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5/21/03 ConservOrdCvrPg.wpd
STATE OF ALASKA
OIL AND GAS CONSERVATION COMMISSION
3001 Porcupine Drive
Anchorage Alaska 99501-3192
THE APPLICATION OF ARCO )
ALASKA, INC. to expand the miscible )
gas enhanced oil recovery project in the )
Kuparuk River Oil Pool, Kupamk River )
Field. )
Conservation Order No. 198A
Kupamk River Field
Kupamk River Unit
Kuparuk River Oil Pool
September 8, 1995
IT APPEARING THAT:
By letter dated June 6, 1995, ARCO Alaska, Inc. applied to the Alaska Oil and Gas Conservation
Commission ("AOGCC") for large scale expansion of the miscible gas enhanced oil recovery
project in the Kuparuk River Oil Pool in the Kupamk River Unit.
2. Notice of opportunity for public hearing was published on June 17, 1995.
.
.
A notice of public hearing was published July 12, 1995 affirming the date, place and time of
hearing and soliciting testimony on topics related to the application
A public hearing was held July 20, 1995. The hearing was recessed on July 20, 1995 and the
record held open until August 7, 1995 to accommodate additional submittals.
FINDINGS:
1. Enhanced oil recovery ("EOR") operations within portions of the Kuparuk River Oil Pool
("KROP") in the Kuparuk River Unit ("KRU") have been underway since 1983 when waterflood
operations began.
2. KRU EOR operations are conducted in accord with and are authorized by Conservation Order No.
198, dated June 14, 1984 and Area Injection order No. 2, dated June 6, 1986.
3. Immiscible water alternating gas injection ("IWAG") was authorized by Administrative Approval's
198.1 and 198.2 and was begun in the KRU in 1985. IWAG is occurring at 17 drill sites with
expansion to the 18th currently in progress.
4. The IWAG process provides two important benefits at the KRU: 1) increased EOR and 2) efficient
gas storage in the absence of a gas cap.
5. KRU miscible water alternating gas injection ("MWAG") was authorized by Administrative
Approval 198.3 and began as a pilot program at drill sites 1Y and 2Z in 1988. This project was
expanded to include drill site lA in 1993. The area of the pilot project was 8700 acres. The Large
Conservation Order No. lA ,
Page 2
Scale EOR Project ("LSEOR") expansion of MWAG will add 59000 acres to the project and
include all 18 IWAG drill sites.
Original oil in place ("OOIP") of the MWAG project will increase from 575 MMSTB to 2900
MMSTB with the LSEOR expansion. Estimated incremental EOR recovery will increase from up
to 40 MMBO in the original project area to 240 MMBO including the expansion area.
Extensive laboratory and field performance data indicate the EOR benefits of MWAG following
waterflooding and IWAG can be significant in the KRU KROP.
8. The LSEOR will make use of existing 1WAG gas distribution infrastructure.
o
10.
11.
12.
13.
14.
15.
16.
17.
18.
Indigenous KRU supplies of enriching fluid to manufacture KROP miscible injectant ("MI") are
adequate to provide expansion to between two and five additional drill sites. Expansion of MWAG
operations to all existing IWAG drill sites will require importing natural gas liquids ('~qGLs") to
the KRU.
The volume of NGLs imported to the KRU will be a large factor in determining the degree to which
MWAG maturity is reached throughout the KRU KROP.
Prudhoe Bay Unit ("PBU") NGLs are proposed as the source of enriching fluid for the LSEOR.
This selection is largely constrained by the current availability of sufficient volumes of NGLs on the
North Slope.
ARCO testified that export of NGLs from the PBU to the KRU for use in the LSEOR would not
effect ultimate recovery from the Prudhoe Oil Pool ("POP").
Laboratory tests, which simulated the KRU KROP physical conditions, were used to establish the
appropriate level of enrichment for a given enriching fluid composition. These tests indicate NGLs
with a wide range of composition are suitable for the manufacture of the KRU KROP MI.
Laboratory and simulation results, calibrated to field performance data, project 5.9 thousand
standard cubic feet of MI can be manufactured from an average barrel of PBU NGL. A barrel of
PBU NGL converted to MI is estimated to yield approximately 1.3 barrels of EOR oil from the
KROP.
The volume of EOR yield per volume of MI injected is partially a function of the ratio of the
volume of MI injected (slug size) versus the total hydrocarbon pore volume. A slug size up to 30%
of the total hydrocarbon pore volume is projected as optimal in the area proposed for the LSEOR.
Incremental oil recovery in the LSEOR project area could be as low as 4% and as high as 10% of
the original oil in place.
Infill drilling of approximately 70 wells will be required to provide adequate solvent sweep and
increase injection capacity in order to achieve the projected goals of the LSEOR.
MI is preferentially carried through higher permeability intervals. The target slug size for the
LSEOR is 30% of the total hydrocarbon pore volume of the most permeable KROP interval.
Conservation Order No. 1~.. · {
Page 3
19.
20.
21.
The LSEOR plan of development depends upon importing 100 million barrels of PBU NGLs for MI
manufacture. This volume, combined with indigenous enriching fluids and returned MI, will
generate a cumulative total of approximately one trillion cubic feet of MI.
The LSEOR is anticipated to yield 200 million barrels of additional oil recovery through project
life, estimated between 15-20 years.
Approximately one third of the imported NGLs should be recovered through stabilization into the
KRU crude stream. The maximum effect these NGLs should have on the vapor pressure of the
KRU crude stream is an estimated increase from 7.9 psia to 9.9 psia based on compositional and
process simulation models.
22. KRU MWAG operations may be expanded beyond the LSEOR project area in the future.
23. The KRU WIOs have agreed to supply NGLs to the LSEOR project in-kind.
24.
25.
26.
27.
28.
29.
PBU NGL can be transported to the KRU via a pipeline from Skid 50 to the Oliktok Pipeline. NGL
volume would be metered leaving Skid 50 within the PBU and again upon entering the KRU
distribution infrastructure.
Facility improvements include installation of remote control valves on either side of the Kuparuk
River on the Oliktok pipeline, three pipeline pumps at the Central Processing Facility - 1 ("CPF-I")
to boost pressure of NGLs for transport to Central Processing Facility - 2 ("CPF-2"), an 8 inch
NGL pipeline from CPF-1 to CPF-2, collection drums at CPF-1 and CPF-2 and injection pumps at
CPF-1 and 2, which will be upgraded to 360 gpm and 800 gpm respectively.
Indigenous MI components from the KRU include NGLs from the CPF-1 gas plant, scrubber
liquids from artificial lif~ compressors at CPF-1 and CPF-2, NGLs from fuel gas conditioning skid
at CPF-2 and naphtha from the KRU topping plant.
NGLs could be imported from the PBU starting in fourth quarter 1995 at a 2000-4000 BPD rate.
The project would be fully implemented in fourth quarter 1996 with importation of 20,000-30,000
BPD of NGL. MI injection will increase from 65 MMSCF/D to 95 MMSCF/D in fourth quarter
1995 and at full implementation will reach 220 MMSCF/D.
Minimum miscibility pressure is expected to be 2900 psi and will be controlled by appropriate
mixing of lean gas and available enriching liquids.
Injection pressure is expected to average 3800 psi in MI injection wells and 2700 psi in water
injection wells within the expanded MWAG area.
CONCLUSIONS:
o
Conservation Order 198, Administrative Approvals 198.1, 198.2, 198.4 and Area Injection Order
No. 2 authorized enhanced recovery waterflood operations, immiscible water alternating gas and
miscible water alternating gas projects in the KROP.
Conservation Order No. 1~~. . (
Page 4
2. Expansion of the MWAG enhanced oil recovery process will add 18 drill sites covering 59000 acres
to the project area and will recover significant additional oil over the life of the project.
