslie Senden, BP
Cm
FRANK MURKOWSKI, GOVERNOR
❑ State Office Building
PO Box 110420
Juneau, AK 99811-0420
907.465.2320
O 550 W Seventh, Suite 500
Anchorage, AK 99501-3566
907.269.6620
www.tax.state.ak.us
October 16, 2003
Ms. Sarah Palin,
Chair
Alaska Oil and Gas Conservation Commission
333 West 7th Ave, Suite 100
Anchorage, Alaska
99501
Francis Sommer
Prudhoe Bay Asset Manager
BP Exploration (Alaska), Inc.
900 East Benson Boulevard
P.O. Box 196612
Anchorage, Alaska 99519-6612
Re: BP Request to treat NGLs from Pt. McIntyre gas commingled with IPA Production
as IPA NGLs
Dear Chair Palin:
In a letter dated September 9, 2003 entitled "Re: Request to Commingle
Production from Pt. McIntyre Participating Area with IPA Production", BP's Francis
Sommer proposes to account for and report NGLs removed from the production of Point
McIntyre Participating Area wells as IPA fluids. The State Department of Revenue Tax
Division believes that NGLs removed from the production of Point McIntyre
Participating Area wells should be accounted for and reported as Point McIntyre fluids.
While recognizing the benefits of commingling Point McIntyre production with IPA
production at Prudhoe Bay Gathering Center 1, such commingling should not transform
Point McIntyre fluids, whether oil or gas liquids, into IPA fluids.
& 0 0
The Tax Division realizes that a precise measure of the NGLs attributable to Pt.
McIntyre gas would require costly and time-consuming process simulations. However, a
simple formula can be used to approximate the quantity of Pt. McIntyre NGLs recovered
at the Central Gas Facility. NGLs are recovered at the CGF from separator off -gas from
the IPA, or, after commingling, Prudhoe Bay satellites and the Point McIntyre PA. The
amount of separator off -gas attributable to Pt. McIntyre wells producing into Gathering
Center 1 can be calculated using the current test separators at Pt. McIntyre. The Point
McIntyre gas lift gas (with its NGLs already stripped out) can be netted out to arrive at an
estimate of the Pt. McIntyre formation gas that becomes separator off -gas. The
percentage of total separator off -gas that is Pt. McIntyre formation gas multiplied by total
NGL recovery at the CGF provides us with a simple -to -calculate way of approximating
NGL recovery from Pt. McIntyre production at the CGF.
At this time, the Tax Division has no objection to treating Pt. McIntyre gas other
than that gas turned into NGLs as indigenous IPA natural gas.
Respectfully,
Dan ickinson, Director, Tax Division
Department of Revenue
Cc: Dr. Mark Myers, Director, Division of Oil and Gas
Mr. Mike Kotowski, Division of Oil and Gas
Ms. Jane Williamson, Alaska Oil and Gas Conservation Commission
Mr. Dan Kruse, ConocoPhillips Alaska, Inc.
Mr. Marc Vela, ExxonMobil
--zaFlr-
7
September 9, 2003
Dr. Mark Myers, Director
Division of Oil and Gas
Department of Natural Resources
550 West 7th Avenue, Suite 800
Anchorage, Alaska
99501
BP Exploration(Alaska)Inc.
900 East Benson Boulevard
P.O. Box 196612
Anchorage, Alaska 99519-6612
(907)561-5111
Ms. Sarah Palin, Chair
Alaska Oil and Gas Conservation Commission
333 West 7th Ave, Suite 100
Anchorage, Alaska
99501
Re: Request to Commingle Production from Pt. McIntyre Participating Area with IPA
Production
Dear Chair Palin and Dr. Myers:
BP Exploration (Alaska) Inc. (BPXA) as Operator of the Pt. McIntyre Participation Area
(PMPA) within the Prudhoe Bay Unit (PBU), requests authorization to commingle a
portion of the production from the Pt. McIntyre PM2 drillsite with production from the
Initial Participating Areas (IPA) of the PBU through surface facilities at Gathering Center
1 (GC -1).
This project will divert some of the Pt. McIntyre production from PM -2 drill site to GC -1,
thereby reducing PM -2 wellhead pressure, increasing drawdown and utilizing water
handling capacity at GC -1. The effects of gas and water constraints at the Lisburne
Production Center (LPC) and hydraulic constraints in the production line to the LPC will
be reduced. This debottlenecking greatly improves performance of the WAG process at
Pt. McIntyre providing significant EOR benefits. The additional volumes of unprocessed
fluids at GC -1 will result in increased produced water volumes, which will be transported
through the GC -1 to GC -2 tie -line for use in Satellite development in the GC -2 area.
Additional project details are included in Attachment 1.
For royalty and tax purposes, production from PMPA wells that is commingled with IPA
production at GC -1 will be treated in the same way as all other production from Prudhoe
satellites that is processed in IPA production facilities. In particular, production from
these wells will be determined and allocated in accordance with the PBU Western
Satellite Production Metering Plan. The oil production so determined will be included in
the Greater Pt. McIntyre Well Allocation Report.
NGLs removed from the production of PMPA wells produced through GC -1 facilities will
be accounted for and reported as IPA fluids and any gas produced into GC -1 facilities
from PMPA wells will be deemed lost or consumed in operations, with the effect that all
gas from all reservoirs separated at GC -1 that is injected into the Prudhoe Bay (Permo-
Triassic) Reservoir will be treated as indigenous IPA natural gas for all purposes.
Changes to Conservation Order 317B Rule 10, which governs the commingling of
PMPA production into the LPC, will be required to address these changes. We've
attached specific language changes to Conservation Order 317B, Rule 10 for the
AOGCC's consideration (Attachment 2) for the commingling of PMPA fluids with IPA
fluids as well as GPMA fluids.
Please let me know if you need any more information to obtain approval for the changes
requested.
RespectfulI
Francis Sommer
Prudhoe Bay Asset Manager
Greater Prudhoe Bay
BP Exploration (Alaska) Inc.
cc: Mr. Dan Kruse, ConocoPhillips Alaska, Inc.
Mr. Marc Vela, ExxonMobil
Mr. Dan Dickinson, Department of Revenue, Tax Division
Mr. Mike Kotowski, Division of Oil and Gas
Ms. Jane Williamson, Alaska Oil and Gas Conservation Commission
0 Attachment 1 •
Application for Commingling of PMPA Production with IPA Production
PM -2 to GC -1 Proiect Description
The PM -2 to GC -1 project debottlenecks Pt. McIntyre's production by allowing some
PM -2 drill site wells to be produced to GC -1. Pt. McIntyre's production is currently
limited by gas and water capacity constraints at the Lisburne Production Center (LPC) as
well as hydraulic constraints in the production line to the LPC. An existing out -of -
service low pressure 36" Seawater Injection (SWI) pipeline will be used to route some of
the PM -2 production to GC -1. With modifications, GC -1 will provide up to 90M BWPD
of water handling capacity for the project and operates at a lower pressure than the LPC.
This additional water capacity and lower pressure will improve the performance of the
waterflood and Enhanced Oil Recovery (EOR) processes at Pt. McIntyre. The produced
water resulting from processing of Pt. McIntyre fluids at GC -1 will be used to supply
water for Satellite development in the GC -2 area through the GC -1 to GC -2 tie -line.
Project start-up is expected to occur in late 2003. Incremental oil rate attributable to the
project is expected to increase from approximately 4500 BOPD initially to a peak of
more than 9000 BOPD as EOR response is realized.
Proiect Scope
Conversion of Seawater Injection Line
The mothballed 36 inch Seawater Injection Line will be converted to move production
from Pt. McIntyre drill site PM -2 to GC -1.
PM -2 Manifoldine
Header modifications will be required at PM -2. The existing production header will be
utilized as a Low Pressure (LP) header for routing production to GC -1, and the existing
Water Injection (WI) header will be utilized as a High Pressure (HP) header to
accommodate production flow to the LPC. A new WI header will be installed for
injection wells, thus minimizing the number of well tie-ins and manifold modules wall
penetrations. Most PM -2 production wells will have the capability to flow to GC -1.
However, only select wells will be able to flow to the LPC. Under the current design,
only those wells capable of flowing into the higher -pressure system will be tied into the
LPC header. PM -2 production is expected to be ramped up to match the GC -1 water
handling capacity. A return line from the existing test separators will be added to allow
for wells flowing to GC -1 to be tested at flowing pressure.
New ESD/Pig Launcher Module
The LP header will be routed to a new ESD/Pig Launcher module. The new module will
contain three 24" ESD valves, a chemical skid and tankage for corrosion inhibitor, a
hydraulic skid for valve actuation, and a 36" pig launcher. Two full port ball valves will
be installed downstream of the new pig launcher to provide double block and bleed
capability.
�
Attachment 1 i
Application for Commingling of PMPA Production with IPA Production
36" Pining
New 36" pipe will be installed on new VSMs from the new pig launcher to the tie-in
point with the 36" SWI pipeline buried in the causeway. The segment of line coming
from the STP will be abandoned in place with a blind and bleed. The tie-in to the
existing 36" line will be made at the north West Dock breach to minimize traffic
interruption.
The following is a depiction of the major components at PM -2:
STP
PM2 Facility Changes
36" Jumper
To GC1
Figure 1
IN
sol ds
Additions in red
Cross Country 36" Pipeline
An evaluation was made of the functionality of the 36 inch cross-country pipeline under
expected flow rates, fluid temperatures and corrosion conditions. This evaluation
resulted in the determination that the pipeline is suitable for the intended change in
service. As a result, no work is planned for the cross-country pipeline as part of this
project.
GC -1 Modifications
Use of the 36 -inch pipeline as a low velocity flowline is expected to cause larger than
normal liquid slugs to the GC -1 Slug Catchers. To assist in mitigating the new slug
impacts, the project scope includes raised weirs on two of the GC -1 Slug Catchers to
2
• Attachment•
1
Application for Commingling of PMPA Production with IPA Production
provide additional surge volume and throttling divert valves to allow adjustment of flow
between Slug Catcher trains. To debottleneck water handling, the project scope also
includes GC -1 piping and control valve modifications downstream of slug catchers,
dehydrators and produced water injection pumps.
Reservoir Analysis
The primary reservoir benefits of the project will result from the debottlenecking of
production capacity limitations and improved efficiency and duration of the Pt McIntyre
EOR flood. Many of the Pt McIntyre wells in the waterflood/EOR area are currently
shut-in because of water handling constraints at the LPC. By moving some production to
GC -1, it will be possible to return most of these shut-in wells to production (Figure 2).
Reserve benefits at Pt McIntyre are therefore the result of enabling high water cut wells
to stay on production longer, restoring the integrity of the 9 -spot patterns and improving
areal conformance of the WAG flood. Also, low permeability wells that cannot produce
into the high pressure LPC system can be produced into the lower pressure GC -1 system.
Pt. McIntyre Field, Need for PM2 to GCI De -Bottlenecking
Watertlood Patterns
P2-22 P2.50A P2.14
P2.10
P2- p240 P2-13
P"- P246 ♦ P 2.18 P240 P2-336
AY %- A
♦
P1-01 P2.12
♦ P2 2I P2 -SB P2•Ii %-27 P2-28
P1-23 pi P2d1 ♦ ♦
P2-10
%•11
P2 P2 -0B
%-2f P2-18
P2-03 ♦ P2-25
Pt -21 P2-01 %-07 P2.29 P2.17♦ P2-20 ♦ P2d2
%-12 P1-1• P2 -3i Current MI Inje
A +♦
pY P2P244Li P2.35 . Patterns
2 %-09
%. P2•M Pb11
%-20 %.17 PI -04 P2.52
%-07 • r • • N %-02A P2: P241 P2-38
♦ •
♦,00• P1 ••� %48 %-05 P2.37
P2-53 %-25
�• -- Gravity D inage Area �, P2 -5/A ♦ P24M
• • %"�+ %-02 �• • P2-506 •
•••• ♦ ¢ •�... t••• P2.37
P2 -57A •
Producer •
•
♦ Injector
♦ Gas Cap Injector
¢Plugged and Abandoned
3
ction
Attachment 2
Application for Commingling PMPA Production with IPA Production
Proposed Modifications to CO 3176
• Modify Rule 10a to provide for commingling at GC -1:
o "Production from the Pt. McIntyre and Stump Island oil pools may
be commingled on the surface with production from other pools for
processing at either the LPC or GC -1 prior to custody transfer."
• Modify Rule 10b, iii and iv to recognize well allocations are to be done by
processing facility:
o "iii. Sum the TMP volume for all wells in all pools by processing
facility (LPC or GC1)."
o "iv. Determine an allocation factor as the ratio of the metered
volume to the TMP for all wells in all pools (i.e., metered/TMP) for
each processing facility."
• Modify Rule 10c to recognize no allocation of NGLs for production sent to
GC1:
o " For production processed in the LPC only, NGLs will be allocated
to each pool based on actual gas production volumes and NGL
process simulations. Process simulations will be updated at least
once per year based on NGL samples and results reported to the
Commission."
fl �
ARCO Alaska, Inc.
Post Office BJ*0360
0360
Anchorage, Alaska 99510-0360
Telephone 907 276 1215
Greater Pt. McIntyre Area
March 9, 2000
Robert N. Christenson, Chairman
Alaska Oil and Gas Conservation Commission
3001 Porcupine Drive
Anchorage, AK 99501-3192
400
RE: Question Raised at the January 12-13 Hearing on Proposed Amendment to
Area Injection Order No. 413.
Dear Mr. Christenson:
This letter is in response to a question that was asked at the January 12-13 hearing on
proposed amendment to Area Injection Order 4B. With respect to the Pt. McIntyre
miscible Enhanced Oil Recovery (EOR) project, you asked what would be the
magnitude of the MMP buffer resulting from the thermal cooling of the rock by injected
source water. Pt. McIntyre injects source water at a temperature of approximately 75
degrees Fahrenheit into a reservoir originally at 182-185 degrees Fahrenheit. Reservoir
temperature increases away from the injection well to the limits of the temperature bulb.
Calculations show that the MMP drops by at least five psi for every one degree of
temperature decrease. Thermal modeling shows that the reservoir temperature is
currently reduced by at least 10 degrees Fahrenheit to a distance of at least 550 feet
from a typical EOR injection well, providing an MMP buffer of at least 50 psi. The
radius of this buffer will increase with time as the temperature bulb propagates further
from the injection wells.
As was stated in the hearing testimony, Pt. McIntyre will be operated to maintain
reservoir pressure at original pressure, nominally 4370 psi. This operating practice
significantly reduces the requirement of an MMP buffer as compared to other fields that
are not operated in this manner.
In addition, a new analytical technique for
Peck (SPE 59378) has been applied to tl-
technique has indicated that the MMP could
of approximately 300 psi.
ARCO Alaska, Inc. is a Subsidiary of AtlanticRichfieldCompany
estimating MMP developed by Wang and
e Pt. McIntyre fluid characterization. This
be as low as 4050 psi, resulting in a buffer
oRiGi'llk!aL
• 00
00
Please contact J. W. Groth (265-6846) or J. L. Hand (265-6036) if you have questions
or require additional information.
Sincerely,
J. L. Hand
cc: D. W. Bose (AAI)
M. P. Evans (ExxonMobil)
J. Hurliman (BPA)
ALASKA OIL AND GAS CONSERVATION COMMISSION
PUBLIC HEARING
In Re:
POINT McINTYRE OIL POOL ENHANCED OIL
RECOVERY PROJECT and WEST BEACH OIL POOL
SECONDARY RECOVERY PROJECT APPLICATION
FOR INJECTION AND AMENDMENT TO AREA
INJECTION ORDER NO. 4B.
APPEARANCES:
Commissioners:
TRANSCRIPT OF PROCEEDINGS
Anchorage, Alaska
January 12, 2000
9:03 o'clock a.m.
MS. CAMILLE OECHSLI
MR. DAVE JOHNSTON
METRO COURT REPORTING, INC.
550 West Seventh Avenue, Suite 1650
Anchorage, Alaska 99501
(907) 276-3876
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P R O C E E D I N G S
(On record 9:03 a.m.)
COMMISSIONER OECHSLI: Good morning. It's
about three minutes after 9:00 on January 12th. We're at the
Commission Office at 3001 Porcupine Drive. This hearing was
originally set for ARCO's application for injection and
amendment to area injection order number 4B with respect to the
Point McIntyre Oil Pool Enhanced Oil Recovery Project, and the
West Beach Oil Pool Secondary Recovery Project. The notice was
published on November 20, 1999, in the Anchorage Daily News for
this hearing.
Present at the head table: Dave Johnston, Cammy
Oechsli. Present in the room are John Groth, Mark Worcester
from ARCO, and Kristen Nelson from Petroleum News.
Are we prepared to proceed?
COMMISSIONER JOHNSTON: You've got to put on
record what the purpose of the hearing is.
COMMISSIONER OECHSLI: Purpose of the hearing
was for the ARCO's application.
COMMISSIONER JOHNSTON: Okay. Before we
I
proceed further, I would like to recuse myself from further
deliberations in these matters. And the reason for that is
that I have been advised by the Governor that I would not be
reappointed to the Commission so I am now serving my last few
days with this organization. Because of that, I think it would
METRO COURT REPORTING, INC.
550 West Seventh Avenue, Suite 1650
Anchorage, Alaska 99501
(907) 276-3876
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be inappropriate to be sitting in a decision-making matter
concerning an affair of a company who I will probably be
approaching for future employment opportunities. For that
reason, I think there would be an ethical violation if I was to
sit in judgment of a decision that is now pending before us.
And for that reason, I feel it appropriate that I recuse myself
from further deliberations in this matter.
MR. GROTH: Well, we have no objection.
COMMISSIONER OECHSLI: Is there anything
further you would like to take up before we go off record?
MR. GROTH: No, there's not.
COMMISSIONER OECHSLI: Okay. With that, we'll
go ahead and recess then until tomorrow morning at 9:00
o'clock.
(Off record 9:07 a.m.)
END OF PROCEEDINGS
METRO COURT REPORTING, INC.
550 West Seventh Avenue, Suite 1650
Anchorage, Alaska 99501
(907) 276-3876
COMMISSIONER
OECHSLI: On
Mr. Johnston's
request, we
no longer have a
quorum since
Mr. Christenson is
not here.
I apologize, Mr.
Groth, and Mr.
Worcester, for the
inconvenience.
If you have
no objection,
we could recess the
hearing now
and continue it
to tomorrow morning at 9:00
o'clock.
MR. GROTH: Well, we have no objection.
COMMISSIONER OECHSLI: Is there anything
further you would like to take up before we go off record?
MR. GROTH: No, there's not.
COMMISSIONER OECHSLI: Okay. With that, we'll
go ahead and recess then until tomorrow morning at 9:00
o'clock.
(Off record 9:07 a.m.)
END OF PROCEEDINGS
METRO COURT REPORTING, INC.
550 West Seventh Avenue, Suite 1650
Anchorage, Alaska 99501
(907) 276-3876
C E R T I F I C A T E
UNITED STATES OF AMERICA)
) ss.
STATE OF ALASKA )
I, Laura Ferro, Notary Public in and for the State of
Alaska, and Reporter for Metro Court Reporting, do hereby
certify:
That the foregoing Alaska Oil & Gas Conservation
Commission Public Hearing, was taken before me on the 12th day
of January 2000, commencing at the hour of 9:03 o'clock a.m.,
at the offices of Alaska Oil & Gas Conservation Commission,
3001 Porcupine Street, Anchorage, Alaska;
That the hearing was transcribed by me to the best of
my knowledge and ability.
IN WITNESS WHEREOF, I have hereto set my hand and
affixed my seal this 9th day of March 2000.
Notary Public in and for Alaska
My commission expires: 05/03/01
METRO COURT REPORTING, INC.
550 West Seventh Avenue. Suite 1650
Anchorage, Alaska 99501
(907) 276-3876
00
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Pt. McIntyre Oil Pool
Enhanced Oil Recovery Project
West Beach Oil Pool
Secondary Recovery Project
Application for Injection and Amendment to
Area Injection Order No. 4B
West Beach Testimony
January 12, 2000
January 12, 2000
1 16 1� 00 00
Table of Contents
SECTION A — TESTIMONY OF CARL E. LUNDGREN....................................................................... I
SECTION B — TESTIMONY OF MICHAEL R. MORGAN................................................................... 3
West Beach Secondary Recovery Project Application - Testimony
SII► � • � •
Section B — Testimony of Michael R. Morgan
Mr. Chairman, members of the commission, ladies and gentlemen, my name is Michael R.
Morgan. I am a Staff Petroleum Engineer with ARCO Alaska. I received a Bachelors of Science
Degree in Petroleum Engineering from the Colorado School of Mines in 1986. I've been
employed by ARCO since 1986 and have worked a variety of engineering projects. I have worked
in the Greater Pt. McIntyre Area on West Beach Pool development since February, 1996.
1 would like to be recognized as an expert witness.
During my testimony today I will provide information regarding West Beach operations and the
engineering aspects of the proposed West Beach Secondary Recovery Project.
West Beach Pool startup occurred in April 1993. The field has been delineated by eleven
penetrations consisting of seven wells and four sidetracks. Three wells currently are active, WB -
04, WB -05B and WB -06. Exhibit B-3 is a plat showing the location of West Beach area wells,
including the three active wells. Our recent efforts have focused on delineation and further
development of the West Beach reservoir, development of a secondary recovery plan, and
construction of additional surface infrastructure to handle anticipated additional production from
the West Beach reservoir.
Secondary recovery plans at West Beach include water injection utilizing locally sourced water
from Tertiary sands produced from a new well on the West Beach Pad. Reservoir simulation
studies indicate incremental recovery from waterflooding to be between 10 to 15%, of the
estimated 15-25 MMSTB original oil in place. Augmenting water injection with gas re-injection to
capture attic oil along the southern fault trap is also being evaluated. Thus, our application
requests authorization for both water and gas injection to enhance recovery from the West Beach
Pool.
The West Beach geologic model was updated in early 1998 to incorporate data from the West
Beach 5 (WB -05) and West Beach 5A (WB -05A) penetrations. Utilizing this new geologic
description and available data from area production and exploration wells, a detailed reservoir
simulation model was constructed. The objectives of the model study were to screen potential
development or delineation well locations and to evaluate secondary recovery options. Results
from the study indicated a peripheral waterflood, injecting into WB -06 and producing from WB -04
and WB -056, as the preferred development scenario, with estimated incremental recovery of 10-
15% of the original oil in place. The modeling study indicated that increased well density primarily
tended to accelerate the base reserve profile, with little incremental recovery. However,
waterflood performance data will be key to assessing additional development potential at West
Beach. Currently the minimum well spacing is 80 acres, which should accommodate potential
future drilling at West Beach.
Recent drilling, production and surveillance data from WB -04, WB -05B and WB -06 have validated
the modeling study and volumetrics. Post-fracture peak production from both WB -05B and WB -06
was initiated at 1700 STBOPD and 2487 STBOPD, respectively. Subsequently, production in
WB -05B has fallen to 829 STBOPD, primarily due to reduced reservoir pressures in the area due
to the increased offtake. The lower well rates and solution GOR of WB -05B make it difficult to
keep the well on-line due to paraffin build-up associated with cold flowing temperatures.
Production from WB -06 is currently at 800 STBOPD with associated gas of 11.2 MMSCFPD.
Reservoir pressure monitoring indicates good connectivity between the wells as evidenced by the
measured pressure drops of 500 to 750 psi following sustained production from all three wells.
West Beach Secondary Recovery Project Application - Testimony 3
00
These pressure drops are consistent with the reservoir model and confirm lateral connectivity
between wells. Lack of connectivity is a key risk to secondary recovery.
The West Beach waterflood involves conversion of WB -06 to injection service in the first quarter
of 2000. The conversion will be conducted in accordance with 20 AAC 25.412. The WB -07 source
water well (permit no. 199-106) will supply injection water with an electrical submersible pump
producing water from the Tertiary sands at a maximum rate of 10,000 BWPD and 2100 psi
surface pressure. This source water well is currently being drilled. Exhibit E-1 shows the
planned and potential completion intervals on the WB -01 shallow section log. A local water
sample from the target water source interval has not been obtained. However, it is anticipated
the water will be of similar composition to that produced from the GC -3 water wells as shown in
Exhibit M-1 from the April 5, 1993 "Application for Modification to Area Injection Order no. 4."
Electric log salinity calculations from the West Beach State #1 well indicate salinities of 20,000 to
40,000 ppm, which are consistent with the GC -3 water sample analyses and previous log
calculations.
Laboratory testing, core analyses and geochemical modeling indicate no significant problems with
clay swelling or in-situ fluid compatibility. Analysis of a sample of the West Beach 4 core in a
lower quality interval indicates significant amounts of clay (11%) may be present, primarily in the
form of Kaolinite. The presence of this clay may cause pore plugging in conventional
unstimulated producing wells at waterflood breakthrough. However, both West Beach producing
wells are hydraulically fracture treated, which will minimize fluid velocities and subsequent fines
movement in the rock near the producing wells and thus minimize the potential for producing well
formation damage. Calculations for WB -04 show the velocities are 280 times less for the
fractured completion compared to an unstimulated completion. No evidence of fines migration
was observed during the initial post -frac clean-up tests in any of the wells.
The Tertiary water is expected to contain excess barium at concentrations from 50 ppm to in
excess of 300 ppm. If uninhibited, barium sulfate scale could result when West Beach produced
water is mixed with Pt. McIntyre produced water containing excess sulfate (SO4) associated with
seawater breakthrough. However, the West Beach produced water stream will be inhibited
upstream of the Pt. McIntyre/West Beach commingling point to prevent BaSO4 precipitation.
Because West Beach has not produced any formation water, reservoir compatibility modeling and
laboratory testing assumed a water composition similar to that of the Pt. McIntyre pool.
Initially, the waterflood will be managed to replace reservoir voidage. As the flood progresses,
injection rates will be adjusted in response to producing well surveillance and performance.
New facilities installed and in service on the West Beach pad include a central manifold designed
to collect production from four initial wells and five additional wells. The pad will also have a new
chemical injection skid and a new electrical distribution skid. A new 12" pipeline has been
installed from the West Beach pad to drill site L1 to handle increased production rates.
Additionally, a 4" high pressure line has been installed that will be used to supply lift gas to the
pad. The line has been designed to accommodate high pressure gas or miscible injectant if
additional pressure maintenance or tertiary recovery can be justified. The existing 6" production
line will be converted to a dedicated test line.
To facilitate initiating production from the WB -05B and WB -06 wells, design and material
procurement for the facility expansion occurred prior to drilling the wells. Consequently, sizing
considered the low incremental cost for additional slots and various future development
scenarios, including potential additional drilling for West Beach or other GPMA fields. Waterflood
performance data will be key to assessing additional development potential at West Beach.
West Beach Secondary Recovery Project Application - Testimony
0• 00
ALASKA OIL AND GAS CONSERVATION COMMISSION
PUBLIC HEARING
January 12,2000
9:00 AM
PtMcIntvre/WBeach
NAME — AFFILIATION TELEPHONE Do you plan to testify?
Yes No
(PLEASE PRINT)
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ALASKA OIL AND GAS CONSERVATION COMMISSION
PUBLIC HEARING
In Re:
POINT McINTYRE OIL POOL ENHANCED OIL
RECOVERY PROJECT and WEST BEACH OIL POOL
SECONDARY RECOVERY PROJECT APPLICATION
FOR INJECTION AND AMENDMENT TO AREA
INJECTION ORDER NO. 4B.
TRANSCRIPT OF PROCEEDINGS
Anchorage, Alaska
January 13, 2000
9:03 o'clock a.m.
APPEARANCES:
Commissioners: MR. ROBERT N. CHRISTENSON, CHAIRMAN
MS. CAMILLE OECHSLI
METRO COURT REPORTING, INC.
550 West Seventh Avenue, Suite 1650
Anchorage, Alaska 99501
(907) 276-3876
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P R O C E E D I N G S
ME
(On record 9:03 a.m.)
CHAIRMAN CHRISTENSON: I would like to call
this meeting to order. The purpose of the hearing is a request
by ARCO on the Point McIntyre/West Beach Oil Pools for request
authority to initiate miscible gas injection tertiary oil
recovery.
And it's about a little after 9:00. We are at 3001
Porcupine Road, and we will be reconvening the hearing that
began yesterday.
The Commission will receive both sworn and unsworn
testimony. However, in our deliberations, we would like to
notify you that you will -- we will give more credit to -- in
our deliberations to sworn testimony.
This will be recorded, and if you would like a
transcription of these proceedings, please contact Metro Court
Reporting Company.
Persons wishing to testify need to sign in. And
there's a list. Cammy's got the list or somebody's got the
list here.
COMMISSIONER OECHSLI: It's being passed
around.
CHAIRMAN CHRISTENSON: So please sign in. If
you wish to give expert testimony, then please ask us about
that and we will listen to your qualifications and then we will
METRO COURT REPORTING, INC.
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rule on whether it will be admissible as expert witness.
After the original presentation, we will accept
testimony from those in the public who are present, and we will
also accept written testimony.
I think that's about it. Oh, the Notice was published
in the Anchorage Daily News. I think that was the only paper
that we did it in.
So I think we are ready for the presentation of the
testimony. So, ARCO, would you care to begin and be sworn in,
if you so wish?
MR. GROTH: Would -- my name is John Groth.
Would you prefer to swear each of us in individually or.....
CHAIRMAN CHRISTENSON: Yeah.
MR. GROTH: .....collective? Okay.
CHAIRMAN CHRISTENSON: Would you raise your
right hand?
(Oath administered)
MR. GROTH: I do.
19!1 CHAIRMAN CHRISTENSON: Okay. Please be seated.
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20,! MR. GROTH: Mr. Chairman, Commissioner, my name
2111 is John Groth. I am a supervisor with ARCO Alaska. I hold a
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221!1' Bachelors of Science Degree in Chemical Engineering from Rice
231' University. I've been employed by ARCO since 1977 in a variety
241!1 of positions, and I've supervised the Greater Point McIntyre
2511 area development support effort since 1995. I would like to be
METRO COURT REPORTING, INC.
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(907) 276-3876
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recognized as an expert witness.
CHAIRMAN CHRISTENSON: Okay. Do you have any
questions?
COMMISSIONER OECHSLI: I have no objection.
CHAIRMAN CHRISTENSON: Okay. No objections.
Please proceed.
MR. GROTH: ARCO Alaska is presenting testimony'
in support of the application to amend area injection order
number 4, and the pool rules for the Point McIntyre__and West
Beach fields. ARCO presents this testimony on behalf of the
Point McIntyre working interest owners: ARCO, BP Amoco, and
Exxon Corporation, and on behalf of the West Beach working
interest owners, ARCO and Exxon.
The testimony is divided into four parts. For the
Point McIntyre EOR project, John Hand will describe the
reservoir engineering aspects, and Murray Athans will describe
the facility additions and modifications which are required.
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For the West Beach water floor project, Carl Lundgren
will describe the geologic aspects, and Mike Morgan will
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describe the reservoir and facility aspects.
Each witness is prepared to respond to questions
II
concerning his testimony and related exhibits. For the
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convenience of the Commission, we have available the text of
the testimony and copies of the exhibits.
We -- there is a matter of confidentiality that I would
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like to address. There are a number of exhibits -- number of
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aspects of the West Beach portion of the application, exhibits,
and testimony, we plan to give today that contain commercially
sensitive confidential information. We believe that this
information is useful background information for the
Commission, but it's disclosure is not required for the public
to understand or comment on the matter before us today. Those
items are. In the application dated November 8, 1999, Exhibit
F-1, Exhibit F-2; in the supplement dated December 16, 1999,
Figures S-4, S-5, S-6, S-7, S-8, S-9; and with regard to
today's testimony, the oral testimony of Carl Lundgren; and
figures S-10, S-11, and S-12. And we request confidentiality
of these items at this time.
CHAIRMAN CHRISTENSON: I think before we get to
the testimony, we can go into executive session, right? And
listen to that. With respect to the items, you will submit
these as confidential?
MR. GROTH: The.....
CHAIRMAN CHRISTENSON: .....items right now?
MR. GROTH: Yes, we can.
CHAIRMAN CHRISTENSON: Okay with you?
COMMISSIONER OECHSLI: Yeah.
(Off record comments)
MR. GROTH: I think we've got a matter with BP
folks as well on the West Beach items.
METRO COURT REPORTING, INC.
550 West Seventh Avenue, Suite 1650
Anchorage, Alaska 99501
(907) 276-3876
(Off record comments)
COMMISSIONER OECHSLI: Do you want to take a
break?
CHAIRMAN CHRISTENSON: Do you want to take a
break to figure this out? Or we can start now.
COMMISSIONER OECHSLI: Let me just ask a
question. With respect to the order of information, were you
going to do the Point McIntyre information all first and then
do West Beach?
!.No
MR. GROTH: Yes.
COMMISSIONER OECHSLI: Do any of these exhibits
relate to that? They don't, do they?
MR. GROTH: None of these exhibits that we just
mentioned relate to the testimony with regard to Point
McIntyre.
COMMISSIONER OECHSLI: Do you want to do the
first part of the Point McIntyre? Do that first and then we
can address the West Beach.
CHAIRMAN CHRISTENSON: Are you guys set up to
do that?
that
MR. GROTH: Yes, we are set up to do that.
CHAIRMAN CHRISTENSON: Okay. Why don't we do
COMMISSIONER OECHSLI: Why don't we do that.
MR. GROTH: Okay.
METRO COURT REPORTING, INC.
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CHAIRMAN CHRISTENSON: Let's do Point Mac
first.
MR. GROTH: Unless there are any other
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questions at this time.....
CHAIRMAN CHRISTENSON: I don't have any.
MR. GROTH: .....I'll turn the podium over to
I John Hand.
CHAIRMAN CHRISTENSON: Okay.
COMMISSIONER OECHSLI: John, do you have copies
of all those packages for us?
MR. HAND: Here's the original testimony.
CHAIRMAN CHRISTENSON: Do you wish to be sworn
in?
MR. HAND: Yes.
CHAIRMAN CHRISTENSON: Please raise your right
hand.
(Oath administered)
MR. HAND: Yes, I do.
CHAIRMAN CHRISTENSON: Do you wish to be
considered an expert witness?
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MR. HAND: Yes, I do.
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CHAIRMAN CHRISTENSON: Would you please tell us
about your qualifications?
MR. HAND: Mr. Chairman, members of the
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Commission, ladies and gentlemen, my name is John L. Hand. I
i
METRO COURT REPORTING, INC.
550 West Seventh Avenue, Suite 1650
Anchorage, Alaska 99501
(907) 276-3876
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am the Subsurface Development Team Leader for the Point
McIntyre Field. The Subsurface Development Team is a multi-
company, multi -disciplinary team established by the owner
4'i companies. This team is responsible for the ongoing reservoir
5i management activities of the Point McIntyre Field. These
6'' activities include, but are not limited to, development
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drilling, reservoir surveillance, production/injection
scheduling, and hydrocarbon miscible EOR evaluation and
implementation.
I received a Bachelors of Engineering Degree in
Chemical Engineering with Honors from the University of New
South Wales in Sydney, Australia, in 1987, and a Degree of
Doctor of Philosophy in Petroleum Engineering also from the
University of New South Wales, Sydney, Australia, in 1991. I
have been employed by ARCO since 1990 and have worked on a
variety of reservoir engineering projects both at ARCO
Exploration and Production Technology and ARCO Alaska,
181' Incorporated, as well as a number of field development planning
19'' assignments at ARCO Alaska, Incorporated. I worked in the
20 Greater Point McIntyre Area in my current position since
21' September of 1997.
22 I would like to be recognized as an expert witness.
23: CHAIRMAN CHRISTENSON: Do you have any
24 objections?
25.: COMMISSIONER OECHSLI: No, I don't.
METRO COURT REPORTING, INC.
550 West Seventh Avenue, Suite 1650
Anchorage, Alaska 99501
(907) 276-3876
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proceed.
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CHAIRMAN CHRISTENSON: No objections. Please
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MR. HAND: During my testimony today, I will
provide information regarding current Point McIntyre field
operations as well as the reservoir engineering aspects of the
proposed Point McIntyre enhanced oil recovery project.
Point McIntyre Pool startup occurred in October of
1993. Current operations involve a combination of processed
gas reinjection and 80 -acre inverted nine -spot pattern
waterflooding for pressure maintenance. Gas reinjection into
the gas cap began concurrent with field startup, with water
injection beginning in July of 1994. As of January 1, 1999,
fifteen water injectors and one gas injector provided pressure
support to the reservoir, maintaining an average reservoir
pressure at the original pressure of approximately 4,370 psi.
Source water, from the seawater treatment plant, is currently
used for the Point McIntyre waterflood.
Point McIntyre production is processed at the Lisburne
Production Center, the LPC. Field oil production reached a
facility -constrained plateau of 165,000 barrels of oil per day
during the second quarter of 1996, and this nominal rate was
maintained until the third quarter of 1997. Oil production has
since declined due to increasing water cuts at Point McIntyre
and water handling constraints at the LPC.
To enhance recovery at oil -- of oil at Point McIntyre,
METRO COURT REPORTING, INC.
550 West Seventh Avenue, Suite 1650
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(907) 276-3876
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1 the working interest owners, ARCO, BP Amoco, and Exxon
2 Corporation, have approved a hydrocarbon miscible EOR project.
3 Planned startup for MI injection is the first half of 2000.
4 Exhibit B-1 is a plat showing the location of all
5 existing injection wells, production wells, abandoned wells,
6 dry holes, and any other wells within the Point McIntyre Pool
7 as of June 1, 1999. The current Point McIntyre water and
8 potential miscible solvent injector locations are identified in
9 the plat shown in Exhibit B, and are also tabulated in Exhibit
10 B-2.
11 Seventy-four wells have been drilled in Point McIntyre
12 Pool through January 1, 1999, not including P and A'ed wells.
13 The two Point McIntyre drill sites, PM1 and PM2, have
14 production, water injection, and gas lift facilities in place.
15 Drill site PM1 also has gas injection facilities in place.
16 Ultimate well count at Point McIntyre is envisioned to be as
17 high as 86 wells, not including P&A'ed wells, depending on the
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18i number of 80 -acre infill wells and the extent of peripheral
19i development. Present estimates are that drill site PM1 will
20 ultimately have 20 to 23 wells, including four water injectors
21 and one gas injector, and that drill site PM2 will ultimately
22 have 53 to 62 wells, including 10 to 13 water injectors. An
23 additional water injector, P1-25, is located at the West Dock
24 staging area.
25 All Point McIntyre water injection wells are completed
METRO COURT REPORTING, INC.
550 West Seventh Avenue, Suite 1650
Anchorage, Alaska 99501
(907) 276-3876
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with L-80 grade steel. All tubing jewelry is completed with
Chrome Moly, which is compatible with both L-80 and 13 Chrome.
Point McIntyre water injection completions are designed as a
single zone, single string with a single packer. Exhibits G-1
through G-5 show typical wellbore schematics for the five basic
well completion designs.
The current waterflood pattern configuration for the
Point McIntyre Pool is an inverted nine -spot. This pattern
selection provides maximum flexibility for potential future
conversions to other pattern configurations, as well as in
reservoir description and/or -- as changes in reservoir
description and/or performance dictate. Additional drilling
within the EOR project area may be undertaken to improve sweep
in areas of the reservoir unaffected by the hydrocarbon
miscible EOR process and to result in the recovery of oil from
areas and reservoir volume not otherwise affected by the
implemented tertiary recovery activities. Future development
plans will be based on field performance, including the
performance of the patterns already receiving MI. There are no
plans to reduce the well density below 40 acres.
A surveillance program to monitor the Point McIntyre
EOR flood performance is in place, and is based on experience
of operating similar projects at the Prudhoe Bay and Kuparuk
Fields. This program will be used to monitor field performance
for field management and additional development opportunities.
METRO COURT REPORTING, INC.
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The Point McIntyre EOR project involves the eventual
conversion of the existing 15 waterflood injectors, and
potentially any future water injectors to water -alternating -
gas, or WAG, service. Water will be injected alternatively
with MI in the WAG injection wells to improve the MI sweep in
the reservoir. At startup of the EOR project, water injection
is anticipated to be approximately 250,000 barrels of water a
day. Not all of the patterns will be receiving MI
simultaneously. THOse patterns not initially converted to WAG
injection will remain on continuous water injection until MI is
available.
Source water is currently used for the Point McIntyre
waterflood. It is anticipated that the same injection water
will be used during the initial stages of the EOR project.
Conversion from source water injection to produced water
injection is possible in later stages of the flood. Both of
these water sources have been approved for injection into the
Point McIntyre reservoir under Area Injection Order 4B.