3. Conservation Order 198 may be amended to accommodate expansion of the enhanced recovery
operations to include the entire affected area of the Kupamk River Oil Pool within the KRU.
4. Nothing in this record requires the owners of the PBU to make NGLs available for import to KRU
or to increase the total volume of NGLs being produced by PBU.
5. Expanding the affected area for application of the MWAG process to the boundaries of the KRU
will enhance the flexibility of future expansion of MWAG operations.
6. The LSEOR project requires importing a minimum 100 million barrels ofNGLs, infill drilling 70
wells, establishing adequate injectivity and expanding to at least 18 drill sites to achieve goals
outlined in hearing testimony.
7. Expansion of MWAG in the Kuparuk River Unit KROP will increase ultimate recovery, will not
cause waste nor violate correlative rights.
8. Surveillance activity covering reservoir development, waterflood, miscible and immiscible flood
operations reporting should be consolidated into one report documenting significant activity on an
annual basis.
9. The use of PBU NGL will not affect ultimate recovery from the Prudhoe Oil Pool.
10. The record for this order should include the hearing record and administrative files related to
Conservation Order 198
NOW THEREFORE IT IS ORDERED THAT Conservation Order 198 is amended and the rules
hereinat'rer set forth apply to the following affected area:
Umiat Meridian,
T14N
T14N
T13N
T13N
T12N
T12N
T12N
T12N
TllN
TllN
TllN
TllN
T10N
T10N
T10N
R8E
R9E
R8E
R9E
R8E
R9E
R10E
RllE
R8E
R9E
R10E
RllE
R8E
R9E
R10E
Sections 24, 25, 36
Sections 19, 30, 31
Sections 1-3, 10-12, 13-15, 19-36
Sections 1-12, 15-22, 25-36
Sections 1-4, 9-16, 21-28, 33-36.
All
Sections 3-10, 14-23, 25-36
Section 31
Sections 1-4, 9-16, 21-36.
All
All
Sections 5-8, 16-22, 29-31
Sections 1-24, 27-34.
Sections 1-14, 17-20, 23, 24
Sections 1-12, 17-20,
,,
Conservation Order No. 1~ .,
Page 5
Rule 1. Well Spacing.
Within the area affected by this order, four wells may be drilled per governmental quarter section except
for governmental sections adjacent to the Kuparuk River Unit boundary where one well may be drilled
per quarter section. The pool may not be opened to a well bore within 500 feet from the Kupamk River
Unit boundary nor closer than 1000 feet to the Pool opened to the well bore in another well.
Rule 2. Administrative Action.
Upon its own motion or upon written request, the Commission may administratively amend these rules
to enhance the efficiency of EOR projects so long as the change does not promote waste nor jeopardize
correlative rights and is based on sound engineering principles.
Rule 3. Kuparuk River Unit Reservoir Surveillance Program
The Unit Operator will submit an annual report to the commission on the Kupamk River Oil Pool
development and enhanced recovery operations. The report will be submitted by April 1 of each year
for the period ending December 31 and will include but is not limited to the following information:
1. Progress of enhanced recovery project(s) implementation and reservoir management summary
including engineering and performance parameters.
Voidage balance by month of produced fluids, oil, water and gas, and injected fluids, gas,
water, low molecular weight hydrocarbons, and any other injected substances which may be
filed in lieu of monthly Forms 10-413 for each EOR project.
3. Analysis of reservoir pressure surveys within the field.
4. Results and where appropriate, analysis of production logging surveys, injection surveys, tracer
surveys and observation well surveys.
5. Results of MI surveillance efforts including a summary and analysis of returned MI,
representative or periodic composition of MI and an estimate of MMP.
6. Current and future LSEOR project scope, timetable or utilization of NGL for MI.
Rule 4. Injectivity Profiles.
An injection profile survey will be obtained on each well with A and C sand injection within the first
nine months of sustained multiple zone injection. One third of all multiple zone injectors will be
surveyed each calendar year. The completed injection surveys will be filed with the Commission within
90 days atter performing the survey.
Rule 5. Approval of Expansion of the KRU Miscible Gas Injection Project.
Expansion of the KRU Miscible Gas Injection Project is approved for the area of the Kupanfl~ River Oil
Pool within the Kuparuk River Unit.
Conservation Order No. l.~ .~
Page 6
Rule 6. Importation of PBU NGL.
The Commission approves, but does not require, importing up to 30,000 BPD of PBU NGLs for use in
the KRU Miscible Gas Injection Project.
DONE at Anchorage, Alaska and dated September 8, 1995.
Russell A. Douglass,' Commissione~
~Tuckerman Babcock, Commissioner
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 p.m. on the 23rd day following the date of the order,
or next working day ifa holiday or weekend, to be timely filed. The Commission shall g/ant 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 (i.e., 10th day at~er the application for reheating was filed).
AOGCC HEARING QUESTIONS
& FOLLOW-UP ANSWERS
During the July 20, 1995 Public Heating on the Kuparuk LSEOR Project,
ARCO agreed to provide additional information regarding six items of interest to
the Commission.
QI:
How will the vapor pressure of the Kuparuk stream be
affected by the LSEOR project? (Transcript at 41-42)
A.'
We have estimated the maximum effect on the vapor pressure of the
Kuparuk stream resulting from the LSEOR project to be an increase of
approximately 2 psi.
We performed this analysis using a compositional Kuparuk facility model
and a compositional TAPS PS#1 vapor pressure analyzer model. Based
on current conditions (without LSEOR), these models calculate a
Kuparuk crude oil vapor pressure of 7.9 psia (TVP). The Kuparuk / Milne
Pt. blended stream vapor pressure reported by Alyeska is generally in
the range of 6-8 psia (TVP), confirming the reasonableness of our model.
The maximum Kuparuk vapor pressure effect of the LSEOR Project
should occur when the ratio of exported NGLs to crude oil is at a
maximum. Based on the Project scope presented to the Commission,
this NGL-to-crude ratio is expected to peak around the year 2011 at 6-
7%. Introduction of sufficient PBU NGLs into the front end of the facility
model to produce a 6-7% exported NGL-to-crude ratio results in a
Kuparuk stream vapor pressure of 9.9 psia (TVP). Therefore, a maximum
vapor pressure rise of approximately 2 psia is anticipated. This
maximum vapor pressure is well below the TAPS vapor pressure limit of
14.2 psia (TVP).
- 1 - August 1, 1995
Q 2:
What NGL composition was assumed in calculating that one-
third of the imported NGL volume will ultimately stabilize in
the Kuparuk export stream, and has ARCO evaluated the
effect of PBU NGL composition variations on the LSEOR
Project's NGL recovery factor? (Tr. 48)
A:
For the purposes of evaluating the LSEOR Project, a range of information
provided by the Prudhoe Bay Unit Operators regarding NGL composition
was reviewed. The following NGL composition was selected as being
representative of the average NGL composition over the life of the
Project:
CQmponent Mole %
propane 0.1
isobutane 4.1
normal butane 24.5
isopentane 14.4
normal pentane 19.8
hexane 19.2
heptane 12.5
octane plus 5.4
There are many factors which are likely to affect the LSEOR Project's
ultimate NGL recovery, including:
· MI enrichment level,
· MI slug size injected,
· Reservoir trapping of the MI,
· Composition of the returned MI,
· Facility recapture of the returned MI, and
· Duration of the Project.
While some of these factors are dependent on PBU NGL composition,
the sensitivity of ultimate NGL recovery to NGL import composition has
not been analyzed.
- -2- August 1, 1995
Q 3:
What total volumes of Kuparuk enriching fluid and Kuparuk
lean gas will be injected during the 15 to 20-year Project life?
(Tr. 52)
A.'