Currently, injection of an MI slug of 35 percent of
hydrocarbon pore volume is planned. The maximum size of the MI
slug for the project is limited by the rate of delivery of MI
manufactured at the LPC. Exhibit S-1 shows the relationship
between miscible injectant slug size and incremental oil
recovery for the Point McIntyre Enhanced Oil Recovery Project.
MI generated at the LPC is expected to be delivered to
METRO COURT REPORTING, INC.
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Point McIntyre at a nominal 50 million standard cubic feet per
day. Exhibit S-2 shows the predicted incremental oil
production rates for the Point McIntyre Enhanced Oil Recovery
Project for the next 23 years for the miscible gas injection
rate of 50 million standard cubic feet per day. Exhibit S-3
shows the projected field oil production rates for the Point
McIntyre base, primary and secondary, and a base plus EOR for
the 50 million standard cubic foot case for this same period.
Under the planned scope, the LPC MI supply will be limited,
requiring the staging of MI injection into existing patterns as
MI becomes available. Initially, two patterns will receive MI
injection. As EOR patterns mature, the availability of excess
MI will allow additional patterns to begin receiving MI.
Nominally, two patterns will be receiving MI at any one time
during the life of the project. It will take around 15 plus
years for the last pattern to receive its first MI slug. Peak
incremental oil rate is expected to exceed 5,000 barrels per
day as a result of the project.
Current Point McIntyre operations, processed gas
reinjection and pattern waterflooding, are expected to yield an
estimated total recovery of approximately 42 to 45 percent
original oil in place for the Point McIntyre Pool. The planned
hydrocarbon miscible EOR project at Point McIntyre is estimated
to increase oil recovery for an additional 32 million stock
tank barrels of oil, or approximately six percent of the
METRO COURT REPORTING, INC.
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original oil in place in the current 15 waterflood patterns.
The existing waterflood patterns contain varied
reservoir quality with incremental oil recovery estimates
ranging from four to eight percent of original oil in place of
the targeted oil column under a hydrocarbon miscible EOR
process. These estimates are based on analysis of core from 20
wells distributed around the field, detailed field wide
stratigraphic correlations, PVT and fluid displacement
laboratory studies, and fine scale fully compositional fluid
flow reservoir simulations tied back to the laboratory data.
The fine scale results were subsequently scaled up to the field l'
wide scale, with the estimated incremental oil recovery for the
waterflood area determined using the Point McIntyre Full Field
reservoir simulation model.
MI for the Point McIntyre EOR project will be
manufactured at the LPC from a mixture of produced fluids from
the Point McIntyre, West Beach, North Prudhoe Bay, Nuyakuk, and
Lisburne Pools. Based on the current operating practice of
injecting processed natural gas from the LPC into Point
McIntyre reservoir, and given that the injected MI comprises
the same hydrocarbon components in a more concentrated form, no
compatibility problems are anticipated.
The miscibility pressure criteria planned for the EOR
project is designed to maximize oil recovery and miscible
injectant utilization for an MI -limited project. The minimum
METRO COURT REPORTING, INC.
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enrichment level for the Point McIntyre miscible injectant was
determined from standard laboratory PVT and slim -tube
displacement experiments. The blended MI will have a minimum
miscibility pressure of approximately 4,350 psi. The expected
composition is given in Exhibit H-1.
Injection and production at the Point McIntyre field
are managed to maintain the average reservoir pressure at the
original reservoir pressure of approximately 4,370 psi. There
are no plans to change this reservoir management philosophy.
Reservoir pressure monitoring is performed in accordance with
Rule 12 of Conservation Order 317A and reported annually to the
Alaska Oil and Gas Conservation Commission in the Point
McIntyre Oil Pool Annual Reservoir Report.
The constant reservoir pressure with temperature along
with ne- -- excuse me. The constant reservoir pressure with
time along with negligible temperature variations across the
field mean that miscibility pressure requirements are not
expected to change as a result of reservoir conditions during
the life of the EOR project. Similarly, the compact nature of
the Point McIntyre waterflood/EOR patterns exhibit negligible
differences in reservoir conditions across the field. The
minimum miscibility pressure/minimum miscibility enrichment
evaluations for the project were performed at reservoir
temperature, 185 degrees Fahrenheit. The thermal temperature
bulb at Point McIntyre, due to source water injection, should
METRO COURT REPORTING, INC.
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1' provide an MMP buffer, but the project design was developed
2' without including this factor. Taken together, these factors
3, reduce the need for a large MMP buffer compared to other North
4 Slope EOR projects.
5The projected potential maximum miscible injectant rate
6 under the current scope is 70 million standard cubic feet per
12
1 day. Expanding the Point McIntyre Enhanced Oil Recovery
Project by increasing miscible gas injection rate beyond the
current scope would require an external source of enriching
components for the manufacturing the additional miscible
injectant. This is a technically viable option and was part of
the initial scoping studies for an EOR project at Point
McIntyre. However, when this initial evaluation indicated less l
14' favorable economics for this option, subsequent studies focused
15; on self -generating MI project options. These studies resulted
16. in the owner decision to approve the funding of the project
17'' described in the testimony today. Analyses to investigate the
18 benefits of a miscible gas injection rate of up to 150 million
19 standard cubic feet per day are being evaluated and will be
20 based on the field performance under the current scope. Such a
21 rate would require an external source of enriched miscible
22 injectant, as well as additional drill site facilities and
23 incremental capital expenditures.
24 That concludes my prepared testimony. Thank you.
25 CHAIRMAN CHRISTENSON: Cammy, do you have any
METRO COURT REPORTING, INC.
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1 questions?
2 COMMISSIONER OECHSLI: I don't.
3 CHAIRMAN CHRISTENSON: I've got a couple of
4 questions. With regard to the miscible injectant, you said you
5 don't have as much as you could use. How much more recovery
6 could you get if you had a miscible injectant that you wanted?
7 MR. HAND: When we initially did the screening
8 studies for the Point Mac EOR, we looked at a variety of
9 alternatives. And it was found that there were less -- the
10 expansions were less favorable and so we focused more on the
11 LPC or inhouse MI generating options. From that point on, we
12 followed and developed the technical work based on the scope of
13 the current plan project. We do not really have a -- we did
14 not develop the technical work to a similar caliber for the
15 other cases so we do not really have a similar caliber benefit
16 stream for a larger slug or larger MI volume. But as mentioned
17 in my testimony, we do plan to evaluate that as we get a field
18 performance back from out initial patterns that we put on MI
19 injection.
20 CHAIRMAN CHRISTENSON: What about -- did you
21 mention early in the testimony that you had limits on the
221 processing capacity, water processing capacity and LPC, that's
231 holding you up as well? Or did I get that wrong?
24� MR. HAND: We talked about -- in the testimony
I,
251 all I talked about was the expected water injection volumes at
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the time of MI.
CHAIRMAN CHRISTENSON: Okay. Well, somewhere I'
thought I heard that there was a limitation on that.....
MR. HAND: Oh, right.
CHAIRMAN CHRISTENSON: .....processing
capability.
MR. HAND: Right.
CHAIRMAN CHRISTENSON:
MR. HAND: Right.
CHAIRMAN CHRISTENSON:
in this project?
In LPC, right?
Are you addressing that
MR. HAND: I -- I feel that pro- -- I'm
probably not the best person to answer that question. Maybe
Murray Athans will be able to answer that when he talks about
the facility -- facilities at Point McIntyre or the LPC in
relation to this project.
CHAIRMAN CHRISTENSON: Okay. So what you're
going to do is in the initial phases, you're going to see how
effective this MI is under the current project, and then you'll
evaluate whether it would be advantageous to acquire additional
MI for -- if it looks like that would be cost-effective. Is
that correct?
MR. HAND: That is correct. That is correct.
CHAIRMAN CHRISTENSON: But any of that would
have to come from another facility. Have I got that right?
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MR. HAND: Yes. We would acquire an external
source of miscible injectant or enriched hydrocarbon components
to make miscible injectant. Yes.
CHAIRMAN CHRISTENSON: Thanks. Anything else,
Cammy?
COMMISSIONER OECHSLI: I don't.
CHAIRMAN CHRISTENSON: Thank you very much.
MR. HAND: Thank you.
MR. ATHANS: Good morning. My name is Murray
Athans.
CHAIRMAN CHRISTENSON: Would you like to be
sworn in, sir?
MR. ATHANS: Yes, I would.
CHAIRMAN CHRISTENSON: Please raise your right
hand.
(Oath administered)
MR. ATHANS: I do.
CHAIRMAN CHRISTENSON: Do you wish to be
considered an expert witness?
MR. ATHANS: Yes, I do.
CHAIRMAN CHRISTENSON: Would you present your
qualifications, please?
MR. ATHANS: Mr. Chairman, members of the
Commission, ladies and gentlemen, my name is Murray P. Athans.
I am the ARCO Project Engineer for the Point McIntyre EOR
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1 project. In this role, my job responsibilities have included
2I facility design, oversight and review, and acting as the
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3 1 primary coordinator between the engineering contractor and the
4) Lisburne Production Center, LPC, Operations Team. It has been
5my job to insure that the new facilities are fit for their
6 intended purpose, are built to ARCO Alaska standards, and meet
7 all operating and safety design requirements.
8 I received a Bachelors of Science Degree with Honors in
9 Chemical Engineering from the University of Texas at Austin in
10 1978, and a Masters of Science Degree in Chemical Engineering
11 from the University of Texas at Austin in 1980. I began work
12 for ARCO at the Exploration and Production Research Center in
13 Plano, Texas, in 1980, then transferred to ARCO Alaska in 1984.
141 Since arriving in Alaska, I have worked in a broad variety of
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151 facility planning and process engineering positions within the
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17� Greater Point McIntyre Area in August 1997, at which time I
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181 began my current assignment as Project Engineer for the Point
1911 McIntyre EOR project.
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20!I would like to be recognized as an expert witness.
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21I CHAIRMAN CHRISTENSON: Thank you.
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2211 COMMISSIONER OECHSLI: I have no objection.
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2311 CHAIRMAN CHRISTENSON: No objection. Please
24: proceed.
251, MR. ATHANS: Okay. During my testimony today,
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I will provide an overview of the facility modifications and
additions which are being installed to implement the Point
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McIntyre EOR project. I will also briefly discuss some of the
project facility considerations that impacted the miscible
injectant rate projections previously discussed by John Hand.
Vapors generated in the LPC NGL, natural gas liquids,
plant downstream from the feed flash drum, which are currently
being injected as residue gas, will provide the enriching
components for the MI solvent stream. Facility modifications
are designed to ensure that the volume of blendable NGLs
extracted at the LPC will not be impacted by the EOR project.
Manufacture of MI at the LPC at a greater rate than planned for
the project would adversely impact NGL production.
The nominal annual average MI manufacturer rate is
expected to be 50 million cubic feet per day. During the
summer months, we expect to see an MI manufacture rate lower
than winter months due to reduced NGL refrigeration capacity
resulting from higher ambient temperatures. In the first four
to five years of the project, MI rates during the summer are
expected to range between 42 to 45 million cubic feet per day,
while in the winter ranging between 52 to 53 million cubic feet
per day. After four to five years, MI rates should be
consistently in the 50 million cubic feet range, with peaks as
high as 60 to 70 million cubic feet per day. Peak rates --
peak rate estimates are based in part on predictions of the
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volumes of return miscible injectant, MI.
The primary factors limiting the amount of MI
manufacture at LPC are the LPC piping and vessel metallurgical
limit of minus 50 degrees Fahrenheit, per ASME codes, and the
plant refrigeration capacity. The new chiller installed as
part of the project was sized to utilize the existing excess
refrigeration capacity, propane system, at the LPC. Increasing
refrigeration capacity would require significant incremental
capital.
Modifications at the LPC during 1999 and early 2000 in
support of the Point McIntyre EOR project include the
installation of an MI compressor, a second chiller, new
compressor coolers and blending station, and an upgrade of the
LPC NGL plant liquid piping. MI will be transported to the
Point Mac drill sites via a new distribution pipeline shown in
Exhibit A-1 using currently installed vertical support members.
The EOR project will also require installation of drill site
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distribution piping.
Hydrogen sulfide, H2S concentrations, during the life
of the project are expected to remain low. The equipment being
installed is designed to handle the expected H2S
concentrations. we will continue to observe existing H2S
safety precautions.
The estimated maximum and average injection pressures
anticipated for the Point McIntyre enhanced recovery projects
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are listed in the following table. These pressures represent
pump discharge pressures.
The estimated maximum injection rates for Point
McIntyre enhanced recovery wells will not initiate or propagate
fractures through the confining strata, and, therefore, will
not allow injection or formation fluid to enter any freshwater
strata. All field data collected to date indicate that
injection in the current water injectors and the single gas
injector at Point McIntyre has been confined to the injection
strata. It is our expectation that the injected MI will remain
confined to the injection strata.
Existing water injection operations in the Point
McIntyre Pool Kuparuk River Formation have been above formation
parting pressure to improve recovery of oil. In no instance
have such injection pressures breached the integrity of the
confining zone.
This concludes my testimony.
CHAIRMAN CHRISTENSON: Cammy, do you have any
questions?
COMMISSIONER OECHSLI: I don't.
CHAIRMAN CHRISTENSON: Could you answer the
question with regard to the limit on the facilities?
MR. ATHANS: Yes. Again, as I discuss in here,
there are basically two primary factors that limit our MI rate
to about the 50 million cubic foot per day number.
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And, again, the first one is our metallurgical
temperature limit on our piping. All of our piping is only
rated by code down to minus 50 degrees Fahrenheit. So per
code, we cannot go below minus 50 on the piping. You know,
safety issue.
And then secondly is we had some excess propane
refrigeration capacity at the LPC already existing. And what
we did with this project was we added a second chiller to
basically, you know, use up that excess capacity so that we've
sized that chiller such that it will efficiently use the rest
of our capacity.
And so basically those are the two things, our
metallurgical temperature limit, and then now we are using up
all the excess capacity. To go beyond that would have required
very significant capital cost additions which we didn't judge
to be economic. So those are the two primary factors that
limit our rate.
CHAIRMAN CHRISTENSON: Is there anything else
that limits your rate? Is there a water handling problem?
MR. ATHANS: No. Water handling really -- I
mean that may limit our production rate but that really doesn't
affect the MI rate.
1 CHAIRMAN CHRISTENSON: I know but does it
I affect the rate of this EOR project?
MR. ATHANS: No. No, because we're already --
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you know, we already have -- that really doesn't affect the
amount of the MI components that we're going to be able to
remove again. The temperature limits and the refrigeration
limits are really what affect that, and water is really a
separate issue.
25
MR. GROTH: May I?
CHAIRMAN CHRISTENSON: Yeah, John.
MR. GROTH: To the extent that, you know, water
handling.....
(Witness walks up to microphone)
MR. GROTH: To the extent that the water
handling capacity in and of itself has an effect upon the
recovery for the EOR project, the answer would be limited. But
to the extent the water handling capacity in and of itself has
an impact on the ability of all of the fields within the
Lisburne GPMA production system to produce, if you've got a
higher water handling capacity within the plant, well, yes.
There would be a higher through put rate associated with all
the fields, and there would be instantaneous increases in
production associated with that.
CHAIRMAN CHRISTENSON: So it does have an
overall effect then in -- I mean you could produce more if you
had more water handling capacity?
MR. GROTH: On an instantaneous basis, yes.
MR. ATHANS: It starts to get pretty technical
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though because if we're all -- I think what John is saying is
we could produce more total gas if we could also produce more
total oil but, again, it really begins to get complex then as
to whether if we're already using all of our refrigeration
capacity, those few extra components that we would bring in
with the gas, you may or may not, depending on where you are in
the life of the project, be able to capture those and
efficiently use those. So it's not a, you know -- I don't
think the affect is large at all. The fact that, you know, if
we had a little more water handling capacity, I don't think you
would see a tremendous increase in the MI rate.
CHAIRMAN CHRISTENSON: Okay. Thanks.
MR. GROTH: That does conclude our testimony
for the Point McIntyre portion of the application.
CHAIRMAN CHRISTENSON: Okay. Thank you.
COMMISSIONER OECHSLI: Do you want to take a
break at this point?
CHAIRMAN CHRISTENSON: Yeah. Let's take a 10
minute break at this point, then we'll reconvene.
(Off record 9:42 a.m.)
(On record 10:08 a.m.)
CHAIRMAN CHRISTENSON: Let's reconvene. John,
we have one more question that came up in our discussions. It
relates to the buffer between MMP and reservoir pressure. And
we would like to know what you all think the -- in terms of
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some general parameter there how much that temperature is going
to affect that buffer. You're talking about 20 psi between MMP
and reservoir pressure. And then you also talked about how the
temperature was going to give you a wider margin. We would
like to hear your comments on what you think that's going to
be, how much help you're going to get out of that? And our
reasons are because we've heard a lot in other discussions with
regard to that where you're looking at a 100 to 150 psi buffer.
MR. HAND: The average reservoir pressure that
we try and maintain the reservoir at, we talk about is a normal
4370. We take pressures every year and report that to the
Commission, and other than the first eight months of production
which we were not -- didn't have any water injection, we've
actually probably normally kept it above that. And we monitor
that pressure every year. We report that every year and
monitor our pressure, with sag bottom hole pressures or flowing
bottom hole pressures, right throughout the year. So it
generally is a little higher than 4370 so that press- -- that
type of pressure buffer is a little higher.
20ii With regards to the temperature effect, the lower
21:! temperature reduces the requirement of enrichment and so,
22'therefore, gives a larger effective minimum miscibility
23'L pressure buffer. We -- I could -- at this point in time, I
241 could not give you the exact number of what that buffer would
25' be. We can get -- we can report back to you on that if
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required.
CHAIRMAN CHRISTENSON: I don't think we're so
much interested in a specific number as sort of a range. What
do you expect to get in terms of overall benefit out of that?
MR. HAND: You would.....
CHAIRMAN CHRISTENSON: Because you said
you.....
8' MR. HAND: You would get a -- for the given
9 enrichment we have, it would essentially represent a slight
10 overenrichment of the MI. And so it would be less of a concern
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11 of losing miscibility. It basically is essentially the same
12affect as increasing the pressure buffer that you have in the
13 field. So your miscibility will be met. You have less concern
14111 about losing miscibility.
151 CHAIRMAN CHRISTENSON: Yeah. Can you
it
161, equivocate that to -- is that like going to be like a 50 psi
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1711 buffer or a 100 psi buffer or what?
MR. HAND: I really couldn't.....
19 j1 CHAIRMAN CHRISTENSON: We're not looking for
20! specific numbers here.
21 MR. HAND: Yeah.
22; CHAIRMAN CHRISTENSON: Just if you could give
23,11 us an idea so we would have some idea relative to other things
24 we know about.
251'1 MR. HAND: I really couldn't give you a
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definite answer on that. I would have to get back to you on
that one.
CHAIRMAN CHRISTENSON: That's fine.
MR. HAND: I will calculate that for you.
CHAIRMAN CHRISTENSON: Okay. Do we have any
other questions?
29
COMMISSIONER OECHSLI: No.
CHAIRMAN CHRISTENSON: All right. John.
MR. GROTH: May I -- one -- I guess a couple
points of clarification on the water handling capacity
question. I think we've got amongst ourselves a better
understanding of what you were driving for there.
The facility limits at the LPC are integrated and have
implications upon each other. So you can have gas handling
constraints. You can have water handling constraints. Within
the GPMA system, there may be hydraulic constraints within
certain common lines that feed into the LPC. We tend to look
at that system as a whole. And in the past, water handling has
been a constraint. Gas handling may have been a constraint.
Oil processing capacity within the system has been a
constraint. Those are things that we have looked at and will
continue to look at to see if there are opportunities to de -
bottleneck those. With the initiation of miscible injectant
operations, that's another constraint that is now into the
system but it will be integrated and will be part of our
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ongoing evaluations to see if there are any opportunities to
de -bottleneck the system as appropriate.
CHAIRMAN CHRISTENSON: I noted that you said
instantaneous value. So I guess the implication of that is
that you don't expect -- even if you would find some things you
wouldn't expect an increase in overall recovery. It just --
it's a timing situation whether you get it now or whether you
get it later.
MR. GROTH: I think there are elements of
additional recovery that may come with a particular de-
bottlenecking opportunity. But we look at both the
instantaneous rate benefit and the additional recovery benefits
associated with those to determine if that particular
opportunity is economical. But the instantaneous rate benefit
associated with those typically is a -- the larger portion of
the benefits.
CHAIRMAN CHRISTENSON: I think that clears it
up for us. Let's see, at this time, is there any public
testimony with regard to Greater Point Mac? We're going to try
to split this up into the confidential and non -confidential
issues. So we would like to wash out the Point Mac question.
Are there any other testimonies or comments with regard to
Point Mac? And then we'll move on to the confidential session.
Seeing none, we need to go into confidential session.
So, John, do you want to help me out here and see who would
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need to -- besides Kristen. Are there others? Thank you,
Kristen.
2884
(Meeting adjourned to go into executive session)
4415
31 1
(Public hearing reconvened)
CHAIRMAN CHRISTENSON: Good morning.
MR. MORGAN: Good morning. My name is Michael
Morgan. I would like to be sworn in.
CHAIRMAN CHRISTENSON: Okay, sir. Raise Your
right hand.
(Oath administered)
MR. MORGAN: I do.
CHAIRMAN CHRISTENSON: Do you wish to be
considered an expert witness?
MR. MORGAN: Yes, I do.
CHAIRMAN CHRISTENSON: Okay. Would you proceed
with your qualifications?
MR. MORGAN: Mr. Chairman, members of the
Commission, ladies and gentlemen, my name is Michael R. Morgan.
I am a Staff Petroleum Engineer with ARCO Alaska. I received a
Bachelors of Science Degree in Petroleum Engineering from the
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Colorado School of Mines in 1986. I have been employed by ARCO
since 1986, and have worked a variety of engineering projects.
I have worked in the Greater Point McIntyre Area on West Beach
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I would like to be recognized as an expert witness.
CHAIRMAN CHRISTENSON: Cammy, do you have
4 any.....
5 ji
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proceed.
COMMISSIONER OECHSLI: No objection.
CHAIRMAN CHRISTENSON: No objections. Please
32
8j MR. MORGAN: Okay. During my testimony today,
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9' I will provide information regarding West Beach operations and
101111i the engineering aspects of the proposed West Beach Secondary
11 Recovery Project.
12 (Off record comments)
13i West Beach Pool startup occurred in April 1993. The
141j field has been delineated by 11 penetrations consisting of
151; seven wells and four sidetracks. Three wells currently are
16; active: West Beach 4, West Beach 5B, and West Beach 6.
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17;' Exhibit B-3 is a plat showing the location of West Beach area
18! wells, including the three active wells, which are West
1911 Beach 4, 5B, and 6. Our recent efforts have focused on
20'!:t delineation and further development of the West Beach
21": reservoir, development of a secondary recovery plan, and
22!' construction of additional surface infrastructure to handle
2311 anticipated additional production from the West Beach
24 I! reservoir.
25 Secondary recovery plans at West Beach include water
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injection utilizing locally sourced water from Tertiary sands
produced from a new well on the West Beach Pad. Reservoir
simulation studies indicate incremental recovery from water
33
flooding to be between 10 to 15 percent of the estimated 15 to
25 million stock tank barrels of oil originally in place.
Augmenting water injection with gas injection to capture attic
oil along the southern fault trap is also being evaluated.
Thus, our application requests authorization for both water and
gas injection to enhance recovery from the West Beach
reservoir.
The West Beach geologic model was updated in early 1998
to incorporate data from the West Beach 5 and West Beach 6
wells. Utilizing this new geologic description and available
data from area production and exploration wells, a detailed
reservoir simulation model was constructed. The objectives of
the model study were to screen potential development or
delineation well locations and to evaluate secondary recovery
options. Results from the study indicate a peripheral
waterflood injecting into West Beach 6, which is the well down
to the -- getting backwards here. Right there. And producing
from the updip, West Beach 4 and West Beach 5B as a preferred
development scenario, with estimated incremental recovery of 10
to 15 percent of the original oil in place. The modeling study
indicated that increased well density primarily tended to
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accelerate the base reserve profile, with little incremental
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recovery. However, waterflood performance data will be key to
assessing additional development potential at West Beach.
Currently the minimum well spacing is 80 acres which should
be -- which should accommodate potential future drilling at
West Beach.
Recent drilling production and surveillance data from
West Beach 4, 5B, and 6 have validated the modeling study and
volumetrics. Post-fracture peak production from both West
Beach 5 and West Beach 6 was initiated at 1,700 stock tank
barrels of oil per day and 2,500 stock tank barrels of oil per
day, respectively. Subsequently, production in West Beach 5B
has fallen to 830 stock tank barrels of oil per day, primarily
due to reduced reservoir pressures in the area due to the
increased offtake. The lower well rates and solution GOR of
West Beach 5B make it difficult to keep this well online due to
paraffin build-up associated with cold flowing temperatures.
Production from West Beach 6 is currently at 800 stock tank
barrels of oil per day with associated gas of 11.2 million
standard cubic feet per day. Reservoir pressure monitoring
indicates good connectivity between the wells as evidenced by
the pressure drop of 500 to 750 psi following sustained
production from all three wells. These pressure drops are
consistent with the reservoir model and confirm lateral
�I connectivity between the wells. Lack of connectivity is a key
risk to secondary recovery at West Beach.
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1 The West Beach waterflood involves conversion of West
2 Beach 6 to injection service in the first quarter of 2000. The
3 conversion will be conducted in accordance with Alaska
4 Administrative Code. Can everybody see that? The West Beach 7
5 source water well, permit number 199-106, will supply injection
6 water with an electrical submersible pump producing water from
7 the Tertiary sands at a maximum rate of 10,000 barrels of water'
8 per day and 2,100 psi surface pressure. This source water well
9 is currently being drilled. Exhibit E-1 shows the planned
10 potential completion intervals on the West Beach 1 shallow
11 section log, this section here. A local water sample from the
12 target water source interval has not been obtained. However,
13 it is anticipated the water will be of similar composition to
14 that produced from the GC -3 water wells as shown in Exhibit M-1
15 from the April 5, 1993, Application for Modification to Area
16 Injection Order Number 4. Electric log salinity calculations
17 from West Beach State 1 indicates salinities of 20 to 40,000
18 ppm, which are consistent with the GC -3 water sample analyses
19I and previous log calculations.
20 Laboratory testing, core analyses, and geochemical
21 modeling indicate no significant problems with clay swelling or
2211 in-situ fluid compatibility. Analysis of a sample of West
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2411 amounts of clay, 11 percent, may be present, primarily in the
25'1 form of Kaolinite. The presence of this clay may cause pore
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1 plugging in conventional unstimulated producing wells at
2 waterflood breakthrough. However, both West Beach producing
3i wells are hydraulically fracture treated which will minimize
4 fluid velocities and subsequent fines movement in the rock near
it
5� the producing wells and thus minimize the potential for
6 producing well formation damage. Calculations for West Beach 4
7 show the velocities are 280 times less for the fractured
8 completion compared to an unstimulated completion. No evidence
9 of fines migration was observed during the initial post-frac
10 clean up tests in any of the wells at West Beach.
11 The Tertiary water is expected to contain excess barium
12 at concentrations from 50 to in excess of 300 parts per
13 million. If uninhibited, barium sulfate scale could result
14 when West Beach produced water is mixed with Point McIntyre
15 produced water containing excess sulfate associated with
16 seawater breakthrough. However, the West Beach produced water
17I stream will be inhibited upstream of the Point McIntyre/West
181 Beach commingling point to prevent barium sulfate
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19precipitation. Because West Beach has not produced any
201formation water, reservoir compatibility modeling and
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21laboratory testing assumed a water composition similar to that
22 1 of Point McIntyre.
231 Initially, the waterflood will be managed to replace
2411 reservoir voidage. As the flood progresses, injection rates
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25'I' will be adjusted in response to producing well surveillance and
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1 performance.
2 New facilities installed and in service on the West
3 Beach Pad include a central manifold designed to collect
4 production from four initial wells and five additional wells.
5 The pad will also have a new chemical injection skid and a new
61 electrical distribution skid. A new 12 inch pipeline has been
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7 installed from the West Beach pad to drill site L1 to handle
8 the increased production rates. Additionally, a four inch high
9 pressure line has been installed that will be used to supply
10 lift gas to the pad. The line has been designed to accommodate
11 high pressure gas or miscible injectant if additional pressure
12 maintenance or tertiary recovery can be justified. The
13 existing six inch production line will be converted to a
14 dedicated test line.
15 To facilitate initiating production from the West
16 Beach 5B and 6 wells, design and material procurement for the
17 facility expansion occurred prior to drilling the wells.
18 Consequently, sizing considered the low incremental cost for
19 additional slots and various future development scenarios,
20i including potential additional drilling for West Beach or other
21 GPMA fields. Waterflood performance data will be key to
22ii assessing additional development potential at West Beach.
23 That concludes my testimony.
24I CHAIRMAN CHRISTENSON: Mike, I think I missed
2511 it in the first part. How many wells did you say you were
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going -- intended to drill, additional wells?
MR. MORGAN: Right now, we're -- we have no
plans to drill additional wells until we get some response from
the waterflood. And at that point, we will re-evaluate our
plans for the field.
CHAIRMAN CHRISTENSON: Okay. Gotcha. Thank
you. No further questions.
MR. MORGAN: Thank you.
MR. GROTH: That concludes our testimony for
the West Beach portion of the application.
CHAIRMAN CHRISTENSON: Okay, sir. Thank you.
Any further comments from the public with regard to the West
Beach? Do you want to take a break?
COMMISSIONER OECHSLI: Sure.
CHAIRMAN CHRISTENSON: We're going to go off
record here for about 10 minutes to do some deliberation, make
sure we got all the questions. So if you would excuse us.
(Off record 11:00 a.m.)
(On record 11:12 a.m.)
CHAIRMAN CHRISTENSON: We back on record?
We've got a couple of questions -- further questions.
General questions we would like you to answer -- I'll
just tell you what the questions are, then you guys can figure
out who you want to answer them.
Question one. Are you planning to maintain voidage?
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Question two. What are the initial and current reservoir
pressures? And we would like you to elaborate a bit more on
the paraffin build-up and any mitigation plans you might have,
and your concerns there.
MR. MORGAN: I think that's me.
CHAIRMAN CHRISTENSON: Okay. Mike.
MR. MORGAN: Regarding question one --
actually, if you could repeat it for me so I make sure I get
them in the right order there.
CHAIRMAN CHRISTENSON: Question one was are you
planning to maintain voidage? Because you -- or make up
voidage because you had talked about it staying the same or
doing something like that and so we wondered if you were going
to -- did that meant that you were making it up or are you just
going to maintain what you're doing or where are you in the
voidage picture?
MR. MORGAN: I guess that's our initial
strategy is to replace voidage but I think right up front,
given that we're at, depending on which well you measure the
pressure in, anywhere from 3,000 -- just above 3,000 pounds to
3,300 pounds we will exceed voidage from the wells, especially
given West Beach 5 is not on line.
CHAIRMAN CHRISTENSON: So you will actually
make up and exceed that.....
MR. MORGAN: Yeah.
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1' CHAIRMAN CHRISTENSON: .....ultimately?
2''MR. MORGAN: And I guess that leads into
3: question two which speaks to the initial pressures and current
4' pressures. Initial pressures were measured in West Beach 4,
5, and this is roughly a number. I don't have the number in front
6';' of me but we've provided it in various formats, around 4,250
71) psi in West Beach 4. Stand alone production from that well
8i through this year drew the reservoir pressure down to about
11
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121
3,500 pounds. And then we brought on West Beach 5B and West
Beach 6 in July and August of 1999, and by November, we had
seen the pressure fall in West Beach 5B which is in the updip
area to just above 3,000 psi. And then also at West Beach 6,
it was down around 3,300 pounds.
14 CHAIRMAN CHRISTENSON: Okay.
15.! MR. MORGAN: And that data was submitted for
16 the code. But what we will do is we will go ahead and start up
17'I' the pump and inject at voidage and see if we see an initial
18' response because we do have gas in the system. We don't want
19, to overdisplace the oil.
20 CHAIRMAN CHRISTENSON: Okay. Then the last
21 question was you made some mention of the paraffin build-up in
22 one of the wells, and we're curious about what the effect you
23 think that's -- the new injection is going to have on that. Is
I
24 that a problem?
25 MR. MORGAN: The paraffin we see, we have seen
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it historically in West Beach 4 but it's become severe in West
Beach 5B. I don't have a schematic but that well is basically
a 16,000 foot measured depth well with tubing down to about
13,800. It's three and a half inch tubing. We do have lift
gas out to the well. Initially, at the 1,700 barrel a day
rates, it was fine. And with even a small water cut associated!
with the fracture treatment, we were able -- we didn't have too
many paraffin problems but as the reservoir pressure declined
and the rates in the well dropped pretty low down to around 800
barrels a day, we get severe paraffin build-up throughout that
tubing to the point where it plugs off and we have to go out
with coil tubing and clean it up. And so that's just a cost
that we incur. What we expect, if -- when we get waterflood
response from West Beach 6, is that the pressure will start to
come back up and that we will be able to sustain production
from that well. That's the current plan.
CHAIRMAN CHRISTENSON: Okay.
MR. MORGAN: It's similar to other wells at
Point McIntyre and Nuyakuk that you get to those rates in these
high departure wells. Temperatures drop pretty low.
CHAIRMAN CHRISTENSON: Okay. Cammy, do you
have any further questions?
COMMISSIONER OECHSLI: I don't. Thanks.
CHAIRMAN CHRISTENSON: I think that cleans us
j up on the question area.
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MR. MORGAN: One other point I would like to
make regarding the operation of the flood is our intent is to
operate the flood to increase pressures up towards 3,800 psi.
And we think that's an optimal point for the field. So prior
to that, we'll probably exceed voidage replacement. So it will
be above one on the VRR ratio.
CHAIRMAN CHRISTENSON: So your target is 3,800
then?
MR. MORGAN: Yeah.
CHAIRMAN CHRISTENSON: Great. Thank you.
MR. MORGAN: You're welcome.
MR. GROTH: If I may, one other point of
clarification.
CHAIRMAN CHRISTENSON: Sure.
MR. GROTH: In our prepared testimony, we had
mentioned a maximum injection rate of 10,000 barrels a day.
That is, in fact, the name plate capacity on the pump equipment
iI
that we are planning to install. In the event that we see
better than expected pump performance, we would ask that we
have a maximum injection rate 15,000 barrels a day that the
Commission consider that so that we're not back in here shortly
soon after start up requesting another amendment.
CHAIRMAN CHRISTENSON: Okay. So you want to
change or expand I guess the injection rate from 10 to 15?
j MR. GROTH: To 15 so that we've got some head
METRO COURT REPORTING, INC.
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room for daily operations above name plate capacity on the
equipment.
CHAIRMAN CHRISTENSON: We'll look at that. I
guess one point of clarification we have to do on this
confidential thing, too. We are understanding the 2003 date
and the information contained in those items we talked about
there, to be only those items, and we're not going to
retrograde back into other stuff that's already happened and
records and stuff that we already have. And is that your
understanding?
43
MR. GROTH: We concur with that understanding.
CHAIRMAN CHRISTENSON: Okay. Good. Is there
any other testimony or comments to be made today with regard to
West Beach? No. Cammy, do you have anything else?
COMMISSIONER OECHSLI: I don't.
CHAIRMAN CHRISTENSON: I think we've completed
it. And I would like to thank you for coming in and making a
presentation. All good presentations. We appreciate the
information. And that concludes our hearing for today. We'll
adjourn. Thank you.
i
(Off record 11:18 a.m.)
END OF PROCEEDINGS
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C E R T I F I C A T E
UNITED STATES OF AMERICA)
) ss.
STATE OF ALASKA )
I, Laura Ferro, Notary Public in and for the State of
Alaska, and Reporter for Metro Court Reporting, do hereby
certify:
That the foregoing Alaska Oil & Gas Conservation
Commission Public Hearing, was taken before me on the 13th day
of January 2000, commencing at the hour of 9:03 o'clock a.m.,
at the offices of Alaska Oil & Gas Conservation Commission,
3001 Porcupine Street, Anchorage, Alaska;
That the hearing was transcribed by me to the best of
my knowledge and ability.
IN WITNESS WHEREOF, I have hereto set my hand and
affixed my seal this 18th day of January 2000.
No ary Public in and for Alaska
My commission expires: 05/03/01
METRO COURT REPORTING, INC.
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Pt. McIntyre Oil Pool
Enhanced Oil Recovery Project
West Beach Oil Pool
Secondary Recovery Project
Application for Injection and Amendment to
Area Injection Order No. 413
Pt. McIntyre Testimony
Z
January 2000
January 13, 2000
Table of Contents
Section A — Testimony of John L. Hand......................................................................................1
Section B — Testimony of Murray P. Athans................................................................................4
Pt. McIntyre EOR Project Application - Testimony
Section A — Testimony of John L. Hand
Mr. Chairman, members of the commission, ladies and gentlemen, my name is John L. Hand. I
am the Subsurface Development Team Leader for the Pt. McIntyre Field. The Subsurface
Development Team is a multi -company, multi -disciplinary team established by the owner
companies. This team is responsible for the ongoing reservoir management activities of the Pt.
McIntyre Field. These activities include, but are not limited to, development drilling, reservoir
surveillance, production/injection scheduling, and hydrocarbon miscible EOR evaluation and
implementation.
I received a Bachelors of Engineering Degree in Chemical Engineering with Honors from the
University of New South Wales, Sydney Australia, in 1987 and a Degree of Doctor of Philosophy
in Petroleum Engineering also from the University of New South Wales, Sydney Australia, in
1991. 1 have been employed by ARCO since 1990 and have worked on a variety of reservoir
engineering projects both at ARCO Exploration and Production Technology and ARCO Alaska,
Inc., as well as a number of field development planning assignments at ARCO Alaska, Inc. I have
worked in the Greater Pt. McIntyre Area in my current position since September, 1997.
would like to be recognized as an expert witness.
During my testimony today I will provide information regarding current Pt. McIntyre field
operations as well as the reservoir engineering aspects of the proposed Pt. McIntyre enhanced oil
recovery project.
Pt. McIntyre Pool startup occurred in October 1993. Current operations involve a combination of
processed gas reinjection and 80 -acre inverted nine -spot pattern waterflooding for pressure
maintenance. Gas reinjection into the gas cap began concurrent with field startup, with water
injection beginning in July of 1994. As of January 1, 1999, fifteen water injectors and one gas
injector provide pressure support to the reservoir, maintaining average reservoir pressure at the
original pressure of approximately 4370 psi. Source water, from the Seawater Treatment Plant, is
currently used for the Pt. McIntyre waterflood.
Pt. McIntyre production is processed at the Lisburne Production Center (LPC). Field oil
production reached a facility -constrained plateau of 165,000 BOPD during the second quarter of
1996 and this nominal rate was maintained until the third quarter of 1997. Oil production has
since declined due to increasing water cuts at Pt. McIntyre and water handling constraints at the
LPC.
To enhance recovery of oil at Pt. McIntyre, the Working Interest Owners (ARCO, BPA and Exxon)
have approved a hydrocarbon miscible EOR project. Planned startup for MI injection is the first
half of 2000.
Exhibit B-1 is a plat showing the location of all existing injection wells, production wells,
abandoned wells, dry holes, and any other wells within the Pt. McIntyre Pool as of June 1, 1999.
The current Pt. McIntyre water and potential miscible solvent injector locations are identified in
the plat shown in Exhibit B-1 and are tabulated in Exhibit B-2.
Seventy-four wells have been drilled in the Pt. McIntyre pool through January 1, 1999 (not
including P&A'ed wells). The two Pt. McIntyre drill sites, PM1 and PM2, have production, water
injection, and gas lift facilities in place. Drill site PM1 also has gas injection facilities in place.
Ultimate well count at Pt. McIntyre is envisioned to be as high as 86 wells (not including P&A'ed
wells), depending on the number of 80 -acre infill wells and the extent of peripheral development.
Present estimates are that DS PM1 will ultimately have 20-23 wells, including four water injectors
Pt. McIntyre EOR Project Application - Testimony
and one gas injector, and that DS-PM2 will ultimately have 53-62 wells, including 10-13 water
injectors. An additional water injector (P1-25) is located at the West Dock staging area.
All Pt. McIntyre water injection wells are completed with L-80 grade steel. All tubin Jewel is
completed with 9-Cr/1 Moly, which is compatible with both L-80 and 13 -Cr. PMclntyre water?
i , c rr ompletions are designed as sin le zone, sin le string with a single packer. Exhibits G- /'
1 through G-5 show typical wellbore —scTiematics for the five basic comp a ion designs.