Approximately 30-40 MMBBL of Kuparuk indigenous enriching fluid and
700-800 billion SCF of Kuparuk lean gas will be injected into the 18
additional LSEOR drill sites over the life of the Project. These are gross
injection volumes. If recycled volumes due to the bootstrap effect are
deducted, the net indigenous enriching fluid injection volume is
approximately 20-25 MMBBL. Of this net indigenous enriching fluid
injected, only about 50% would stabilize in the Kuparuk crude if it were
diverted to the CPF oil trains rather than injected as MI.
Q4:
Would you provide a copy of the agreement which addresses
the NGL supply arrangements? (Tr. 57-58)
A: See attached.
Q5: What is the projected capital cost for drilling? (Tr. 62)
A-'
The projected capital cost associated with drilling approximately 66 new
wells within the LSEOR Project area, is $125-135 million (in 1995
dollars). This estimate includes the costs of drilling, completing,
stimulating, and connecting these wells to the production or injection
infrastructure.
- 3 - ~ August 1, 1995
Q6:
Can you provide projected Kuparuk production profiles with
and without the LSEOR Project? (Tr. 64)
Am
The LSEOR Project is expected to produce the incremental production
profile set forth below. This profile will hold Kuparuk production level
until approximately the year 2000 after which decline will set in.
LSEOR Production
Year (MBPD)
1995 0
1996 2
1997 19
1998 33
1999 32
2000 38
2001 44
2002 43
2003 38
2004 40
2005 46
2006 48
2007 43
2008 42
2009 42
2010 40
2011 38
2012 31
2013 20
2014 14
2015 7
The LSEOR incremental production profile includes the following rate
adjustments for the 18 additional LSEOR drill sites:
+ EOR oil due to PBU NGLs
+ Stabilized returned MI liquid due to PBU NGLs
- Salable indigenous enriching fluid injected as MI
+ EOR oil due to indigenous enriching fluid
+ Stabilized returned MI liquid due to indigenous enriching fluid.
These rates are based on the EOR recovery curves described in Shaun
Hoolahan's testimony, expected drill site injectivities with the proposed
new wells, expected facility performance, and expected NGL import
rates.
-4- August 1, 1995
ARCO Alaska, Inc.~,
Legal Department
Post Office Box 100360
Anchorage Alaska 99510
Telephone 907 265 1354
Daniel G. Rodgers
Senior Attorney
August 2, 1995
HAND DELIVERY
Mr. David W. Johnston, Chairman
Mr. Russell A. Douglass, Commissioner
Mr. Tuckerman Babcock, Commissioner
Alaska Oil and Gas Conservation Commission
3001 Porcupine Drive
Anchorage, AK 99501-3193
Re:
The Application of ARCO Alaska, Inc. for Approval
To Initiate a Large-Scale Enhanced Oil Recovery
Project in the Kuparuk River Unit
Dear Mr. C'hairman and Commissioners:
At the July 20, 1995 public hearing on ARCO Alaska's application for 'the Kuparuk
Large-Scale EOR Project, the Commission asked ARCO to provide additional
information with respect to six items that came up during the hearing. Enclosed please
find ARCO Alaska's responses, which have been reviewed and agreed to by BP and
Unocal. We ask that the enclosed responses be included as part of the record in this
matter.
Very truly yours,
Daniel G. Rodgers
enclosures
c/Hand Delivery:
Mr. Chris Costelloe, Unocal (w/encl)
Mr. Andy Inglis, BP (w/encl)
AUG 02 1995
Alaska Oil & Gas Cons. Commission
Rnchorage
ARCO Alaska, Inc. is a Subsidiary of Atlantic RichfleOd Company
KUPARUK RIVER UNIT
LARGE SCALE ENHANCED OIL RECOVERY PROJECT
OPERATING PROCEDURES
This agreement is entered into by and among the parties who have signed
this agreement or a counterpart of this agreement, regardless of whether it
is signed by all Kuparuk Participating Area ("KPA") Working Interest
Owners ( "WIOs'3.
.~. RECITALS.
I. A Kuparuk River Unit I"KRU") Enriched Gas Enhanced Oil Recovery
"EOR") Project was approved bv Conservation Order No. 198.3 of the
Alaska Oil and Gas Conservation Commission for the tertiarv recovery of oil
from the Kuparuk River Reservoir through injection of an enriched gas
miscible injectant. The initial phase of this approved project was initiated
at KPA Drill Sites I Y and 2Z in 1988 under the project name of Small Scale
EOR ("SSEOR"~ and was expanded to Drill Site IA in 1993.
2. The Large Scale EOR ("LSEOR") Project. as included in the KRU Field
Development Plan, is a significant expansion of the SSEOR Project. The
LSEOR Project is currently under evaluation by the KPA WIOs for the
purpose of increasing the economic recovery of oil from the Kuparuk River
Reservoir. Implementation of the LSEOR Project will require acquisition of
enriching fluid, herein referred to as solvent, from a source outside the
KRU to be blended with lean gas from the Kuparuk River Reservoir to
make miscible injectant.
3. The LSEOR Project scope, funding requirements, and timing are
summarized in Exhibit A for informational purposes only. These elements
are subject to revision prior to execution of the Project funding documents.
4. The parties hereto desire to set forth and agree upon the method
of operation, method of solvent acquisition, and allocation of the obligation
to provide outside solvent for the [_SEOR Project.
5. Article iV of Exhibit [ of the Kuparuk River Unit Operating
Agreement ("KRUOA") provides, among other things, that {a) the Operator
is responsible for Joint Account Material and shall make proper and timely
charges and credits ~'or all material movements affecting the Joint
Property, and (b) the Operator shall procure all Materials and services for
use on the Joint Property and. at the Operator's option, such Materials and
~ervices mav be supplied bv the Non-Operators.
6. Article i of Exhibit i of the KRUOA defines the Joint Account as the
account showing the charges and credits accruing because of the Joint
Operations and which are to be shared by the Parties.
7. Article [ of Exhibit I of the KRUOA defines Material as personal
property, equipment or supplies acquired or held for use on the Joint
Property.
8. Section 4.304 and Subsection 4.304.01 of the KRUOA provide that
a Master Commitment Authorization ("MCA") will be required for
submission to the KPA WIOs for.. their approval with respect to any
recovery mechanism other than waterflood and that approval is required
by an 88% affirmative vote of the KPA WIOs.
9. Section 4.305 and Subsection 4.305.04 of the KRUOA provide that
a' Component Authorization For Expenditure ("Component AFE") will be
required for submission to the KPA WIOs for their approval with respect to
each item or group of items identified in or arising out of an approved
MCA when the cost of such item or group of items exceeds the Operator's
Expenditure ..X. uthoritv. The approval requirement t'or any such
Component AFE is a 68% affirmative vote of the KPA WIOs.
B. AGREE~NT.
l. General Provisions
1.1 This agreement establishes procedures for the KRU LSEOR Project
governing the following activities'
al method of operation of the LSEOR Project facilities:
b) allocation of the obligation to supply outside solvent for
blending with Kuparuk lean ~as to make miscib.le injectant: and
c l acquisition or' outside solvent for blending with Kuparuk
lean gas to make miscible injectant.
1.2 This agreement shall be effective as to each signatory on the
date signed by that KPA WIO and shall remain in effect during the term of
the LSEOR Project: provided, however, that this agreement may be
terminated as to any signatory to this agreement by written notice by that
KPA WIO at any time before approval of the LSEOR Project MCA.
1.3 Upon approval of the LSEOR Project MCA and the associated NGL
Component AFEs. the signatories to this agreement shall be committed to
supply outside ,solvent. either in kind or in value, in accordance with the
terms of the Project MCA. the Component AFEs. and this agreement.
1.4 The LSEOR Project Operating Procedures may be amended by a
98% affirmative vote of the signatories to this agreement, which voting
level shall be based on the signatories' normalized KPA Area Participationi
provided however that the PBU NGL import rates, as set forth in Paragraph
B.2.4 below, may be amended by an 88% affirmative vote of the KPA WIOs.
1.5 Termination of the LSEOR Project. including each KPA WIO's
oblioation~ to supply, outside solvent, will require an 88% affirmative vote
of the K. PA WIOs.
1.6 Unless otherwise specified, all capitalized words in this
agreement shall have the same meaning as ziven them in the KRUOA.
2. LSEQR Project Operations
2.1 Prudhoe Bav Unit /"PBU") Natural Gas Liquids ("NGLs"), as
defined in Paragraph 5.3 of the Amended and Restated Prudhoe Bay Unit
NGL/EOR Project Operating Procedures and Flow Station 3 Injection Project
Operating Procedures. are hereby approved as the outside solvent acquired
to make miscible iniectant for the LSEOR Project. The estimated volumes
of PBU NGLs required by the KRU over the expected life of the LSEOR
Project are set forth in Exhibit B.
2.2 Acquisition of alternative solvents to PBU NGLs shall require
amendment of this agreement.
2.3 [t is expected that NGLs transported from the PBU to the KRU
will be shipped through the 16" pipeline owned by the Oliktok Pipeline
Company ("OPC"). Upon approval of this agreement and the LSEOR Project
MCA. the KRU Operator shall request that OPC convert the 16" pipeline to
service as a carrier of NGLs from the PBU to the KRU.
2.4 The KRU LSEOR Project facilities shall be operated in a prudent
manner to maximize Kuparuk River Reservoir oil recovery through
injection of enriched gas miscible injectant. [n pursuit of this objective, the
Operator shall first utilize all KRU produced solvent, including scrubber
liquids from Central Processing Facilities ("CPFs") No. i and No. 2, naphtha
from the KRU Topping Plant. KRU NGLs from CPF No. 1, and fuel gas liquids
from CPF No. 2. Secondarily, PBU NGLs will be imported so as to maximize
use of (a) solvent injection pump facilities. (b) excess available lean gas, or
(c) immature EOR target patterns. However. the PBU NGL import volume
for any month shall not exceed that volume of xvhich BP Exploration
(Alaska) lnc.'s allocated share of PBU NGLs is adequate to supply: (a) its
own Solvent Supply Obligation. as defined in Paragraph 3 below' plus (b)
the Solvent Supply Obligation of any KPA WIO that does not own a share of
PBU NGLs.
3. Allocation of Solvent Supply Obligation
[n accordance with the terms of this agreement and subject to
approval of the Project MCA and associated NGL Component AFEs. the KPA
WIO's are obligated to supply PBU NGLs. either in kind or in value
t"Solvent Supply Obligation"). The sharing ratios for the Solvent Supply
Obligation shall be the f,~RU Cost Participation i decimals. From and after
January I. 2000, cacta KPA WIO's Cost Participation and. [herefore, its
Solvent Suppiy Obligation sharing ratio shall equal its Area Participation,
pursuant to Article 2 c)f the KRUOA.
4. Solvent Acquisition Procedures.
4.1 The KRU Operator shall acquire PBU NGLs for the LSEOR Project
in accordance with the provisions of the KRUOA, subject to the provisions
below regarding the election of individual KPA WIOs to supply PBU NGLs
in kind.
4.2 [n accordance with the terms of this agreement and Section IV
of Exhibit [ of the KRUOA, the Operator shall consent to elections by Non-
Operators to supply PBU NGLs in kind ("Supply in Kind Option") up to their
Solvent Supply Obligations.
4.3 The Suppty in Kind Option shall be a renewable commitment by
a KPA WIO to supply a specified percentage of its Solvent Supply
Obligation. The initial commitment period shall be from LSEOR Project
start-up t,i.e., the commencement of PBU NGL deliveries) through December
31, 1997. Thereafter. the Supply in Kind commitment shall be for a two-
year period and shall be renewed biennially.
4.4 Supply in Kind notifications and elections shall be made in
accordance with Exhibits C and D.
4.5 If bv the Supply in Kind Option election deadline, the Supply in
Kind Option commitments for the following Supply in Kind term total less
than 100% of each KPA WIO's Solvent Supply Obligation. the Operator shall
enter into a solvent purchase contract or contracts on behalf of the KPA
WIOs ("Solvent Contracts") for the acquisition of sufficient PBU NGLs to
meet the LSEOR Project's PBU NGL requirements not covered bv the Supply
In Kind Option.
-[.6 The Operator shall award the Solvent Contracts in accordance
with competitive bidding procedures, and the Non-Operators shall have the
right to audit the Operator's accounts and records related to the Joint
Account pursuant to Exhibit [ of the KRUOA.
4.7 The parties executing this agreement shall not object to or
challenge -- under the audit provisions of the KRUOA or otherwise -- the
price of PBU NGLs acquired for the LSEOR Project pursuant to Solvent
Contracts approved according to the terms of these Operating Procedures.
4.8 All acquisition and transportation costs associated with the PBU
NGLs acquired under the Solvent Contracts shall be charged to the Joint
Account. That part of the Joint Account attributable to the PBU NGLs
acquired under the Solvent Contracts shall be funded by the KPA WIOs
which have not elected to supply their entire Solvent Supply Obligation
through the Supply in Kind Option. Said KPA WIOs shall share the funding
in proportion to the volume of NGLs acquired on their behalf under the
Solvent Contracts.
4..9 All costs associated with PBU NGLs provided by the KPA WIOs
pursuant to the Supply in Kind Option. including, but not limited to,
purchase price, royalties, transportation (if not arranged for by the
Operatorl, and taxes shall be the responsibility of each KPA WIO providing
such NGLs and shall not be charged to the Joint Account. The charges for
transportation through OPC's pipeline which are arranged bv the KRU
Operator shall be charzed to the Joint Account and funded bv the KPA
WIOs on whose behalf the Operator has arranged such transportation.
4.10 Volume nominations and associated accounting procedures for
PBU NGL shipments made pursuant to the Solvent Contracts shall be made
bv the Operator in accordance with Exhibit D. Volume nominations and
associated accounting procedures for PBU NGL shipments made pursuant to
the Supply in Kind Option shall be coordinated in accordance with Exhibit D
between the Operator and the KPA WIOs supplying such NGLs.
4.11 The procedures for forecasting and nominating LSEOR Project
?BU NGL requirements as set forth in Exhibit D mav be changed by the
Operator from time to time upon 60 days prior written notice and with an
88% affirmative vote of the KPA WIOs.
IN WITNESS WHEREOF, the parties hereto have executed this
agreement on the dates set forth below.
ARCO Alaska. Inc.
By: ~ _ a'..,.-//_. ,/-t /.>-~,_/-,--/ Date ,,/-~.~
Title' Sr. Vice Presicr~nt, ~-(tmaruk/Cook Inlet Business Unit
Date'
,,
~ ZO~ 459 70 I_i~., R,g PR~HT~HG
Exxon !Corporation
Title:
Mobil ~il CCrporation
By: I ., .
Title:
Union 43ii CC~mpany of California
By: ,
Title'[
Date' (,,'/J ?/~a~'''
Date:
Date:
Date:
Chevron U.S.A. Inc.
Bv:
Title:
Date'
Exxon Corporation
By:
/,
Title'
Date:
Mobil Oil Corporation
By:
Title:
Date:
Union Oil Company of California
By:
Title:
Date:
.... - .... e~- ; ,.-..c. ~,¢: 2. -'" ' -: MEP'U~_ CF_.O
Chavron U.S.A. £n¢.