The current waterflood pattern configuration for the Pt. McIntyre Pool is an inve�nine-sThis pattern selection provides maximum flexibility for potential future convers
pattern configurations as changes in reservoir description and/or performance dictate. Additional
drilling within the EOR project area may be undertaken to improve sweep in areas of the reservoir
unaffected by the hydrocarbon miscible EOR process and to result in the recovery of oil from
areas and reservoir volume not otherwise affected by the implemented tertiary recovery activities.
Future development plans will be based on field performance, including the performance of the j
patterns already receiving MI. There are no plans to reduce well density below 40 acres. �J
A surveillance program to monitor the Pt. McIntyre EOR flood performance is in place and is
based on experience of operating similar projects at the Prudhoe Bay and Kuparuk Fields. This
program will be used to monitor field performance for field management and additional
development opportunities.
The Pt. McIntyre EOR project involves the eventual conversion of the existing 15 waterflood
injectors and potentially any future water injectors to water -alternating -gas (WAG) service. Water
will be injected alternately with MI in the WAG injection wells to improve the MI sweep in the
reservoir. At start up of the EOR project, water injection is anticipated to be approximately 250
MBWPD. Not all of the patterns will be receiving MI simultaneously. Those patterns not initially
converted to WAG injection will remain on continuous water injection until MI is available.
Source water is currently used for the Pt. McIntyre waterflood. It is anticipated that the same
injection water will be used during the initial stages of the EOR project. Conversion from source
water injection to produced water injection is possible in later stages of the flood. Both of these
water sources have been approved for injection into the Pt. McIntyre reservoir under Area
Injection Order No. 4B.
Currently, injection of an MI slug of 35 percent of hydrocarbon pore volume (HCPV) is planned.
The maximum size of the MI slug for the project is limited by the rate of delivery of MI
manufactured at the LPC. Exhibit S-1 shows the relationship between miscible injectant slug size
and i�r rrP^��^tai nil rFcovery for t e Pt Mcln yre n ance ai Recovery"'Frofe
Zn:ee,,d at the LPC is expected to be delivered to Pt. McIntyre at a nominal 50 MMSCFD.
hows the predicted incremental oil production rates for the Pt. McIntyre Enhanced Oil
Sdroject for the next 23 years for the miscible gas injection rate of 50 MMSCFD. Exhibit
shows the projected field oil production rates for the Pt. McIntyre base (primary/secondary)
base plus EOR (50 MMSCFD) for this same period. Under the planned scope, the LPC MI
supply will be limited, requiring the staging of MI injection into existing patterns as MI becomes
available. Initially, two patterns will receive MI injection. As EOR patterns mature, the availability
of excess MI will allow additional pattern(s) to begin receiving MI. Nominally, two patterns will be
receiving MI at any one time during the life of the project. It will take around 15+ years for the last
pattern to receive its first MI slug. Peak incremental oil rate is expected to exceed 5 MBD as a
result o ifie project. r
Current Pt. McIntyre operations (processed gas re-injection and pattern waterflooding) are
expected to yield an estimated total oil recovery of approximately 42 to 45% OOIP for the Pt.
McIntyre Pool. The planned hydrocarbon miscible EOR project at Pt. McIntyre is estimated to
Pt. McIntyre EOR Project Application - Testimony 2
.,r
V7 T M.
•
iDR-recovery by an additional 32 MMSTB of oil, or approximately 6% of the OOIP within
the current 15 pattern waterflood area.
The existing waterflood patterns contain varied reservoir quality with incremental oil recovery
estimates ranging from 4 to 8% OOIP of the targeted oil column under a hydrocarbon miscible
EOR process. These estimates are based on analysis of core from 20 wells distributed around
the field, detailed field wide stratigraphic correlations, PVT and fluid displacement laboratory
studies, and fine scale fully compositional fluid flow reservoir simulations tied back to the
laboratory data. The fine scale results were subsequently scaled up to a field wide scale, with the
estimated incremental oil recovery for the waterflood area determined using the Pt. McIntyre Full
Field reservoir simulation model.
MI for the Pt. McIntyre EOR project will be manufactured at the LPC from a mixture of produced
fluids from the Pt. McIntyre, West Beach, North Prudhoe Bay, Niakuk, and Lisburne Pools.
Based on the current operating practice of injecting processed natural gas from the LPC into the
Pt. McIntyre reservoir and given that the injected MI comprises the same hydrocarbon
components in a more concentrated form, no compatibility problems are anticipated.
The miscibility pressure criteria planned for the EOR project is designed to maximize oil recovery
and miscible injectant utilization for an MI -limited project. The minimum enrichment level for the
Pt. McIntyre miscible injectant was determined from standard laboratory PVT and slim -tube
displacement experiments. The blended MI will have a minimum miscibility pressure of
approximately 4350 psi. The expected composition is given in Exhibit H-1.
Injection and production at the Pt. McIntyre field are managed to maintain the average reservoir
pressure at the original pressure of approximately 4370 psi. There are no plans to change this
reservoir management philosophy. Reservoir pressure monitoring is performed in accordance
with Rule 12 of Conservation Order 317A and reported annually to the Alaska Oil and Gas
Conservation Commission in the Pt. McIntyre Oil Pool Annual Reservoir Report.
The constant reservoir pressure with time along with negligible temperature variations across the
field mean that miscibility pressure requirements are not expected to change as a result of
reservoir conditions during the life of the EOR project. Similarly, the compact nature of the Pt.
McIntyre waterflood/EOR patterns exhibit negligible differences in reservoir conditions across the
field. The minimum miscibility pressure/minimum miscibility enrichment evaluations for the project
were performed at reservoir temperature (1850F). The thermal temperature bulb at Pt. McIntyre,
due to source water injection, should provide an MMP buffer, but the project design was
developed without including this factor. Taken together, these factors reduce the need for a large
MMP buffer compared to other North Slope EOR projects.
The projected potential maximum MI rate under the current scope is 70 MMSCFD. Expanding the
Pt. McIntyre Enhanced Oil Recovery Project by increasing the miscible gas injection rate beyond
the current scope would require an external source of enriching components for manufacturing
the additional miscible injectant. This is a technically viable option and was part of the initial .U,>
scoping studies for an EOR Project at Pt. McIntyre. However, when this initial evaluation
indicated less favorable economics for this option, subsequent studies focused on self -generating
MI project options. These studies resulted in the Owner decision to approve the funding of the
project described in the testimony today. Analyses to investigate the benefits of a miscible gas
injection rate of up to 150 MMSCFD are being evaluated and will be based on the field
performance under the current scope. Such a rate would require an external source of enriched
MI, as well as additional drill site facilities and incremental capital expenditures.
Pt. McIntyre EOR Project Application - Testimony 3
Mr. Chairman, members of the commission, ladies and gentlemen, my name is Murray P. Athans.
I am the ARCO project engineer for the Pt McIntyre EOR project. In this role, my job
responsibilities have included facility design oversight and review, and acting as the primary
coordinator between the engineering contractor and the Lisburne Production Center (LPC)
Operations team. It has been my job to insure that the new facilities are fit for their intended
purpose, are built to ARCO Alaska standards, and meet all operating and safety design
requirements.
I received a Bachelors of Science degree with Honors in Chemical Engineering from the
University of Texas at Austin in 1978, and a Masters of Science degree in Chemical Engineering
from the University of Texas at Austin in 1980. 1 began work for ARCO at the Exploration and
Production Research Center in Plano, Texas in 1980, then transferred to ARCO Alaska in 1984.
Since arriving in Alaska, I have worked in a broad variety of facility planning and process
engineering positions within the Prudhoe Bay and Kuparuk business units. I transferred into the
Greater Point McIntyre Area in August, 1997, at which time I began my current assignment as
Project Engineer for the Pt McIntyre EOR project.
would like to be recognized as an expert witness.
During my testimony today I will provide an overview of the facility modifications and additions
which are being. installed to implement the Pt McIntyre EOR project. I will also briefly discuss
some of the project facility considerations that impacted the MI rate projections previously
discussed by John Hand.
Vapors generated in the LPC NGL plant downstream from the feed flash drum, which are
currently being injected as residue gas, will provide the enriching components for the MI solvent
stream. Facility modifications are designed to ensure that the -volume of blendable NGLs
extracted at th C will not be impacted by the EOR project. Manufacture of MI at the LPC at a
greater rate than planned for the project would adversely impact NGL production.
The nominal annual average MI manufacture rate is expected to be 50 MMSCFD. During the
summer months we expect to see an MI manufacture rate lower than winter months due to
reduced NGL refrigeration capacity resulting from higher ambient temperatures. In the first 4-5 �t�y
years of the project, MI rates during the summer are expected to range between 42-45 MMSCFD,
while in winter ranging between 52-53 MMSCFD. After 4-5 years, MI rates should be consistently
in the 50 MMSCFD range, with peaks as high as 60-70 MMSCFD. Peak rates estimates are
based in part on predictions of the volumes of returned MI.
The primary factors limiting the amount of MI manufacture at LPC are the LPC piping and vessel 7
metallurgical limit of —50°F (per ASME codes) and the plant refrigeration capacity. The new
chiller installed as part of the project was sized to utilize the existing excess refrigeration capacity
(propane system) at LPC. Increasing refrigeration capacity would require significant incremental
capital.
Modifications at the LPC during 1999 and early 2000 in support of the Pt. McIntyre EOR project
include the installation of an MI compressor, a second chiller, new compressor coolers and c {
blending station, and an upgrade of the LPC NGL plant liquid piping. MI will be transported to the
Pt. McIntyre drill sites via a new distribution pipeline (shown in Exhibit A-1) using currently
installed vertical support members. The EOR project will also require installation of drill site
distribution piping.
Pt. McIntyre EOR Project Application - Testimony 4
.il
�r
H2S concentrations during the life of the project are expected to remain low. The equipment
being installed is designed to handle the expected H2S concentrations. We will continue to
observe existing H2S safety precautions.
The estimated maximum and average injection pressures anticipated for the Pt. McIntyre
enhanced recovery projects are listed in the following table. These pressures represent pump
discharge pressures.
Injection Type Estimated Maximum Injection Estimated Average Injection
Pressure (psig) Pressure (psig)
Pt. McIntyre Water Injection 2850 2250
Pt. McIntyre MI Injection 4500 4100
Pt. McIntyre Gas Injection 5000 4300
The estimated maximum injection rates for Pt. McIntyre enhanced recovery wells will not initiate o J4" a
or propagate fractures through the confining strata, and, therefore, will not allow injection or ,,15 �,,•S 7
formation fluid to enter any freshwater strata. All field data collected to date indicate that injection
in the current water injectors and the single gas injector at Pt. McIntyre has been confined to the
injection strata. It is our expectation that the injected MI will remain confined to the injection
strata.
Existing water injection operations in the Pt. McIntyre Pool Kuparuk River Formation have been
above formation parting pressure to improve recovery of oil. In no instance have such injection
pressures breached the integrity of the confining zone.
Pt. McIntyre EOR Project Application - Testimony
5
ALASKA OIL AND GAS CONSERVATION COMMISSION
NAME - AFFILIATION
(PLEASE PRINT)
PUBLIC HEARING
Januar 1$, 2000
9.00 AM
PtMcIntvre/WBeach
TELEPHONE Do you plan to testify?
Yes No
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-43
ALASKA OIL AND GAS
CONSERVATION COMMISSION
December 1. 1999
Mr. J. W. Groth
ARCO Alaska, Inc.
PO Box 100360
Anchorage, Alaska 99510-0360
Dear Mr. Groth:
TONY KNOWLES, GOVERNOR
3001PORCUPINE DRIVE
ANCHORAGE. ALASKA 99501-3192
PHONE: (907) 279-1433
FAX: X907) 276-7542
The Commission will hold a hearing on January- 12, 2000 concerning your November 8. 1999
application for authon'ty to initiate a waterflood in the West Beach Oil Pool and a miscible gas
project in the Point McIntyre Oil Pool. The purpose of this hearing is to insure the public record
is as complete and accurate as possible for this important matter.
The Commission staff has reviewed your application and requests that information be provided to
the Commission to address the following questions.
Point McIntyre
1) Existing well spacing in the Point McIntyre Oil Pool is 40 acres per well. will the increased
well density your project envisions require a closer spacing?
2) What is the relationship between miscible slug size and oil recovery_ (miscible injectant
volume Vs incremental oil recovery)''
3) The proposed minimum miscibility pressure for the injectant is 20 psi below the average
reservoir pressure: this difference is much less than in other North Slope miscible gas
projects. What actions will Arco take to insure miscibility is maintained field wide? What
are the impacts of manufacturing injectant with a minimum miscibility pressure 100 psi
below average reservoir pressure? Is the proposed solvent likely to increase ultimate
recovery over a richer solvent with a lower miscibility pressure? If so why?
4) What are the projected production rates for the next 23 years for miscible gas injection rates
of 50 mmcf/d and 150 mmcf/d'? (Show primary_ recovery. «-aterflood recovery and miscible
gas incremental oil volumes separately).
5) Can sufficient enriching components to manufacture 150 mmcf/d of miscible injectant be
obtained at the Lisburne Production Facility without impacting ngl production'?
6) What are the sensitivities for manufacturing 150 mmcf/d of miscible injectant?
7) Is miscible injectant from an external source a viable option'? If not why'?
8) What are the projections for H2S concentrations and associated problems. if any?
WEST BEACH
1) The phi*h and structure map (annotated Nvith fluid contacts) used in generating the current
volumetrics should be included in the exhibits.
J.W. Groth
2
December 1, 1999
2) Are the net sand trends corroborated with seismic data, or are they based on a geologic model
and well control?
3) W est Beach facilities envision it wells. do these include delineation wells?
4) Is the 10-15% incremental waterflood recovery estimate based on existing wells? Will
additional wells increase incremental recovers? To what extent?
5) Current well spacing is 160 acres. is a closer spacing warranted?
6) Significant amounts of clay are present in the West Beach #4 core, which raises concerns
about pore plugging and fines migration. Please discuss potential problems and mitigation
techniques. Please describe your plans to obtain and analyze additional rock samples during
drilling of future wells.
We look forward to receiving your reply to this information request. In order to allow the
Commission staff adequate time to review vour submittal prior to the hearing, your reply is
requested as soon as possible. Please contact Jack Hartz or Bob Crandall of this office if you
wish to discuss anv of the items listed above.
Sincerely,
Robert N. Christenson, P.E.
Chair
42
Notice of Public Hearing
STATE OF ALASKA
Alaska Oil and Gas Conservation Commission
Re: Pt McIntyre and West Beach Oil Pools in the Prudhoe Bay Unit
ARCO Alaska, Inc. by letter dated November 8, 1999, has requested authority to
initiate a Miscible Gas Injection Tertiary Oil Recovery Project at Pt McIntyre and a
Water Injection Enhanced Oil Recovery Project at West Beach.
A person who may be harmed if the requested order is issued may file a written
protest prior to 4:00 PM, December 6, 1999 with the Alaska Oil and Gas Conservation
Commission, 3001 Porcupine Drive, Anchorage, Alaska 99501, and request a hearing on
this matter. If the protest is timely filed a hearing on the matter will be held at the above
address at 9:00 AM on January 12, 2000, in conformance with 20 AAC 25.540. If no
protest is filed, the Commission will consider the issuance of the order without a hearing.
If you are a person with a disability who may need a special modification in order
to comment or to attend the public hearing, please contact Diana Fleck at 793-1221
before January 5, 2000.
Robert N. Christenson, P.E.
Chairman
Published November 20 1999
ADN AO# 02014016
of Publicat 0
0OAffidavit �►
Ad # Run Dates ED Po #
217069 11/20/99 DN 02014016
Price per Account
day
$67.50 STOF0330
STOF0330
$67.50
STATE OF ALASKA
THIRD JUDICIAL DISTRICT
Eva Alexie, being first duly sworn on oath deposes and says that
she is an advertising representative of the Anchorage Daily
News, a daily newspaper.
That said newspaper has been approved by the Third Judicial
Court, Anchorage, Alaska, and it now and has been published in
the English language continually as a daily newspaper in
Anchorage, Alaska, and it is now and during all said time was
printed in an office maintained at the aforesaid place of
publication of said newspaper. That the annexed is a copy of an
advertisement as it was published in regular issues (and not in
supplemental form) of said newspaper on the above dates and
that such newspaper was regularly distributed to its
subscribers during all of said period. That the full amount of the
fee charged for the foregoing publication is not in excess of the
rate charged private individuals.
Legal ClerkC�'�_
Subscribed and sworn to me before this date:
6 UCMiC/6,'ZP,1z.:;L-z�
Notary Public in and for the State of Alaska.
Third Division. Anchorage, Alaska
MY COMMISSION EXPIRES: Fill g ?e
---- —� —T -----------
'���ti�(uLrO�`'
c
PUBV
of- ,
A person who may' be
harmed ; if the requested
order is issued may file a
written protest prior to 4:00
PM, December 6, 1999 with
the Alaska:. Oil and Gas
Conservation Gommission,
3001 Porcupine Drive,
Anchorage,Alaska 99501,
and requesta hearing on
this matter. If the protest is
timely filed a hearing on
the matter will be heldat
the above address at 9:00
AM on January 12, 2000, in
conformance with 20 AAC
25.540. If no protest isfiled,
the Commission will con-
sider the issuance of the
order without a hearing.
If you are a person with a
disability who may need a
special modification in
order to comment or to
attend the public hearing,
Please contact Diana Fleck
at 793-1221 before January
5, 2000.
/s/Robert N. Christenson
P.E., Chairman
Pub.: 11/20/99
41
.r ARCO Alaska, Inc.
Post Office B 036
Anchorage, Alaska 99510-0360
Telephone 907 2761215
Greater Pt. McIntyre Area
November 8, 1999
Robert N. Christensen, Chairman
Alaska Oil and Gas Conservation Commission
3001 Porcupine Drive
Anchorage, AK 99501-3192
Joe
ORIGINAL
RE: Pt. McIntyre Field Enhanced Oil Recovery Project and West Beach
Secondary Recovery Project Application for Injection and Amendment to
Area Injection Order No. 4B.
Dear Mr. Christensen:
Enclosed is the Pt. McIntyre Field Enhanced Oil Recovery Project and West Beach
Secondary Recovery Project Application for Injection and Amendment to Area Injection
Order No. 4B. The application was prepared in accordance with 20 AAC 25.402
(Enhanced Recovery Operations) and 20 AAC 25.460 (Area Injection Orders). ARCO
Alaska, Inc. as Operator of the Pt. McIntyre and West Beach Pools, seeks Alaska Oil
and Gas Conservation Commission endorsement and authorization for the proposed
projects and amendments to Area Injection Order 4B.
In the event that a public hearing is held under 20 AAC 25.540, we would like to meet
with the Commission prior to the hearing, if held, for clarification of the hearing
procedures and deadlines. ARCO Alaska, Inc. will be prepared to provide testimony in
support of the application, and we anticipate that it will take about one day to present
our testimony.
Please contact J. W. Groth (265-6846), M. R. Morgan (263-4332) or J. L. Hand (265-
6036) if you have questions or require additional information.