By:
Title:
Date:
Exxon Corporauon
By:
Title:
Data'
Mo{~i! Oil Corporation /~
Umon Oil Company of Calit~ortua
By:
Title:
Dat~:
EXHIBIT A
KUPARUK RIVER UNIT
LARGE SCALE ENHANCED OIL RECOVERY PROJECT
SCOPE. FUNDING REQUIREMENTS. AND TIMING
Project Scope
The LSEOR Project will be a significant expansion of the KRU's present
Enricheci Gas EOR Proiect ',~t Drill Sites i.-X. i Y. and 2Z. This project will
~nvotve the aCOulsition ~ i t~vdrocarbon solvent from at source outside the
KRU to be blended with lean gas from the Kuparuic River Reservoir and re-
injected as miscible in.jectant. PBU NGLs are currently the only approved
outside solvent for making miscible injectant. The LSEOR Project includes
the following maior :~ctivities.
· Import NGLs from the PBU to the KRU via the existing 16" Oliktok
Pipeline. NGL tie-in and metering facilities will be provided in the
vicinitv of PBU Skid 50 bv ARCO and BP as two of the PBU WlOs who
intend to ship NGLs to Kuparuk.
¥ iving, umging, and blending facilities at KRU's
· Provide . GL ~'ece p
Central Processinz Facilities ("CPFs") No. I and No. 2 to blend PBU
NGLs with Kuparuk River Reservoir lean gas to produce miscible
injectant.
· Utilize the existinz immiscible ~,as distribution infrastructure to
deliver miscible injectant to KRU drill sites for injection. Within the
economic life l)r' the Kuparuk River Reservoir. approximately 20 drill
sites will Iiketv receive miscible injectant as a result of PBU NGLs
acquired under the LSEOR Project.
EXHIBIT A
Pa~e 2
P,roject Fundirlg Requirements
Since the LSEOR Project involves a recovery mechanism other than
waterflood, an MCA is required by the KRUOA. Approval of multiple
Component AFEs will be requested over the life of the LSEOR Project for
funding of facilities and PBU NGLs. In accordance with the KRUOA, the
Project MCA will require an 88% affirmative vote of the KPA WIOs, and
each Component AFE will require a 68% affirmative vote of the KPA WIOs.
The following KRU funding documents are anticipated for the LSEOR
ProJect.
· LSEOR Project MCA
· LSEOR Component AFEs - Facility Additions & Modifications
- Phase 1 PBU NGL Commitment
Phase 2 PBU NGL Commitment
- Phase 3 PBU NGL Commitment
- Phase 4 PBU NGL Commitment
(Start-up - 12/31/99)
(1/1/2000 - 12/31/03)
(1/1/04 - 12/31/07)
(1/1/08 - 12/31/11)
Project Timing
Upon approval of the LSEOR Project MCA and associated Component AFEs.
the Project will be implemented as soon as is feasible (possibly as early as
October. 1995). For planning purposes, however, the following funding
schedule supports start-up of the LSEOR Project within the fourth quarter
of 1995 with full facility implementation by mid-1996.
· LSEOR Project MCA
· LSEOR Component AFEs - Facility Additions & Modifications
- Phase I PBU NGL Commitment
- Phase 2 PBU NGL Commitment
- Phase 3 PBU NGL Commitment
- Phase 4 PBU NGL Commitment
First Quarter. !995
First Quarter. 1995
First Quarter. 1995
July 1. 1999
July 1, 2003
July 1, 2007
EXHIBIT B
KUPARUK RIVER UNIT
LARGE SCALE ENHANCED OIL RECOVERY PROJECT
ESTIMATED VOLUMES OF PBU NGLs
(1)
?BU NGLs
Year Daily Volume
(MBPD)
1995 3
1996 16
1997 25
1998 22
1999 19
2OOO 16
2001 18
2002 20
2003 20
2004 19
2005 18
2006 18
2007 15
2008 12
2009 9
2010 6
Total -
PBU NGLs
Annual Volume
(MBBL)
200
6.000
9.000
8.200
6.900
6,000
6,500
7,500
7,400
7.000
6.500
6.600
5.400
4.300
3,400
2,200
93,100
Assumes a fourth quarter. 1995 start-up. The
NGLs imported during 1995 and 1996 will
Project start-up date.
actual
depend
volume of PBU
on the actual
EXHIBIT. C
KUPARUK RIVER UNIT
LARGE SCALE ENHANCED OIL RECOVERY PROJECT
NOTICE OF ELECTION OF SUPPLY IN KIND OPTION
TO: ARCO ALASKA. INC.
I. In accordance with Paragraph B.4.4 of the LSEOR Operating
Procedures. the undersigned KPA WIO herebv elects to supply ~% of
its LSEOR Solvent Supply Obligation in kind. .,nv additional PBU NGLs
required to meet the undersigned's Solvent Supply Obligation will be
supplied bv the KRU Operator under the Solvent Contracts pursuant to this
agreement.
2. [.The election in (1) above is an irrevocable commitment to supply
PBU NGLs in kind for a period beginning upon LSEOR Project start-up (i.e.,
the commencement of PBU NGL deliveries) and ending December 31, 1997
("Delivery Period").1
or ,
[The election in (I) above is an irrevocable commitment to supply PBU
NGLs in kind for a period of two years beginning January I. ("Delivery
Period").]
3. Each month during the Delivery Period. the undersigned shall
provide the elected percentage in ('1) above of its Solvent Supply
Obligation. The undersigned shall deliver PBU NGLs at such rates as the
Operator shall request in accordance with procedures set forth in Exhibit D
of the LSEOR Operating Procedures.
4.. The delivery point for PBU NGLs supplied bv the undersigned
shall be the Oliktok Pipeline Company's ("OPC's") connection at the point of
receipt within the Kuparuk River Unit /"KRU point of receipt").
EXI-tm 1T C
Pa~e 2
5. The condition oi the PBU NGLs supplied bv the undersigned shall
reasonably match OPC's pipeline pressure and temperature as they exist
therein from time to time.
6. The delivery quality of the PBU NGLs supplied bv the undersigned
shall be "as produced" from the PBU Central Gas Facility.
7. The undersigned warrants title to the PBU NGLs delivered by it
hereunder. Title to the PBU NGLs shall be deemed to pass to the KRU
Operator on behalf of the KPA WIOs from the undersigned at the KRU point
receipt.
8. The undersigned shall be responsible for the costs of all PBU NGLs
supplied by it hereunder, including, but not limited to, the purchase price,
royalties, and taxes. Transportation shall be handled as follows:
CHECK OPTION (A) OR (B)
Option A
Operator. as agent for the undersigned, shall arrange for transportation of
the PBU NGLs through OPC's pipeline to the KRU point of receipt. The
charges for such transportation shall be charged to the Joint Account and
funded by the undersigned. The undersigned shall indemnify, defend, and
hold the Operator harmless from and against any and all claims and
liabilities arising out of said transportation services.
Option B
The undersigned shall arrange for transportation of the ?BU NGLs through
OPC's pipeline to the KRU point of receipt and shall be responsible for all
such transportation charges.
EXHIB~ C
Pa~e 3
The undersigned may change the above election at any time during the
Delivery Period ur>on 60 davs prior written notice to the Operator.
9. In the event the undersigned, bv reason of an event of force
majeure, is rendered unable wholly or in part. to perform its obligation
hereunder, then upon the undersigned's giving notice and particulars of
such event, its obligation to perform shall be suspended or correspondingly
reduced durinz the continuance of any inabilitv so caused, but in no
greater amount than required bv the event of force majeure and for no
longer period. The effect of such event shall, so far as possible, be
remedied :vith all ~'easonable and prompt dispatch. Force majeure means
any event bevonu the controi of the undersizned and which bv the
exercise of due diligence the undersigned is unable to prevent or
overcome, includin,.z, but not limited to. an act of God. fire. t'lood, volcano.
earthquake, explosion, sabotage, and act of the public enemy, civil or
military authoritv, including court orders, injunctions and orders of
governmental agencies of competent jurisdiction, insurrection or riot, an
act of the elements, t'ailure of equipment, or the inability to obtain or ship
equipment or materials because of the effect of similar causes on carriers
or shippers. Strikes, lockouts, and other labor disturbances shall be
considered events of force majeure, and nothing herein shall require the
undersigned to settle :~ labor dispute against its best judgment.
10. This election and the obligations hereunder are subject to the
LSEOR Operating Procedures.
KPA WORKING h-NTE~ST OWNER
Companv'
By'
Title'
Date:
EXHIBIT D
KUPARUK RIVER UNIT
LARGE SCALE ENHANCED OIL RECOVERY PROJECT
PBU NGL FORECASTING AND NOMINATING PROCEDURES
Initial Supply in Kind Period
I. No later than 120 days prior to the commencement of PBU NGL
deliveries, the KRU Operator shall notify the KPA WIOs ~)t' the LSEOR
Project's projected maximum PBU NGL requirements ~'or each month
during that delivery period, and shall notify each KPA WIO or' its projected
maximum Solvent Supply Obligation for each month during that delivery
period.
2. No later than I10 days prior to the commencement of PBU NGL
deliveries, each KPA WIO shall notify the Operator of its election to supply
PBU NGLs through the Supply In Kind Option.
3. Following receipt of the supply in kind election notices, the KRU
Operator shall submit bid requests for Solvent Contracts to the owners of
PBU NGLs. The Operator shall award the Solvent Contracts in accordance
with competitive bidding procedures no later than 70 days prior to the
commencement of PBU NGL deliveries.
Biennially
4. No later than 180 days prior to the first day of each two-year
deliverv period, the KRU Operator shall notify the KPA WIOs of the LSEOR
Project's projected maximum PBU NGL requirements for each month
during that delivery period, and shall notify each KPA WIO of its projected
maximum Solvent Supply Obligation for each month during that delivery
period.
EX.BIT D
Pa~e 2
5. No later than 120 davs prior to the first dav of each two-year
delivery period, each KPA WIO shall notify the Operator of its election to
supply PBU NGLs through the Supply In Kind Option.
6. Following receipt of the supply in kind election notices, the KRU
Operator shall submit bid requests for Solvent Contracts to the owners of
PBU NGLs. The Operator shall award the two-vear Solvent Contracts in
accordance with competitive bidding procedures no later than 70 days
prior to the first day of the delivery period.
Annually
7. No later than 90 days prior to the first day of each year during
which PBU NGLs are required, the KRU Operator shall submit the LSEOR
Project's annual NGL forecast to the Oliktok Pipeline Company ("OPC"). OPC
will utilize this NGL forecast to establish its tariff rate for the following
year.
Monthly
8. Bv the !0th dav of each month, the KPA WIOs who have elected
the Supply in Kind Option shall notify the KRU Operator of their PBU NGL
supplier(s) for the month which begins approximately 70 days after this
notification deadline.
9. By the last day of each month, the KRU Operator will issue an NGL
import forecast for the following three months to the PBU Oil Movements
Coordinator and will make the following notifications for the month which
begins approximately 60 davs from this notification deadline' (a) the PBU
Oil Movements Coordinator will be notified bv facsimile of the LSEOR
Project's dailv PBU NGL import rate nomination and percentage of this rate
to be supplied bv each PBU WIO' (b) each KPA WIO will be notified of its
Solvent Supply Obligation: and (c) each PBU NGL supplier will be notified of
EXHIBIT D
Page 3
its PBU NGL delivery rate nomination. The KRU Operator shall not adjust
the NGL import rate nomination after the notification deadline unless
required by events unforeseen at the time of the original nomination or
beyond the control of the KRU Operator.
10. The KPA WI'Os who have elected the Supply In Kind Option shall
be responsible for the t)rocurement and associated accounting of their PBU
NGLs to be delivered that month.
Il. The KRU Operator shall be responsible for the procurement and
associated accounting of PBU NGLs acquired under the Solvent Contracts
for that month.
12. As the LSEOR Project solvent acquisition coordinator, the KRU
Operator shall control the PBU NGL import rate. In accordance with the
LSEOR Operating Procedures. sufficient PBU NGLs shall be acquired to
maximize use of (a) solvent injection pump facilities, (b) excess available
lean gas, or (c) immature EOR target patterns, subject to the PBU NGL rate
limit described in Paragraph B.2.4. The Kuparuk LSEOR Project will take
the PBU NGL volumes nominated, provided that (a) all PBU NGL Owners
can supply their nominated volumes and (b) unforeseen circumstances or
matters beyond the control of the KRU Operator do not prevent the LSEOR
Project from physically taking the nominated volumes.
EXHIBIT C
KUPA~t~x vuvt~ uNIT
LARGE SCALE ENHANCED OIL RECOVERY PROJECT
NOTICE OF ELECTION OF SUPPLY IN KIND OPTION
TO: ARCO ALASKA, D4C.
i, In accordance with Paragraph B.4.4 of the LSEOR Operating Procedures, the
undersigned KPA WIO hereby elects to supply t0 ¢, % of ;.ts LSEOR Solvent Supply Obligation
in kind. Any additional PBU NGLs required to meet the undersigned's Solvent Supply Obligation
will be supplied by the KRU Operator under the Solvent Contracts pursuant to this agreement.
2. The election in (1) above is an irrevocable commitment to supply PBU NGLs in kind
for a period beginning upon LSEOR Project start-up (i.e., the commencement of PBU NGL
deliveries) and ending December 31, 1997 ("Delivery Period").
3. Each month during the Delivery Period, the undersigned shall provide the elected
percentage in (1) above of its Solvent Supply Obligatmn., The undersigned shall deliver PBU
NGLs at such rates as the Operator shall request in accordance with procedures set forth in Exhibit
D of'the LSEOR Operating Procedures.
4. The delivery point for PBU NGLs supplied by the undersigned shall be the Oliktok
Pipeline Coml~any's ("OPC's") connection at the point of receipt within the Kupamk River Unit
("KRU point of receipt").
5. The condition of the PBU NGLs supplied by the undersigned shall reasonably match
OPC's pipeline pressure and temperature as they exist therein from time to time.
6. The delivery quality of the PBU NGLs supplied by the undersigned shall be "as
produced" from the PBU Central Gas Facility..
EXHIBIT C
Pa~e 2
7. The undersigned warrants title to the PB U NGLs delivered bv it hereunder. Title to the
PBU NGLs shall be deemed to pass to the KRU Operator on behalf of the KPA WlOs from the
undersigned at the KRU point of receipt.
8. The undersigned shall be responsible for the costs of all PBU NGLs supplied by it
hereunder, including, but not limited to. the purchase price, royalties, and taxes. Transportation
shall be handled as follows:
Option A
CHECK OPTION (A) OR (B)
Operator. as agent for the undersigned, shall arrange for transportation of the PB U NGLs through
OPC's pipeline to the KRU point of receipt. The charges for such transportation shall be charged
to the Joint Account and funded by the undersigned. The undersigned shall indemmfy, defend,
and hold the Operator harmless from and against any and all claims and liabilities arising out of'
said transportation services.
Option B
The undersigned shall arrange for transportation of the PBU NGLs through OPC's pipeline to the
KRU point of receipt and shall be responsible for all such transportation charges.
The undersign.ed may change the above election at any time during the Delivery, Period upon 60
days prior written notice to the Operator.