Sincerely,
J. W. Groth
Attachments
cc: D. W. Bose (AAI)
ARCO Alaska, Inc. is a Subsidiary of AtlanticRichfieldCompany
M. P. Evans (Exxon)
J. Hurliman (BPA)
Pt. McIntyre Oil Pool
Enhanced Oil Recovery Project
West Beach Oil Pool
Secondary Recovery Project
Application for Injection and Amendment to
Area Injection Order No. 4B
20 AAC 25.402
20 AAC 25.460
November 8, 1999
November 8, 1999
0
Table of Contents
Section A - Application for Injection and Amendment to Area Injection Order No. 4B ....................1
Section B - Plat of Project Area........................................................................................................3
Section C - Operators/Surface Owners............................................................................................4
SectionD - Affidavit..........................................................................................................................6
Section E - Description of Operation................................................................................................7
Section F — Geologic Information.....................................................................................................9
Section G - Injection Well Casing Information................................................................................10
SectionH - Injection Fluids.............................................................................................................11
Section I - Injection Pressures........................................................................................................13
Section J - Fracture Information.....................................................................................................14
Section K - Hydrocarbon Recovery ................................................................................................15
Section L - Proposed Findings.......................................................................................................16
Section M — Recommended Conclusions......................................................................................19
Section N — Requested Decisions..................................................................................................20
Exhibits...........................................................................................................................................21
Pt. McIntyre EOR Project Application
0
List of Exhibits
Exhibit A-1: Greater Pt. McIntyre Area Drillsites and Pipeline Routing Map
Exhibit B-1: Plat of Wells Within Pt. McIntyre Participating Area
Exhibit B-2: Pt. McIntyre Injection Wells
Exhibit B-3: Plat of West Beach Pool/Participating Area
Exhibit C-1: Native Allotment Parcel Map
Exhibit D-1: Affidavit
Exhibit E-1: West Beach Shallow Section Type Log WB -1 — Source Water Targets
Exhibit F-1: West Beach West to East Structural/Stratigraphic Cross -Section
Exhibit F-2: West Beach Reservoir Net -to -Gross Map, Post West Beach 6
Exhibit G-1: Pt. McIntyre Well Schematic — Conventional Gas Injection Well Design
Exhibit G-2: Pt. McIntyre Well Schematic — Conventional Water Injection Well Design
Exhibit G-3: Pt. McIntyre Well Schematic — Slimhole Water Injection Well Design
Exhibit G-4: Pt. McIntyre Well Schematic — Ultra Slimhole Water Injection Well Design
Exhibit G-5: Pt. McIntyre Well Schematic — Mono -bore Water Injection Well Design
Exhibit G-6: West Beach Well Schematic — WB -04
Exhibit G-7: West Beach Well Schematic — WB -06
Exhibit H-1: Pt. McIntyre Miscible Injectant Compositional Analysis
Exhibit H-2: LPC Reinjection Gas Compositional Analysis
Pt. McIntyre EOR Project Application
Section A - Application for Injection and Amendment to Area Injection
Order No. 413
20 AAC 25.460
20 AAC 25.402
ARCO Alaska, Inc. ("ARCO"), in its capacity as a Working Interest Owner (WIO) in, and Operator
of, the Pt. McIntyre and West Beach Oil Pools, hereby applies for Alaska Oil and Gas
Conservation Commission (Commission) authorization to inject an enriched hydrocarbon miscible
gas in the Pt. McIntyre Pool and water and gas in the West Beach Pool for the Pt. McIntyre Pool
Enhanced Oil Recovery (EOR) Project and the West Beach Pool Secondary Recovery Project,
respectively, for the purpose of enhanced recovery of oil, and amendment to Area Injection Order
No. 46, issued April 13, 1998. This application has been prepared in accordance with 20 AAC
25.402 (Enhanced Recovery Operations) and 20 AAC 25.460 (Area Injection Orders). It follows
the same format and exhibit numbering as set forth in the Application for Modification to Area
Injection Order No. 4, dated April 5, 1993.
Pt. McIntyre
Pt. McIntyre Pool startup occurred in October 1993. Current operations involve a combination of
processed gas reinjection and 80 -acre inverted nine -spot pattern waterflooding for pressure
maintenance. Gas reinjection into the gas cap began concurrent with field startup, while
waterflood injection began in July of 1994. As of January 1, 1999, fifteen water injectors and one
gas injector provide pressure support to the reservoir, maintaining average reservoir pressure at
the original pressure of approximately 4370 psi. Source water, from the Seawater Treatment
Plant, is currently used for the Pt. McIntyre waterflood.
Pt. McIntyre production is processed at the Lisburne Production Center (LPC). Field oil
production reached a facility -constrained plateau of 165,000 BOPD during the second quarter of
1996 and this nominal rate was maintained until the third quarter of 1997. Oil production has
since declined due to increasing water cuts at Pt. McIntyre and water handling constraints at the
LPC.
To enhance recovery of oil at Pt. McIntyre, the Working Interest Owners (ARCO, BPA and Exxon)
have approved a hydrocarbon miscible EOR project. Vapors generated in the LPC NGL plant
downstream from the feed flash drum, which are currently being injected as residue gas, will
provide the enriching components for the miscible injectant (MI) solvent stream. Facility
modifications are designed to ensure that the volume of blendable NGLs extracted at the LPC will
not be impacted by the EOR project. Planned startup for MI injection is the first quarter of 2000.
Additional Pt. McIntyre EOR project details are provided in the discussion of the specific
requirements of 20 AAC 25.402(c). Proposed findings, recommended conclusions, and
requested decisions of the Commission are included at the end of this application.
West Beach
West Beach Pool startup occurred in April 1993. The field has been delineated by eleven
penetrations consisting of seven wells and four sidetracks. Three wells currently are active, WB -
04, WB -05B and WB -06. Recent work efforts have focused on delineation and further
development of the West Beach reservoir, development of a secondary recovery plan, and
construction of additional surface infrastructure to handle additional production from the West
Beach reservoir. Significant progress has been made in developing the West Beach reservoir,
including plans for secondary recovery.
Pt. McIntyre EOR Project Application
Secondary recovery plans at West Beach include water injection utilizing locally sourced water
from Tertiary sands produced via a new well on the West Beach Pad. Reservoir simulation
studies indicate incremental recovery from waterflooding to be between 10 to 15% of the
estimated 15-25 MMSTB original oil in place. Additionally, augmenting water injection with gas re-
injection to capture attic oil along the southern fault trap is being evaluated. This application
requests authorization for both water and gas injection to enhance recovery from the West Beach
Oil Pool.
Additional West Beach Secondary Recovery Project details are provided in the discussion of the
specific requirements of 20 AAC 25.402(c) or by reference to the Application for Modification to
Area Injection Order No. 4, dated April 5, 1993. Proposed findings, recommended conclusions,
and requested decisions of the Commission are included at the end of this application
Pt. McIntyre EOR Project Application
0
Section B - Plat of Project Area
20 AAC 25.402(c)(1)
Exhibit B-1 and B-3 are plats showing the location of all existing injection wells, production wells,
abandoned wells, dry holes, and any other wells within the Pt. McIntyre Pool or West Beach Pool,
respectively, as of June 1, 1999. The current Pt. McIntyre water and potential miscible solvent
injector locations are identified in the plat shown in Exhibit B-1 and are tabulated in Exhibit B-2.
Specific approvals for any new injection wells or existing wells to be converted to injection service
will be obtained pursuant to 20 AAC 25.005, 25.280 and 25.507, or any applicable successor
regulation.
Pt. McIntyre EOR Project Application
Section C - Operators/Surface Owners
20 AAC 25.402(c)(2)
The Pt. McIntyre and West Beach PAs are operated by ARCO Alaska, Inc. The Surface Owners
within one-quarter mile and inclusive of the Pt. McIntyre and West Beach PAs are listed in the
following table. The Native Allotment Landowners are listed by allotment parcel. Exhibit C-1 is an
areal map of the parcels.
Surface Owners
State of Alaska
Department of Natural Resources
Attn: M. Kotowski
P.O. Box 107034
Anchorage, AK 99510
Selection within Section 28 (ADL 414852)
City of Barrow
City of Barrow
P. O. Box 629
Barrow, AK 99723
Parcel 16 (USS 9137)
Lawrence Ahmaogak
P.O. Box 411
Barrow, AK 99723
And
C/o Kathleen Dickinson, Land Director
Arctic Slope Native Association, Ltd.
714 Fourth Ave., Suite 201
Fairbanks, AK 99701-4470
Pt. McIntyre EOR Project Application
Parcel 17 (USS 6905)
Alice Glenn
899 Blair Ave.
Sunnydale, CA 94087
And
C/o Kathleen Dickinson, Land Director
Arctic Slope Native Association, Ltd.
714 Fourth Ave., Suite 201
Fairbanks, AK 99701-4470
George Ahmaogak
P.O. Box 338
Barrow, AK 99723
And
C/o Kathleen Dickinson, Land Director
Arctic Slope Native Association, Ltd.
714 Fourth Ave., Suite 201
Fairbanks, AK 99701-4470
Lawrence Ahmaogak
P.O. Box 411
Barrow, AK 99723
And
C/o Kathleen Dickinson, Land Director
Arctic Slope Native Association, Ltd.
714 Fourth Ave., Suite 201
Fairbanks, AK 99701-4470
•
Parcel 16 (USS 9267)
John P. Nicholls (minor)
C/o Ely Varner (guardian)
P.O. Box 473
Barrow, AK 99723
And
C/o Kathleen Dickinson, Land Director
Arctic Slope Native Association, Ltd.
714 Fourth Ave., Suite 201
Fairbanks, AK 99701-4470
USS 4044
United States Department of the Navy
U.S. Dept. of Navy
Commanding Officer (Code 051-M)
Engineering Field Activity NW
Naval Facilities Engineering Command
19917 7th Ave., NE
Poulsbo, WA 98370-7570
Pt. McIntyre EOR Project Application
•
Parcel 18 (USS 6906
Barbara Ahmaogak, Life Estate Holder
1628 Hilton Ave.
Fairbanks, AK 99701
And
C/o Kathleen Dickinson, Land Director
Arctic Slope Native Association, Ltd.
714 Fourth Ave., Suite 201
Fairbanks, AK 99701-4470
Lawrence Ahmaogak, George Ahmaogak and
Alice Glenn, remaindermen
(service as provided above)
Parcel NA F-14632
Wallace Oenga, Georgene Shugluk, Leroy
Oenga, Michael Delia and Jennie Oenga
(deceased, probate pending)
C/o Kathleen Dickinson, Land Director
Arctic Slope Native Association, Ltd.
714 Fourth Ave., Suite 201
Fairbanks, AK 99701-44
Section D - Affidavit
20 AAC 25.402(c)(3)
Exhibit D-1 is an affidavit showing that the Operators and Surface Owners within a one-quarter
mile radius of the area included in the Pt. McIntyre and West Beach PAs have been provided a
copy of this application for injection and amendment to Area Injection Order No. 4B.
Pt. McIntyre EOR Project Application
Section E - Description of Operation
20 AAC 25.402(c)(4)
Pt. McIntyre
Enhanced recovery injection wells are used for the introduction of additional fluids into the
reservoir to increase the ultimate recovery of oil. Currently, two types of injection wells are in
operation at Pt. McIntyre: produced gas reinjection and water injection. Gas reinjection began
concurrent with field startup, with water injection beginning in July of 1994. As of January 1, 1999,
fifteen water injectors and one gas injector provide pressure support to the reservoir, maintaining
average reservoir pressure at the original pressure of approximately 4370 psi. Source water, from
the Seawater Treatment Plant, is currently used for the Pt. McIntyre waterflood.
Seventy-four wells have been drilled in the Pt. McIntyre pool through January 1, 1999 (not
including P&A'ed wells). The two Pt. McIntyre drill sites, PM1 and PM2, have production, water
injection, and gas lift facilities in place. Drill site PM1 also has gas injection facilities in place.
Ultimate well count at Pt. McIntyre is envisioned to be as high as 86 wells (not including P&A'ed
wells), depending on the number of 80 -acre infill wells and the extent of peripheral development.
Present estimates are that DS-PM1 will ultimately have 20-23 wells, including four water injectors
and one gas injector, and that DS-PM2 will ultimately have 53-62 wells, including 10-13 water
injectors. An additional water injector (P1-25) is located at the West Dock staging area.
The current waterflood pattern configuration for the Pt. McIntyre Pool is an inverted nine -spot.
This pattern selection provides maximum flexibility for potential future conversions to other
pattern configurations as changes in reservoir description and/or performance dictate. Additional
drilling within the EOR project area may be undertaken to improve sweep in areas of the reservoir
unaffected by the hydrocarbon miscible EOR process and to result in the recovery of oil from
areas and reservoir volume not otherwise affected by the implemented tertiary recovery activities.
The Pt. McIntyre EOR project involves the eventual conversion of the existing 15 waterflood
injectors and potentially any future water injectors to water -alternating -gas (WAG) service.
Currently, injection of an MI slug of 35 percent of hydrocarbon pore volume (HCPV) is planned.
MI generated at the LPC is expected to be delivered to Pt. McIntyre at a nominal 50 MMSCFD.
At this rate, MI injection would occur for a period of approximately 23 years to inject the entire 35
percent HCPV slug in the existing patterns. Peak incremental oil rate is expected to exceed 5
MBD as a result of the project. Potential benefits from additional MI for the EOR project are being
evaluated. Increased MI volume would provide flexibility with respect to project phasing and WAG
ratios.
Vapors generated in the LPC NGL plant downstream from the feed flash drum, which are
currently being injected as residue gas, will provide the enriching components for the MI solvent
stream. Facility modifications are designed to ensure that the volume of blendable NGLs
extracted at the LPC will not be impacted by the EOR project. Planned startup for MI injection is
the first quarter of 2000.
Modifications at the LPC during 1999 in support of the Pt. McIntyre EOR project include the
installation of an MI compressor, a new parallel chiller, new compressor coolers and blending
station, and an upgrade of the LPC NGL plant liquid piping. MI will be transported to the Pt.
McIntyre drill sites via a new distribution pipeline (shown in Exhibit A-1) using currently installed
vertical support members. The EOR project will also require installation of drill site distribution
piping.
Pt. McIntyre EOR Project Application
•
West Beach
The West Beach geologic model was updated in early 1998 to incorporate data from the West
Beach 5 (WB5) and West Beach 5A (WB5A) penetrations (Exhibit B-3). Utilizing this new
geologic description and available data from area production and exploration wells, a detailed
reservoir simulation model was constructed. The objectives of the model study were to screen
development/delineation well locations and to evaluate secondary recovery options. Results
indicated peripheral waterflood as the preferred development scenario, with estimated
incremental waterflood recovery factors from 10-15% of the original oil in place.
Pending successful testing and sustained production from both WB -05B and WB -06, a peripheral
waterflood is planned for the reservoir The West Beach waterflood involves conversion of one
.well, either WB -06 or WB -04, to injection service in the first quarter of 2000. The decision of
which well to convert will be dictated by additional performance data from all wells in the field.
Planning , design engineering and funding have been completed for drilling a source water well
on the West Beach pad and converting WB -06 to water injection service. The source water well
would supply injection water via an electrical submersible pump sourcing water from the Tertiary
sands (Exhibit E-1). Initially, the waterflood would be managed to replace reservoir voidage. As
the flood progresses, injection rates would be adjusted in response to producing well surveillance
and performance. Augmenting water injection with gas re-injection to capture attic oil along the
southern fault trap is being evaluated. Thus, this application requests authorization for both water
and gas injection to enhance recovery from the West Beach Oil Pool. The source water well will
be permitted and constructed in accordance with 20 AAC 25.005.
New pad facilities installed and in service on the West Beach pad include a central manifold
designed to collect production from four initial wells and five future wells. The pad will also have a
new chemical injection skid and a new electrical distribution skid. A new 12" pipeline has been
installed from the West Beach pad to drill site L1 to handle increased production rates.
Additionally, a 4" high pressure (5230 psi) line has been installed that initially will be used to
supply lift gas to the pad. The line has been designed to accommodate high pressure gas or
miscible injectant should additional pressure maintenance or tertiary recovery be justified. The
existing 6" production line will be converted to a dedicated test line. The pipelines and manifold
skid have been installed and are in service on the pad.
Pt. McIntyre EOR Project Application
Section F — Geologic Information
20 AAC 25.402(c)(6)
Pt. McIntyre
Refer to Section G of the "Application for Modification to Area Injection Order No. 4", dated April
5, 1993.
West Beach
The West Beach Pool produces from the Lower Cretaceous (Late Hauterivian) Kuparuk River
Formation. The Kuparuk River formation in this area is a package of sand to conglomerate sized
debris flows that have infilled the West Beach graben, prograding from south to north and west to
east. Reservoir quality decreases away from the bounding fault in a distal direction toward the
basin (refer to Exhibits F-1 and F-2). Biostratigraphic data indicate the productive sands in the
West Beach reservoir are younger than the reservoir quality sands in the lower Kuparuk River
formation section of the Gull Island 3 well to the east.
The interval targeted for enhanced recovery at West Beach is defined by Conservation Order
311A Rule 2, which defines the pool as the accumulation which is common to and correlates with
the accumulation found in the West Beach No. 4 well between the depths of 14,458' MD and
14,781' MD (refer to Exhibit G-11 in the "Application for Modification to Area Injection Order No.
4, dated April 5, 1993").
Refer to Section G of the "Application for Modification to Area Injection Order No. 4", dated April
5, 1993, for additional information.
Pt. McIntyre EOR Project Application
Section G - Injection Well Casing Information
20 AAC 25.402(c)(8)
Pt. McIntyre
Currently, 15 water injectors and one gas injector are in service in the Pt. McIntyre Pool. A wide
range of departures have been drilled in Pt. McIntyre with a maximum injection well departure of
over 13,300 feet (P2-47).
Injection well tubing sizes in the Pt. McIntyre pool vary from 2-7/8" to 7" with the majority being 4-
1/2" and 5-1/2". In general, the production casing is sized to the tubing in the Pt. McIntyre wells.
Development wells utilize either a "conventional," "slimhole," "ultra slimhole," or "mono -bore"
design similar to designs used in the Kuparuk River Unit and other Prudhoe Bay Unit wells. The
"conventional" design wells requiring 5-1/2" tubing utilize 13-3/8" surface casing, 9-5/8"
production, or intermediate casing with a 7" liner for the high step out wells. The "slimhole"
design wells requiring 4-1/2" tubing utilize 10-3/4" surface casing, 7-5/8" production, or
intermediate casing with a 4-1/2" liner for high step out wells. The lower rate wells utilize the
"ultra slimhole" design, a 4-1/2" tubing string inside a 7" production string with 9-5/8" surface pipe.
One well (P2-34) is a "mono -bore" completion with 9-5/8" production casing and a 5-1/2" liner
over the production interval with 5-1/2" tubing.
All Pt. McIntyre water injection wells are completed with L-80 grade steel. All tubing jewelry is
completed with 9-Cr/1 Moly, which is compatible with both L-80 and 13 -Cr.
Pt. McIntyre water injection completions are designed as single zone, single string with a single
packer. Exhibits G-1 through G-5 show typical wellbore schematics for the five basic completion
designs.
West Beach
WB -06 or WB -04 will be converted to injection service for the West Beach waterflood. The casing
program for both WB -04 and WB -06 were permitted and completed in accordance with 20 AAC
25.030. Cement bond logs were recorded in both wellbores prior to running the completion. The
bond logs and fracture treatment data indicate isolation of the target injection zone. Well
conversion will be conducted in accordance with 20 AAC 25.412. Exhibits G-6 and G-7 detail the
completions for WB -04 and WB -06, respectively.
The actual casing program is included with the "Application to Drill" for each well and is
documented with the AOGCC in the completion record. API injection casing specifications are
included on each drilling permit application. All injection casing is cemented and tested in
accordance with 20 AAC 25.412 for both newly drilled and converted injection wells. All drilling
and production operations will follow approved operating practices regarding the presence of H2S
in accordance with 20 AAC 25.065.
Pt. McIntyre EOR Project Application 10
Section H - Injection Fluids
20 AAC 25.402(c)(9)
Pt. McIntyre
MI for the Pt. McIntyre EOR project will be manufactured at the LPC by blending enriching
components generated from the vapors in the LPC NGL plant downstream from the feed flash
drum with processed reinjected natural gas. Upon full start up of the EOR project, MI manufacture
is expected to reach 50 MMSCFD of blended MI with a minimum miscibility pressure of
approximately 4350 psi. The expected composition is given in Exhibit H-1.The benefits of
additional MI for the EOR project are being evaluated and up to 150 MMSCFD could be injected
into the Pt. McIntyre reservoir as part of the EOR project.
Water will be injected alternately with MI in the WAG injection wells to improve the MI sweep in
the reservoir. At start up of the EOR project, water injection is anticipated to be approximately
250 MBWPD. Not all of the patterns will be receiving MI simultaneously. Those patterns not
initially converted to WAG injection will remain on continuous water injection until MI is available.
Source water is currently used for the Pt. McIntyre waterflood. It is anticipated that the same
injection water will be used during the initial stages of the EOR project. Conversion from source
water injection to produced water injection is possible in later stages of the flood. Both of these
water sources have been approved for injection into the Pt. McIntyre reservoir under Area
Injection Order No. 4B.
Injection fluid information pertaining to the amendment of Area Injection Order No. 4B is given
below.
Type of Fluid — Miscible Injectant. This fluid is an enriched hydrocarbon gas manufactured for the
purpose of miscible hydrocarbon EOR.
Composition — See Exhibit H-1.
Source of Fluid — Natural gas from Pt. McIntyre, West Beach, North Prudhoe Bay, Niakuk, and
Lisburne Pools.
Estimated Maximum Amount to Be Infected Daily — Up to 150 million standard cubic feet per day.
Compatibility with Formation and Confining Zones — MI injected into the Pt. McIntyre pool will be
manufactured at the LPC from a mixture of produced fluids from the Pt. McIntyre, West Beach,
North Prudhoe Bay, Niakuk and Lisburne Pools. Based on the current operating practice of
injecting processed natural gas from the LPC into the Pt. McIntyre reservoir and given that the
injected MI comprises the same hydrocarbon components in a more concentrated form, no
compatibility problems are anticipated.
Pt. McIntyre EOR Project Application
West Beach
Type of Fluid/Source — Tertiary water. The West Beach secondary recovery project will
utilize water produced from the Tertiary Sagavanirktok formation (refer to Exhibit G-3 in the
"Application for Modification to Area Injection Order No. 4", dated April 5, 1993, and attached
Exhibit E-1).
Composition — A water sample from the target water source interval has not been obtained.
However, it is anticipated the water will be of similar composition to that produced from the
GC -3 water wells (refer to Exhibits M-1 and M-2 in the "Application for Modification to Area
Injection Order No. 4", dated April 5, 1993). Electric log salinity calculations from the West
Beach State #1 well indicate salinities of 20,000 to 40,000 ppm, which are consistent with the
GC -3 water sample analyses and previous log calculations.
Estimated Maximum Amount to be Infected Daily — Maximum water injection requirements at
West Beach are estimated at 10,000 BW PD.
Compatibility with Formation and Confining Zones — Laboratory testing, core analyses and
geochemical modeling indicate no significant problems with clay swelling or in-situ fluid
compatibility. Analysis of the West Beach 4 core indicates significant amounts of clay (11%),
primarily in the form of Kaolinite and Illite, which may cause pore plugging in the producing
wells at waterflood breakthrough. However, both wells are hydraulically fracture treated,
which should help minimize fluid velocities and subsequent fines movement in the rock near
the producing wells and the potential for producing well formation damage. The tertiary water
is expected to contain excess barium at concentrations from 50 ppm to in excess of 300 ppm,
which, if uninhibited, will precipitate barium sulfate scale when mixed with the Pt. McIntyre
water containing excess sulfate (SO4) associated with seawater breakthrough. However, the
West Beach produced water stream will be inhibited upstream of the PM/WB commingling
point to prevent BaSO4 precipitation. Because West Beach has not produced any formation
water, reservoir compatibility modeling and laboratory testing assumed a water composition
similar to that of the Pt. McIntyre pool. (refer to Exhibit J-3 in the "Application for Modification
to Area Injection Order No. 4",dated April 5, 1993)
Type of Fluid/Source — Natural Gas. The fluid consists of Lisburne, Pt. McIntyre, West
Beach, North Prudhoe, and Niakuk natural gas produced with the oil and separated from the
oil and water at LPC.
Composition — See exhibit H-2
Estimated Maximum Amount to be Iniected Daily — Maximum gas injection rates are
estimated at 25 MMSCFD.
Compatibility with Formation and Confining Zones — Although Lisburne processed gas
contains H2S, which is not native to the West Beach reservoir, minimal compatibility issues
are anticipated.
Pt. McIntyre EOR Project Application 12
Section 1 - Injection Pressures
20 AAC 25.402(c)(10)
The estimated maximum and average injection pressures anticipated for the Pt. McIntyre and
West Beach enhanced recovery projects are listed in the following table.
Injection Type
Pt. McIntyre Water Injection
Pt. McIntyre MI Injection
Pt. McIntyre Gas Injection
West Beach Water Injection
West Beach Gas Injection
Estimated Maximum Injection
Pressure (psig)
2850
4500
5000
2850
4500
Estimated Average Injection
Pressure (psig)
(These pressures represent pump discharge pressures.)
2250
4100
4300
2100
4100
Pt. McIntyre EOR Project Application 13
Section J - Fracture Information
20 AAC 25.402(c)(11)
The estimated maximum injection rates for Pt. McIntyre and West Beach enhanced recovery
wells will not initiate or propagate fractures through the confining strata, and, therefore, will not
allow injection or formation fluid to enter any freshwater strata. There are no indications of
injection out of zone for the current water injectors and the single gas injector at Pt. McIntyre.
Freshwater Strata
There are no freshwater strata in the area of issue (see Section N of the Application for
Modification to Area Injection Order No. 4, dated April 5, 1993). Therefore, even if a fracture were
propagated through all confining strata, injection or formation fluid would not come in contact with
freshwater strata.
Enhanced Recovery
Existing water injection operations in the Pt. McIntyre Pool Kuparuk River Formation have been
above formation parting pressure to improve recovery of oil. In no instance has such injection
pressures breached the integrity of the confining zone. The Kuparuk River Formation at both Pt.
McIntyre and West Beach is overlain by the Kalubik and HRZ shales. The HRZ is a thick shale
sequence which tends to behave as a plastic medium and can be expected to contain
significantly higher pressures than sandstones. Mechanical properties determined from log data
for the HRZ and Kalubik intervals indicate a fracture gradient from approximately 0.8 to 0.9 psi/ft.
Fracture data from the Pt. McIntyre and West Beach Kuparuk River Formation indicate a fracture
gradient of between 0.6 and 0.63 psi/ft under virgin reservoir conditions. Fracture data from Pt.
McIntyre No. 9 (P2-59) indicated a fracture gradient of 0.624 psi/ft, while data from West Beach
No. 4 indicated a fracture gradient of 0.602 psi/ft.
The Kuparuk River Formation is underlain by the Miluveach/Kingak shale sequence. A leakoff
test in the Kingak shale formation demonstrated leakoff at a gradient of 0.85 psi/ft.
In addition, data from the Prudhoe Bay Oil Pool indicate that sandstone fracture gradients may be
reduced during waterflooding operations due to reduced in-situ stress associated with the
injection of water that is colder than the reservoir. At Pt. McIntyre, water at a temperature of
approximately 70°F is injected into the Kuparuk River Formation, which is at a temperature of
176-184°F. Water injection temperatures at West Beach are also expected to be around 70°F.
Pt. McIntyre EOR Project Application 14
Section K - Hydrocarbon Recovery
20 AAC 25.402(c)(14)
Pt. McIntyre
Current Pt. McIntyre operations involve a combination of processed gas re-injection and pattern
waterflooding, which is expected to yield an estimated total oil recovery of approximately 42 to
45% OOIP for the Pt. McIntyre Pool. The planned hydrocarbon miscible EOR project at Pt.
McIntyre is estimated to increase oil recovery by an additional 32 MMSTB of oil, or approximately
6% of the OOIP within the current 15 pattern waterflood area.
The existing waterflood patterns contain varied reservoir quality with incremental oil recovery
estimates ranging from 4 to 8% OOIP of the targeted oil column under a hydrocarbon miscible
EOR process. These estimates are based on analysis of core from 20 wells distributed around
the field, detailed field wide stratigraphic correlations, PVT and fluid displacement laboratory
studies, and fine scale fully compositional fluid flow reservoir simulations tied back to the
laboratory data. The fine scale results were subsequently scaled up to a field wide scale and the
expected total incremental oil recovery for the entire waterflood area was calculated using the Pt.
McIntyre Full Field reservoir simulation model.
West Beach
The West Beach pool is estimated to have originally contained 15 to 25 MMSTB of oil. Reservoir
modeling studies indicate peripheral waterflooding should improve expected ultimate recovery by
10 to 15% OOIP, yielding approximately 2 MMSTB incremental oil. The benefits associated with
gas injection along the southern bounding fault have not been determined.
Pt. McIntyre EOR Project Application 15
Section L - Proposed Findings
ARCO Alaska, Inc., as Pt. McIntyre and West Beach Operator, respectfully requests that the
Commission consider adopting the following findings for Area Injection Order No. 4C, which
would amend the referenced findings in Area Injection Order No. 4A.
1) Initial enhanced recovery plans for the West Beach Pool call for conversion of one
well, WB -06 or possibly WB -04, to water injection. Injection start-up is expected to
begin fourth quarter 1999. (Finding No. 8, AIO 4A)
2) Fifteen water injection wells and one gas injection well currently exist in the Pt.
McIntyre oil field. ARCO's application includes the locations and mechanical
configuration for all current injection wells, and the locations of all existing and
abandoned wells within the field. (Finding No. 14, AIO 4A)
3) None of the existing or proposed injection wells in the Pt. McIntyre oil field are within
one-quarter mile of the affected area as defined under Conservation Order No. 317A.
(Finding No. 15, AIO 4A)
4) Enhanced recovery for the Pt. McIntyre Oil Pool currently includes fifteen water
injection wells and one gas injection well. The waterflood pattern configuration is
currently inverted nine -spot on nominal 80 -acre spacing utilizing source water, with
conversion to produced water injection under evaluation. (Finding No. 20, AIO 4A)
5) Maximum injection rates for enhanced recovery operations in the Pt. McIntyre Oil
Pool are currently estimated to be about 500 MMSCFD gas, 250 MBD water, and
150 MMSCFD of miscible injectant. (Finding No. 22, AIO 4A)
6) Incremental hydrocarbon recovery of approximately 160 MMSTB is expected from
the Pt. McIntyre waterflood and gas injection project, with an additional 32 MMSTB
expected from the Pt. McIntyre hydrocarbon miscible EOR process. (Finding No. 23,
AIO 4A)
7) Estimated maximum and average injection pressures (psig) for Pt. McIntyre gas
injection are 5000 psi and 4300 psi; for Pt. McIntyre water injection, 2850 psi and
2250 psi; and for Pt. McIntyre MI injection, 4500 psi and 4100 psi. (Finding No. 25,
AIO 4A)
ARCO Alaska, Inc., as Pt. McIntyre and West Beach Operator, respectfully requests that the
Commission consider adopting the following as findings for Area Injection Order No. 4C.
8) The Commission has issued the following Area Injection Orders and approvals for the
Eastern Operating Area of the Prudhoe Bay Unit: Area Injection Order 4 on July 11,
1986, Administrative Approval 4.1 on October 28, 1996, Area Injection Order 4A on
August 12, 1993, revised October 4, 1993, a letter approval on July 5, 1994, and
Area Injection Order 4B on April 13,1998.
9) The hearing records and administrative files for the above listed Area Injection
Orders and approvals remain valid for the Eastern Operating Area of the Prudhoe
Bay Field, and are incorporated by reference into this order.
10) All surface owners within one quarter mile of all proposed injection wells in the Pt.
McIntyre and West Beach fields have been duly notified of the proposed injection
project.
Pt. McIntyre EOR Project Application 16
11) Injection of miscible injectant into the EOR project area is scheduled to commence
during the first quarter of 2000.
12) Within the EOR project area, 15 current water injection wells will eventually be
converted to water -alternating -gas (WAG) service. There are currently 51 producing
wells in the EOR project area.
13) If new production wells are drilled within the EOR project area during the life of the
project, some existing producers may be converted to injectors and receive MI
alternated with water injection.
14) The expected increase in oil recovery from the EOR project is 32 MMSTB,
representing approximately 6% OOIP within the EOR project area.
15) WB -04 and WB -06 have been constructed in accordance with 20 AAC 25.030,
including obtaining cement bond logs above the target injection interval. Conversion
of WB -04 or WB -06 to injection service will be conducted in accordance with 20 AAC
25.412.
16) Injection water for the West Beach waterflood will be produced from the Tertiary
sands, defined as strata common to and which correlate with the interval between
2,500' SS and 4,500' SS in the West Beach State No. 1 well.
17) Future West Beach Pool enhanced recovery plans may include gas re-injection to
displace and capture "attic" oil along the southern bounding fault.
18) To provide artificial lift gas for the West Beach Oil Pool a 4" high pressure line which
would accommodate future gas injection has been installed and is in service.
19) Laboratory testing and geochemical modeling indicate the proposed West Beach
enhanced recovery fluids are compatible with the receiving formation. Commingling
of future West Beach produced water with Pt. McIntyre produced water may cause
barium sulfate scale precipitation in surface facilities. A proactive scale inhibition
program should minimize any surface scale.
20) Some increase in the concentration of hydrogen sulfide gas in the West Beach Oil
Pool may be expected from the introduction of commingled gas from the LPC.
21) Reservoir modeling indicates continued primary production from the West Beach
reservoir during the next year should not adversely affect ultimate recovery.
22) Maximum injection rates for enhanced recovery operations in the West Beach oil pool
are currently estimated to be about 10,000 BWPD or 25 MMSCFD gas.
23) Estimated maximum and average injection pressures for West Beach water injection
are 2850 psi and 2100 psi; for West Beach gas injection 4500 and 4100 psi.
24) Incremental hydrocarbon recovery of approximately 2 MMSTB is expected from the
West Beach waterflood. Benefits associated with gas reinjection have not been
determined.
25) All wells drilled within the West Beach oil field have been constructed in accordance
with 20 AAC 25.030. All wells abandoned or suspended in the West Beach Oil Pool
have been abandoned or suspended in accordance with 20 AAC 25.105.
Pt. McIntyre EOR Project Application 17
ARCO Alaska, Inc., as Pt. McIntyre Operator, respectfully requests that the Commission consider
amending Area Injection Order 4B or Conservation Order No. 317A to add the following new rule
as Rule 11 or Rule 16, respectively.
26) Rule _ Pt. McIntyre Oil Pool Enhanced Oil Recovery Project
a. Injection of miscible injectant for enhanced recovery operations is approved
for the Pt. McIntyre Pool.
b. An annual report must be submitted to the Commission detailing
performance of the Pt. McIntyre Oil Pool Enhanced Oil Recovery Project and
outlining compositional information for the current miscible injectant (MI)
necessary to maintain miscibility under anticipated reservoir conditions.
ARCO Alaska, Inc., as West Beach Operator, respectfully requests that the Commission consider
amending either Area Injection Order 4B or Conservation Order No. 311 A to add the following
new rule.
27) Rule 12 West Beach Oil Pool Annual Reservoir Report
An annual West Beach Oil Pool surveillance report will be required by June 1 of
each year starting in the year 2000. The report shall include but is not limited to
the following:
a) Progress of enhanced recovery project(s) implementation and reservoir
management summary including engineering and geotechnical parameters.
b) Voidage balance by month of produced fluids and injected fluids.
c) Analysis of reservoir pressure surveys within the Pool.
d) Results and, where appropriate, analysis of production logging surveys and
tracer surveys.
e) Results of any special monitoring.
f) Future development plans.
Copies of annual progress reports and plans of development for the West Beach
Participating Area filed with the State of Alaska will fulfill this requirement. If
additional information is required a request will be made by the Commission
within 30 days.
Pt. McIntyre EOR Project Application 18
Section M — Recommended Conclusions
ARCO Alaska, Inc., as Pt. McIntyre and West Beach Operator, respectfully requests that the
Commission consider adopting the following as its conclusions.
1) The requirements of 20 AAC 25.402 and 20 AAC 25.460 have been met for the
injection of fluids for the proposed Pt. McIntyre Oil Pool and West Beach Oil Pool
enhanced recovery operations.
2) Revising Area Injection Order No 4B to include the West Beach oil pool area is
appropriate for authorizing injection of fluids for enhanced recovery operations in the
West Beach oil pool
3) Revising Area Injection Order 4B to incorporate the West Beach oil pool area will not
cause waste nor jeopardize correlative rights.
4) No underground sources of drinking water (USDW) are known to exist in the Eastern
Operating Area of the Prudhoe Bay Unit, the Pt. McIntyre oil field, and the West
Beach oil field.
5) Amending Area Injection Order No. 46 is appropriate for authorizing injection of fluids
for enhanced recovery operations in the Pt. McIntyre, Stump Island and West Beach
Oil Pools.
6) Implementation of the Pt. McIntyre hydrocarbon miscible EOR process via the Pt.
McIntyre EOR Project involves the application of a tertiary enhanced oil recovery
method in accordance with sound engineering principles.
7) The application of the Pt. McIntyre hydrocarbon miscible EOR process is expected to
result in an increase in ultimate hydrocarbon recovery.
8) The proposed Pt. McIntyre hydrocarbon miscible EOR process will be undertaken in
areas of the Pt. McIntyre oil pool where tertiary activities have not been applied
previously.
9) Additional drilling within the EOR project area may be undertaken to improve sweep
in areas of the reservoir unaffected by the hydrocarbon miscible EOR process and to
result in the recovery of oil from areas and reservoir volume not otherwise affected by
the implemented tertiary recovery activities.
10) Injection operations in the Eastern Operating Area of the Prudhoe Bay Unit, the Pt.
McIntyre Oil Pool and the West Beach Oil Pool will be conducted in permeable strata
which can reasonably be expected to accept fluids at pressures less than the fracture
pressure of the confining strata.
11) Specific approvals to convert or drill injection wells will be required.
Pt. McIntyre EOR Project Application 19
Section N — Requested Decisions
ARCO Alaska, Inc., as Pt. McIntyre Operator, respectfully requests that the Commission issue an
order authorizing the underground injection of miscible injectant for enhanced oil recovery for the
proposed Pt. McIntyre EOR Project.
ARCO Alaska, Inc., as West Beach Operator, respectfully requests that the Commission issue an
order authorizing the underground injection of Class II fluids for enhanced oil recovery into strata
defined as those which correlate with and are common to the formations found in the West Beach
No. 4 well between the depths of 14,458' MD and 14,781' MD.
Pt. McIntyre EOR Project Application 20
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® 6 New Pt. McIntyre EOR 0 0 0 0 0 0 0 0 0 New West Beach Pipelines
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Pt. McIntyre Injection Wells
Last ARCO Next MIT
MIT Scheduled
(Date)
(Year)
06/21/97
2001
Last State
2002
07/06/98
2002
Minimum
2002
07/06/98
Injection Well
Packer Depth
2002
Witnessed
2003
09/29/98
2002
Test Pressure
2002
07/06/98
2002
08/08/95
1999
Test
Name
API
(Feet tvdss)
(psi)
(Date)
P1 -G1
500292229800
8199
2050
06/21/97
P1-01
500292201800
8385
2096
None
P1-14
500292233800
8328
2082
07/06/98
P1-16
500292234900
8641
2160
07/06/98
P1-21
500292236300
8610
2153
07/06/98
P1-25
500292193700
8750
2188
07/06/98
P2-09
500292287600
8846
2212
02/02/99
P2-15
500292240900
8870
2218
09/29/98
P2-16
500292239700
8742
2185
09/29/98
P2-23
500292245300
8850
2213
07/06/98
P2-28
500292255100
8860
2215
08/08/95
P2-29
500292240700
8685
2171
None
P2-34
500292255800
4948
1500
08/23/98
P2-42
500292240500
8702
2176
07/06/98
P2-46
500292240100
8286
2072
07/06/98
P2-47
500292262800
8480
2120
06/13/96
Pt. McIntyre Injection Wells
Last ARCO Next MIT
MIT Scheduled
(Date)
(Year)
06/21/97
2001
05/11/98
2002
07/06/98
2002
07/06/98
2002
07/06/98
2002
07/06/98
2002
02/02/99
2003
09/29/98
2002
09/29/98
2002
07/06/98
2002
08/08/95
1999
03/17/98
2002
08/23/98
2002
07/06/98
2002
07/06/98
2002
06/13/96
2000
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Exhibit C- I
Exhibit D-1
Affidavit
STATE OF ALASKA
THIRD JUDICIAL DISTRICT
I, J. W. Groth , declare and affirm as follows:
1. 1 am the Supervisor of Eastern Satellite Development for ARCO
Alaska, Inc., the designated operator of the Eastern Operating Area of the
Prudhoe Bay Unit, and as such have responsibility for West Beach and Pt.
McIntyre operations.
2. On 1999, 1 caused copies of the Application for
Injection and Amendment to Area Injection Order No. 4B with regard to the
Enhanced Oil Recovery Project in the Pt. McIntyre Oil Pool and the Secondary
Recovery Project in the West Beach Oil Pool to be provided to the following
surface owners and operators of all land within a quarter -mile radius of the
proposed injection areas:
Operator: ARCO Alaska, Inc.
Attention: Mr. J. W. Groth
P.O. Box 100360
Anchorage, AK 99510-0360
Surface Owners:
State of Alaska
Department of Natural Resources
Attention: Mr. Mike Kotowski
P.O. Box 107034
Anchorage, AK 99510
Exhibit D-1
Selection within Section 28 (ADL 414852)
City of Barrow
City of Barrow
P. O. Box 629
Barrow, AK 99723
Parcel 16 (USS 9137)
Lawrence Ahmaogak
P.O. Box 411
Barrow, AK 99723
And
C/o Kathleen Dickinson, Land Director
Arctic Slope Native Association, Ltd.