9. In the event the undersigned, by reason of an event of force majeure, is rendered unable
wholly or in part, to perform its obligation hereunder, then upon the undersigned's giving notice
and particulars of such event, its obligation to perform shall be suspended or correspondingly
reduced during the continuance of any inability so caused, but in no greater amount than required
by the event of force majeure and for no longer period. The effect of such event shall, so far as
possible, be remedied with ail reasonable and prompt dispatch. Force majeure means any event
beyond the control of the undersigned and which by the exercise of due diligence the undersigned
is unable to prevent or overcome, including, but not limited to, an act of God. fire, flood, volcano.
EXHZBIT C
Pa~e 3
earthquake, explosion, sabotage, and act of the public enemy, civil or military, authority, including
court orders, injunctions and orders of governmental agencies of competent jurisdiction.
insurrection or not, an act of the elements, failure of equipment, or the inability to obtain or ship
equipment or materials because of the effect of similar causes on carriers or shippers. Strikes.
lockouts, and other labor disturbances shall be considered events of force majeure, and nothing
herein shall require the undersi~maed to settle a labor dispute against its best judgment.
i0. This election and the obligations hereunder are subject to the LSEOR Operating
Procedures.
KPA WORKING INTEREST OWNER
lO ~ /qqs-
2UL 14 ~95 ~8:50AM BP GPMA DEPT 907
P. 2/4
EXHIBIT C
KUPA~,UK P, iv ~¢ iJZSli'
LARGE SCALE ENHANCED OIL RECOYERY PROJECT
NOTICE OF ELECTION OF SUPPLY IN KIND OPTION
TO: ARCO ALASKA. ~'qC.
1. In accordance with Paragraph B.4.4 of thc LSEOR Operating Procedures, the
undersigned'liPA WIO hereby elects to supply/OeO__%~,/its LSEOR Solvent Supply Obligation
in kind. Any additional PBU NGLs required to meet the undersigned's Solvent Supply Obligation
will be supplied by the KRU Operator under the Solvent Contra;ts pursuant to this agreement.
2. The election in (1) above is an inzvocabl¢ commitment to supply PBU NGLs in kind
for a period beginning upon LSEOR Project start-up (i.e., the commencement of PBU NGL
deliveries) arid ending D~cember 31, 1997 ("Delivery Psriod").
3. Each month during the Delivery Period, the undersigned shall provide the clscted
percentage in (1) above of its Solvent Supply Obligation: ..The undersigned shall deliver PBU
NGLs at such rates as the Operator shall request in accordance with procedures set forth in Exlxibit
D of the LSt~OR Operating Procedures.
~,, The delivery point for PBU NGLs supplied by the undersigned shall be the Oliktok
Pipeline Company's ("OPC's") connection at the point of receipt within the Kuparuk River Unit
("KRU point bf receipt").
5. The condition of the PBU NGLf supplied by the undersigned shall reasonably match
OPC's pipeline prmssur~ and temperature as they exist therein from time to time.
6. The delivery quality of the PBU NGLs supphcd by the undersigned shall be "as
produced" from the PBU C, entra[ Gas Facility.
5UL 14 ~95 P~8:51AM BP GPMA DEPT 987 56~680
Page 2
P. 9/,4
7. The undersigned warfares t/tie £o the PBU NGLs delivered by it hereunder. Tide to the
PBU NGLs shall be deemed to pass to the KRU Operator on beh~f of o,,~..... I"~ .-, -. ,,.,o .,,m the
undersigned at the KRU poim of ree=ipt.
8. The undersigned shall be responsible for the costs of all PBU NGLs supplied by it
hereunder, including, but not limited to, ~e purchase price, royalties, and taxes. Transportation
shall be handled as follows:
CHECK OPTION (A) OR (B)
Operator, as agent for the undersigned, shall arrange, for transportation of the PBU NGLs through
OPC's pipeline to the KRU point of receipt. The charges for such transportation shall be charged
to the Joint Account and funded by the undersigned. The undersigned shall indemnify, defend,
and hold the Operator harmless from and against any and all claims and liabilities arising out of
said transportation services.
_ Option B
The undersigned shall arrange for transportation of the PBU NGLs through OPC's pipeline to the
KRU point of receipt and shall be responsible for all such transportation charges.
The.undersigned may change the above election at any time during the Delivery Period upon 60
days prior ~;ri~n notice to the Operator.
9. La the event the undersigned, by reason of an event of force majeure, is rendered unable
wholly or in part, to perform its obligation hereunder, then upon the undersigned's giving notice
and particulars of such event, its obligation to perform shall be suspended or correspondingly
reduced during the continuance of any inability so caused, but in no greater amount than required
by the event of force majeure and for no longer period. The effect of such event shall, so far as
possible, be remedied with all reasonable and prompt dispatch. Force majeure means any event
beyond the control of the undersigned and which by the exercise of duc diligence the undersigned
is unable to prevent or overcome, including, but not limited to, an act of God, fire, flood, volcano,
_TUL 14 '9S ~]8:$1AM BP ~PM;q DEPT 90? ~644680
EXHIB1T C
earthquake, explosion, sabotage, and act of the publk enemy, civil or military authority, including
court orders, inju_ncdons and orders of governmental agencies of competent jurisdiction,
insurrection or riot, an act of the elements, failure of equipment, or the inability to obtain or ship
equipment or materials because of the effect of similar causes on earners or shippers. Strikes,
lockouts, and other labor flisturbanees shall be considered events of force ma]em, and nothing
herein shall requite the undersigned to settle a labor dispute against its best judgment.
10. This election and the obligations hereunder are subject to the LSEOR Operating
Proceclures.
KPA WORKING INTEREST OWNER
;~JL 07 '95
P. 2×4
EXHIBIT C
LARGE SCALE ENHANCED OIL RECOVERY PROJECT
NOTICE OF ELEC~ON OF SUPPLY IN ~ND OP~ON
TO: ARCO ALASKA, INC.
I. In accordance with Paragraph B.4.4 of the LSEOR Operating Procedures. the
undersigned KPA WIO hereby elects to supply I ,C,,~ % of its LSEOR Solvent Supply Obligation
in kind. Any additional PBU NGLs required m meet the undersigned's Solvent Supply Obligation
wtll be supplied by the KRU Operator under tile Solvent Contracts pumuant to this agzeement.
2. Thc election in (1) above is an irrevocable commitment to supply PBU NGLs in kind
for a period beginning upon LSEOR Project start-up (i.e., the commcnccment of PBU NGL
d61ivcrics) and ending Dec~miaer 31.1997 ("Dalivery Period").
9. Each month during the Delivery Period. thc undersigned shall provide the elected
percentage in (1) above of its Solvent Supply Obligation. The undersigned shall deliver PBU
NGLs at such rates as the Operator shall request in accordance with procedures set forth in Exhibit
D of thc LSEOR Ofx:rating Procedurr, s.
~,. The delivery point for PBU NGLs supplied by the undersigned shall be the Oliktok
Pipeline Company's ("OPC's") connecUon at the point of receipt within the Kuparuk River unit
CKRU point of receipt").
5. The condition of the PBU NGLa supplied by the undersigned shall reasonably match
OPC's pipeiim: pressure and temperature as they exist therein from time to time.
6. The delivery quality of the PBU NGLs supplied by the undersigned shall be "as
produced" from the PBU Central Gas Facility.
3LIL l~? '95 Fi;~:!I~PM
F ITC
Pag 2
?. The undersigned warrants title tO t.l'l¢ PBU NGL$ delivered by it hereunder. Title to the
PBU NGLa sh~l be deemed to pass to the KRU Operator on behalf of the I~A '&lOs from
undersigned at the KRU point of receipt.