714 Fourth Ave., Suite 201
Fairbanks, AK 99701-4470
Parcel 16 (USS 9267)
John P. Nicholls (minor)
C/o Ely Varner (guardia)
P.O. Box 473
Barrow, AK 99723\
And
C/o Kathleen Dickinson, Land Director
Arctic Slope Native Association, Ltd.
714 Fourth Ave., Suite 201
Fairbanks, AK 99701-4470
Parcel 17 (USS 6905)
Alice Glenn
899 Blair Ave.
Sunnydale, CA 94087
And
C/o Kathleen Dickinson, Land Director
Arctic Slope Native Association, Ltd.
714 Fourth Ave., Suite 201
Fairbanks, AK 99701-4470
Exhibit D-1
George Ahmaogak
P.O. Box 338
Barrow, AK 99723
And
C/o Kathleen Dickinson, Land Director
Arctic Slope Native Association, Ltd.
714 Fourth Ave., Suite 201
Fairbanks, AK 99701-4470
Lawrence Ahmaogak
P.O. Box 411
Barrow, AK 99723
And
C/o Kathleen Dickinson, Land Director
Arctic Slope Native Association, Ltd.
714 Fourth Ave., Suite 201
Fairbanks, AK 99701-4470
Parcel 18 (USS 6906)
Barbara Ahmaogak, Life Estate Holder
1628 Hilton Ave.
Fairbanks, AK 99701
And
C/o Kathleen Dickinson, Land Director
Arctic Slope Native Association, Ltd.
714 Fourth Ave., Suite 201
Fairbanks, AK 99701-4470
Lawrence Ahmaogak, George Ahmaogak and Alice Glenn, remaindermen
(service as provided above)
Exhibit D-1
Parcel NA F-14632
Wallace Oenga, Georgene Shugluk, Leroy Oenga, Michael Delia
and Jennie Oenga (deceased, probate pending)
C/o Kathleen Dickinson, Land Director
Arctic Slope Native Association, Ltd.
714 Fourth Ave., Suite 201
Fairbanks, AK 99701-4470
USS 4044
United States Department of the Navy
U.S. Dept. of Navy
Commanding Officer (Code 05LM)
Engineering Field Activity NW
Naval Facilities Engineering Command
19917 7th Ave., NE
Poulsbo, WA 98370-7570
Dated: 1999.
J. W. Groth
Declared and affirmed before me this day of 1 x �u `� , 1999.
J Notary Public in and for Alaska
My commission Expires: �j Il ItD
Exhibit D-1
•
Alternate
Completion Interva
if needed to
augment water
supply
0
Exhibit E-1
West Beach Shallow Section Type Log
WB -1
•Gi
Subsea JAN
Depth
��• AIG
t
r
AN
l 3000 AN
SV2 Initial Open
Hole Gravel Pack
Completion t-rarget
for Sourcing-, Water
4(XX)
45(X
lti
.P
I
4
�x
t
i
1
7
;
y
i
Exhibit E-1
West Beach Shallow Section Type Log
WB -1
SV2 Initial Open
Hole Gravel Pack
Completion Target
for Sourcing Water
Alternate
Completion Interval 3000
g
if needed to
augment water—
'
supply
,
SV2 Initial Open
Hole Gravel Pack
Completion Target
for Sourcing Water
.2
Post WB6 Net to Gross
West Beach Reservoir Net -To -Gross Ratio Map
Post -Drill West Beach 6 using an 8% porosity cut-off
m
Structural X•Section West Beach
14B ST_3
M -058P61
M6 4 ma
GULL IS ST_3
4
0 X
0 4m
t- Isco -]t
A 3w
454 1
West Beach West to East Structural/Stratigraphic Cross -Section
•
Exhibit G-1
Pt. McIntyre Well Schematic
Conventional Gas Injection Well Design - P1 -G1
Exhibit G-1
Exhibit G-2
Pt. McIntyre Well Schematic
Conventional Water Injection Well Design - 132-47
Exhibit G-2
r
�J
Exhibit G-3
Pt. McIntyre Well Schematic
Slimhole Water Injection Well Design - P2-15
ftKB
2255
2256
TRSSSV
NIP-
PKR ---
NIP
NIP —
TT _—
Perf
Pert-- -
-
tu
i
1E
f
I
{
j
i
P2-15
APL' 500292240900 Spud: 18 -Feb -94 _ PBTD!' 12210 ftKB _
H2S. Ong Compltn: 08 -Mar -94 Max Hole48 deg @ 4042
_ Angle:,
SSSV Type: Last W/� Angle TS: d c7
Annular Fluid: DIESEL T Ref Log Date 05 -Mar -94 Angle @ TD: 45 deg_ & 12220
Reference DIL _...-_-. Last Tag 21Jul-94 _ _
4805
4806
Last T : - 12119' ELMD Last Update: 27 -Jun -98
Rev Reason: - SCH REVISION RKB: 1_47 It
Well T .. INJ KOP: 10 111K
Safety Notes
Date Note
08 -Mar -94 Minimum ID: 3.750" OTIS XN NIPPLE 65 11705' MD
General Notes
Date Note
11597 -
11598
08 -Mar -94 Well Status: ACTIVE
08 -Mar -94 i Tubing Hanger. 4 1/2 _FMC NS Q 28' MD
-Top Of Fluid Depth 0 11788
Last Th 0 12220
Casing Strings - All
Size Weight IGrade Top Btm Feetrsescription
103/4 45.50 NT80 0'. _ 4380
75B -2970 NT80 --01 12210
4380UR.
1221pROD.
CASING
CASING - _....._...
11634-
11635 -
Tubin Stn s -All
Size Weigh Grade Top StmLFeetipescription
41/2 12.00 L-80 01 11727 11727 TUBING
Gas Lift Mandrels/Valves
_
t MD' TVD Man Man Vlv' Vlv Vtv, Viv Vlv Ylv Vlv
Mfr Type ! Mfr. Type Latch Port TROT Run mme
Type
1 4805' 4805' OTIS_ { ; OT ! DM -14W BK ' 0 _ 0.0 GLM
11655 --
11656
2 11597 11597'.OTIS- 'AT' DM -14R' BK 0 0.0' GLM
_Otherlucks, equip., eta JEWELRY
--- - ---
De Descri tion
TypeIOTISXN
a
5th
225:. TRS4-1/2" CAMCO TRDP SSSV, ID=3.812'_
i 11634 NIPOTIS X NIPPLE. ID=3.813"
11655 PKR7-5/8" x 4-1/2" BAKER SABL_-3 PACKER
_
11689 NIPOTIS X NIPPLE.ID=3.813"
11705' NIP NIPPLE, 0=3.75"
11727 TT TUBING TAIL, WLEG 11714' ELMD
11689
11690
Perforations Summary
Interval Zone Status ! Feet SPF Date Comment
!Type
11790-11830 40' 6 21 -Jul -94 I
11920-11970 1 50': 6 21 -Jul -94
i
i
11705
11706-
170611727-
� 11727-
I
i 11726
-•
9
11800
11810-
118:20-
1810 11820Perf
11940 -
j 11960:
Exhibit G-3
Exhibit G-4
Pt. McIntyre Well Schematic
Ultra Slimhole Water Injection Well Design - P2-09
500-
00-100015001
a.omny.ou mea. inn
Size Wei ht Grade
To
1000-
7 26.00
0
15001
95/8 40.00
k
2000-i
SSSV Nip
I`
Size YVeight TGrade lop
---
WRSSSV /
4 12 12.60
2500-
500-3000-3500-4000-4500
Gas Lift M_andrelsNalves
3000-
Man Vlv
Type Mh
12116 - 12166
3500-
KBG-2-L CAI
60 degree
4000-
KBG-2-LCA
�HJ II
45M
5000
I
5500 -
3-3/8"
degree
6000 -,
I
6500 -
7000 -
7500-
500-8000
8000-
i
8500-
500-9000--
9000-
9500-
9500-10000-
10000-
10500 --
10500-11000
11000-
11500 -
PKR
12000 -
NIP -
NIP —'
12500 -
TUBING =
TAIL
09
SL
H2S:
SSSV Type_;
Annular Fluid:..
Reference
L :;
Last Tag:
Rev Reason:
Well T
Safet r�Note:
Diesel to 4000', Ref Log L
SW
4000'-11899'
SWS CET Last
SSSV 4.5"
NIP
W RSSS\ OO
PKR BA?
Max Hole � 56 deg @ 1
Vlv VN Vlv Vivi Vlv
Latch Port TRO Run Commen
Type
BTM I 0 0.01 -May -98
INT
I 1119551 TUBING TUBING TAIL WI WEG 11964' ELM)
TAIL
cuwu- Iguru
a.omny.ou mea. inn
Size Wei ht Grade
To
lou oe9ree
7 26.00
0
HJ 11
95/8 40.00
0
Tubing_Strings . All
proposed
Size YVeight TGrade lop
---
4 12 12.60
squeeze
Gas Lift M_andrelsNalves
t MD' TVD IMan
Mfr
Man Vlv
Type Mh
12116 - 12166
1 4553i 4553; CAMCO
KBG-2-L CAI
60 degree
2 11832I 11832' CAMCOI
KBG-2-LCA
SSSV 4.5"
NIP
W RSSS\ OO
PKR BA?
Max Hole � 56 deg @ 1
Vlv VN Vlv Vivi Vlv
Latch Port TRO Run Commen
Type
BTM I 0 0.01 -May -98
INT
I 1119551 TUBING TUBING TAIL WI WEG 11964' ELM)
TAIL
cuwu- Iguru
[v o ra-u urryi
rsra
lou oe9ree
HJ 11
phasing:
RDX
proposed
squeeze
s
12116 - 12166
50 6 11 -Jul -983-3/8"
60 degree
�HJ II
phasing;
1UC4.3,2
RDX
12264 - 12284
_
20 6 11-Jul-9�
3-3/8"
degree
HJ II
160
phasing; UB1
Exhibit G-4
Exhibit G-5
Pt. McIntyre Well Schematic
Mono -bore Water Injection Well Design - P2-34
ftK6
2091-
2092-
'..
6231-,
6232;
6383-
6384 _
12820-
12821 -
12900-12905-12910-12915
12920 -
13080 -
13090 -
13100-
13110 -
.
SSSV NIP
{
(
i
'
i
PKR —'
-
NIP
Perf -
Perf
'.
P2-34
API: 15002922558001 Sud: 30 -Jun -95
1 PBTD: 13326 ftKB
H2S: I Orig Compltn: 20 -Jul -95 Max Hole 55 deg aQ 8279
An le:
SSSV Type: Last W/O:
Angle Q TS`degA_
Annular Fluo_l DIESEL T Ref LcgOate: 14-Ju1-0An�c
le Cad TD: 49 deg @ 13327
Reference I SWS CDR/GR Last Tag 14 -Jul -98
Log: I Date:
Last Tag;_L3092' SLMD_ Last U_ ate: 24 -Au -98
Rev Reason:' PULL PX PLUG RKB: 52 ft
WeG Typed INJ KOP:, 0 ftKB
SafetyNotes.......
Date_ N_ote
_
20.1ul-95 Minimum ID: 4.562" PARKER SWS NIPPLE cM 2091' MD
General Not.
Date Note
2G -Jul -95 Well Status. ACTIVE
20-JuF95 'Tubing Hanger FMC 3T MD-. _-
Top Of Fluid th 12894 _
Last Tag Depth Q 13326
Casino Strings - All
Size Wei ghtIGrade Top Btnt
Feet Description
9 518 47.00L80 0 6533 _
65331_PROD. CASING
_
Tubing Strings
Size 1Weight_ Grade ;_ Top _. Btm Feed Description_
512 1200 NT80 0 13326 73326iTUBING
Gas lift Mandrels/Valves
tr MD
TVD
ManMan
Mfr
Vlv
Type Mfr
Vlv
Type
Vlv Vlv VW Vlv
Latch Port TRO Run
T e
Vlv
mman
1 6231
6231
HES-LB
'.OT
D -14R
RA
1 0 0.0
GLM
Other (Pius, ss, equip, etc.) -_J _ LRY
--
De th Type IDascriPtion
2091 SSSV 15-1/2" PARKER SWS NIPPLE, tD=4.562"
NIP i
6383 PKR 9-5/8"_X 5-1/2" BAKER LINER TOP 2X_P_ PACKER
_
12820 NIP PARKER SWS NIPPLE, ID=4.562"
Perforations Summary
Interval ;Zone I Status Feet
SPF Date Type Comment
12896-12921 1 1 251
6'01 -Au -91
13070 -13120 1 1 501
6 01 -Aug -9
Exhibit G-5
Well: WB -04 GPMA WEB Date: 4!15/99
ftKB
i
WB -04
API: 500292211700 Well Type: PROD Angle @ TS: deg @
2281
SSSV
SSSV Type: CAT I - SSSV Orig Compltn: 8/8/91 Angle @ TD: 31 deg @ 1491
Annular Fluid: 30000 DI Last W/O: Rev Reason:
2282
Reference GR/DIL/LDT/CNL Ref Log Date: 6/6/91 Last Update: 5/19/98
Log:
Last Tag: 14910 TD: 14909 ftKB
Last Tag Date: Max Hole 65 deg @ 9400
4771
Angle:
Safety Notes
4772
Date Note
6/15/91 Minimum ID: 2.750" OTIS'XN' NIPPLE 14124' MD
General Notes
8735
Date Note
6/15/91 Tubing Hanger. RKB @ 25' MD
8736
6/15/91 Well Status: ACTIVE
Last Tag Depth @ 14910
Top Of Fluid Depth a 14549
11208
Other (plugs, equip., etc. - JEWELRY
Depth TVD Type Description ID
2281 2243 SSSV 3-1/2" OTIS FMX SC SSSV, I0=2.813" 2.81
13056 7691 PKR 9-5/8" x 3-1/2" BAKER'D' PACKER 3.00
11209
12536
14124 8442 NIP OTIS XN NIPPLE, ID=2.75" 2.75
14430 8696 TT TUBING TAIL ELMD 14428' ELMD 4.00
12537
Casing Strings -All
Size Weight Grade Top Btm Feet Description
12936
13.375 72.00 L-80 0 4928 4928 SUR. CASING
9.625 47.00 L-80 0 13443 13443 PROD. CASING
12937JIL,7.000
29.00 L-80 13145 14508 1363 LINER
5.000 18.00 13CR 14208 14909 701 LINER
Tubing Strings - All
13056
PKR
Size Weight Grade Top Btm Feet Description
3.500 9.30 L-80 0 14147 14147 TUBING -IPC
3.500 9.30 13CR 14147 14446 299 TUBING
Gas Lift Mandrels/Valves
13057
Stn MD TVD Man Man V Mfr V Type VOD Latch Port TRO Date Viv
Mfr Type Run Comm
1 4771 3925 CAMCO MMG CA RD 1.5 RK 0.000 0 GLM
(9CR)
13145
2 8735 5742 CAMCO MMG CA RD 1.5 RK 0.000 0 GLM
(9CR)
3 11208 6839 CAMCO MMG CA RD 1.5 RK 0.000 0 GLM
14124
NIP
(9CR)
4 12536 7431 CAMCO MMG CA RD 1.5 RK 0.000 0 GLM
14125(9CR)
5 12936 7625 CAMCO MMG CA E 1.5 RKP 0.000 0 GLM
9CR
Perforations Summary
Interval TVD Zone Status Feet SPF Date Type Comment
14550- 8798-8840 50 4 7/4/91
14600
14620- 8857-8954 114 46/30/91
144301
TT
14734
14754- 8971-8988 20 4 7/3/91
14431
Pert
14774
P14560
Pert
14700
Perf
14760
14770
I
Exhibit G-6
Well: WB -0 GPMA
6 WEB Date: 6/16/99
ftK6
SL
SSSV
WB -06
API: 500292292900 Well Type: PROD Angle @ TS: deg @
2010
SSSV Type: CAT I Ong Compltn: Angle @ TD: 55 deg @ 1821,
Annular Fluid: Diesel & Last W/O: Rev Reason: High tag
Seawater (carbolite)
Reference Ref Log Date: Last Update: 6/13/99
2600
2605
Log:
Last Tag: 16213' SLM TD: 18700 ftKB
7020
Last Tag Date: 6/12/99 Max Hole 69 deg @ 10979
Angle:
7250
Safety Notes
Date Note
9505-
2/2/99 Minimum ID = 3.725" at XN nipple 17393' MD.
3/16/99 Frac Sleeve 2.9" ID 49' long set on 3/14/99 1975' SLM
12190
General Notes
Date Note
1/24/99 In additions to the IPERFs on 3/3/99, there was also 9 shots taken between 17608-18006 du
12195
a SWS RFT.
14595
Fish - FISH
Depth Description Comment
18111 RFT PARTS RFT BOLTS
Other (plugs, equip., etc. - JEWELRY
Depth TVD Type Description ID
2008 1986 SSSV CAMCO 4-1/2" TRM-4E TRSSSV 3.811
16305
17298 8760 NIPPLE X NIPPLE 3.81(
17309 8765 PKR BAKER 7" X 4.5" MODEL S-3 HYDRO SET PACKER 3.88(
17372 8797 NIPPLE X NIPPLE 3.81(
17235
17393 8808 NIPPLE XN NIPPLE (w/ C -SUB ran 5/23/99) 3.72(
17404 8814 TT BAKER WLEG 17405' ELMD 4.00t
Casing Strings - All
17298
NIPPLE
Size Weight Grade Top Btm Feet Description
13.380 68.00 L-80 0 7261 7261 Surface
9.630 47.00 L-80 0 13694 13694 Intermediate
17299
9.630 47.00 L-80 13694 16042 2348 Intermediate
7.000 29.00 L-80 15814 16913 1099 Production
PKR '
7.000 29.00 13CR-80 16913 18210 1297 Production
17309
17310
TubingStrings - All
Size Weight Grade Top Btm Feet Description
4.500 12.60 L-80 0 17405 17405 Tubing
17311
Gas Lift Mandrels/Valves
17312
Stn MD TVD Man Man V Mfr V Type VOD Latch Port TRO Date Vlv,
Mfr Type Run Commc
1 2599 2516 CAMCO MMG CAMCO DMY 1.5 RK 0.000 0 6/3/99
17372
NIPPLE
2 7017 4603 CAMCO MMG CAMCO DMY 1.5 RK 0.000 0 5/15/99
3 9501 5617 CAMCO MMG CAMCO GLV 1.5 RK 0.250 2496 5/25/99
17373
4 12188 6612 CAMCO MMG CAMCO DMY 1.5 RK 0.000 0 5/16/99
17374
5 14592 7604 CAMCO MMG CAMCO GLV 1.5 RK 0.000 2471 5/25/99
6 16300 8304 CAMCO KBG-2 CAMCO MEMORY 1.0 BK 0.000 0 5/26/99
GAUGE
7 17231 8726 CAMCO KBG-2 CAMCO OV 1.0 BK 0.250 0 5/27/99
17393
NIPPLE
Perforations Summary
Interval TVD Zone Status Feet SPF Date Type Comment
17394
17860- 9060-9188 O 230 4 3/3/99 IPERF 60 deg phasing
18090
Stimulations & Treatments
Interval Date Type Comment
17404
TT
17860 - 18090 3/6/99 FRAC 30,000 Ibs of 20/40 LWP
17860 - 17967 3/17/99 FRAC 38,400 lbs of 20/40LWP
17405
FRAC
17860 - 17967 5/19/99 FRAC 124,655 lbs or 20/40 LWP
17900
18000
FRAC
FRAC
RFT
PARTS
18112
18700 J L Exhibit G-7
Exhibit H-1
Pt. McIntyre Miscible Injectant Compositional Analysis
Exhibit H-1
Mole
Component
Percent
Nitrogen
0.41
Carbon Dioxide
9.26
Methane
58.01
Ethane
11.76
Propane
16.15
Iso -Butane
1.70
N -Butane
2.49
Iso -Pentane
0.12
N -Pentane
0.08
Hexane
0.02
Heptane Plus
0.00
Exhibit H-1
0 Exhibit H-2 •
Composition from 9/26/97 Sample # 44590
Exhibit H-2
LPC Reinjection Gas
Component
Value Unit
Hydrogen Sulfide
40 ppm
Carbon Dioxide
7.34 mole %
Nitrogen
0.65 mole %
Methane
79.88 mole %
Ethane
7.3 mole %
Propane
3.75 mole %
I -Butane
0.39 mole %
N -Butane
0.62 mole %
I -Pentane
0.04 mole %
N -Pentane
0.03 mole %
Hexane +
0 mole %
Specific Gravity
0.7171
Composition from 9/26/97 Sample # 44590
Exhibit H-2