8. The undersigned shall be responsible for thc costs of all PBU NGLs supplied by it
hereunder, including, but not limited to, th¢ purchase price, royalties, and taxes. Transportation
shall be handled as follows:
Option A
_
CHECK OPTION (A) OR (B)
Operator. m agent for the undersigned, shall arrange for transponalion of the PBU NGI.,s ~rough
OPC's pipeline to the KRU point of receipt. Thc charges for such transportation shall be charged
to the Joint Account and funded by the undersigned. The undersigned shall indemnify, defend,
and hold the Operator harmless from and against any and all claims and liabilities arising out of
said transportation serviccs.
Option B
The undemgncd shall arrange for transportation of the PBU NGLs through OPC's pipeline to the
KRU point of receipt and shall be responsible for all such transportation charges.
Tim undersigned may change the above election at any time during the Delivery Period upon 60
days prior written notice to the Operator.
9. In the event the undersigned, by reason of an event of force majeure, is r~nder=d unable
wholly or in par~, to perform its obligation hereunder, then upon the undersigned's giving notice
and particulars of such event, its obligation to perform shall be suspended or correspondingly
reduced during the continuance of any inability so caused, but in no grealer amount than required
by the event of force majeure and for no longer period. The effect of such event shall, so far as
possible, be r=rn~died with all reasonable and prompt dispatch. Force majeure weans any event
beyond the control of the undersigned and which by the exercise of due diligence the undersigned
is unable to pre'~nt or overcome, including, but not limited to, an act of God, fire, flood, volcano,
EXHIBIT
Page 3
earthquake, explosion, sabotage, and act of the public enemy, civil or military authority., including
court orders, injunctions and orders of governmental agencies of competent jurisdiction.
insurrection or riot. an act of the elements, failure of equipment, or the inability to obtain or ship
equipment or materials because of the effect of similar causes on carriers or shippers. Strikes,
lockouts, and other labor disturbances shall be considered events of force majeure, and nothing
her~m shall require the undex~igneti to settle a labor dispute against its Imst judgment.
10. This election and thc obligations hereunder are subject to the LSEOR Operating
Procedures.
EXHIBIT C
KUPARUK RIVER UNIT
LARGE SCALE ENHANCED OIL RECOVERY PROJECT
NOTICE OF ELECTION OF SUPPLY IN KIND OPTION
TO: ARCO ALASKA, INC.
1. In accordance with Paragraph B.4.4 of the LSEOR Operating Procedures, the
undersigned KPA WIO hereby elects to supply _J.~_% of its LSEOR Solvent Supply Obligation
in kind. Any additional PBU NGLs required to meet the undersigned's Solvent Supply Obligation
will be supplied by the KRU Operator under the Solvent Contracts pursuant to this agreement.
2. The election in (1) above is an irrevocable commitment to supply PBU NGLs in kind
for a period beginning upon LSEOR Project start-up (i.e., the commencement of PBU NGL
deliveries) and ending December 31, 1997 ("Delivery Period").
3. Each month during the Delivery Period, the undersigned shall provide the elected
percentage in (1) above of its Solvent Supply Obligation. The undersigned shall deliver PBU
NGLs at such rates as the Operator shall request in accordance with procedures set forth in Exhibit
D of the LSEOR Operating Procedures.
4. The delivery point for PBU NGLs supplied by the undersigned shall be the Oliktok
Pipeline Company's ("OPC's") connection at the point of receipt within the Kuparuk River Unit
("KRU point of receipt").
5. The condition of the PBU NGLs supplied by the undersigned shall reasonably match
OPC's pipeline pressure and temperature as they exist therein from time to time.
6. The delivery quality of the PBU NGLs supplied by the undersigned shall be "as
produced" from the PBU Central Gas Facility.
EXHIBIT C
Page 2
7. The undersigned warrants title to the PBU NGLs delivered by it hereunder. Tire to the
PBU NGLs shall be deemed to pass to the KRU Operator on behaff of the KPA WIOs from the
undersigned at the KRU point of receipt.
8. The undersigned shall be responsible for the costs of all PBU NGLs supplied by it
hereunder, including, but not limited to, the purchase price, royalties, and taxes. Transportation
shall be handled as follows:
CHECK OPTION (A) OR (B)
Option A
Operator, as agent for the undersigned, shall arrange for transportation of the PBU NGLs through
OPC's pipeline to the KRU point of receipt. The charges for such transportation shall be charged
to the Joint Account and funded by the undersigned. The undersigned shall indemmfy, defend,
and hold the Operator harmless from and against any and all claims and liabilities arising out of
said transportation services.
Option B
The undersigned shall arrange for transportation of the PBU NGLs through OPC's pipeline to the
KRU point of receipt and shall be responsible for all such transportation charges.
The undersigned may change the above election at any time during the Delivery Period upon 60
days prior written notice to the Operator.
9. In the event the undersigned, by reason of an event of force majeure, is rendered unable
wholly or in part, to perform its obligation hereunder, then upon the undersigned's giving notice
and particulars of such event, its obligation to perform shall be suspended or correspondingly
reduced during the continuance of any inability so caused, but in no greater amount than required
by the event of force majeure and for no longer period. The effect of such event shall, so far as
possible, be remedied with all reasonable and prompt dispatch. Force majeure means any event
beyond the control of the undersigned, and which by the exercise of due diligence the undersigned
is unable to prevent or overcome, including, but not limited to, an act of God, fa'e, flood, volcano,
EXHIBIT C
Page 3
earthquake, explosion, sabotage, and act of the public enemy, civil or mihtary authority, including
court orders, injunctions and orders of governmental agencies of competent jurisdiction,
insurrection or riot, aa act of the elements, failure of equipment, or the inability to obtain or ship
equipment or materials because of the effect of similar causes on carriers or shippers. Strikes,
lockouts, and other labor disturbances shall be considered events of force majeure, and nothing
herein shall require the undersigned to settle a labor dispute against its best judgment.
I0. This election and the obligations hereunder are subject to the LSEOR Operating
Procedures.
KPA WORKING INTEREST OWNER
Company:
By: Date:
Title:
EXHIBIT C
""""~' ~'""" RIVER
~r~u~ UNIT
LARGE SCALE ENHANCED OIL RECOVERY PROJECT
NOTICE OF ELECTION OF SUPPLY IN KIND OPTION
TO: ARCO ALASKA, INC.
1. In accordance with Paragraph B.4.4 of the LSEOR Operating Procedures, the
undersigned KPA WIO hereby elects to supply ~OO% of its LSEOR Solvent Supply Obligation
in kind. Any additional PBU NGLs required to meet the undersigned's Solvent Supply Obligation
will be supplied by the KRU Operator under the Solvent Contracts pursuant to this agreement.
2. The election in (1) above is an irrevocable commitment to supply PBU NGLs in kind
for a period beginning upon LSEOR Project start-up (i.e., the commencement of PBU NGL
deliveries) and ending December 31, 1997 ("Delivery Period").
3. Each month during the Delivery Period, the undersigned shall provide the elected
percentage in (1) above of its Solvent Supply Obligation. The undersigned shall deliver PBU
NGLs at such rates as the Operator shall request in accordance with procedures set forth in Exhibit
D of the LSEOR Operating ~ures.
4. The delivery point for PBU NGLs supplied by the undersigned shall be the Oliktok
Pipeline Company's ("OPC's") connection at the point of receipt within the Kuparuk River Unit
CKRU point of receipt").
5. The condition of the PBU NGLs supplied by the undersigned shall reasonably match
OPC's pipeline pressure and temperature as they exist therein from time to time.
6. The delivery quality of the PBU NGLs supplied by the undersigned shall be "as
produced" from the PBU Central Gas Facility.
EXHIBrr C
Page 2
7. The undersigned warrants title to the PBU NGLs delivered by it hereunder. Title to the
PBU NGLs shall be deemed to pass to the Ic~.U Ope,'~m,' ,,,, ~half of uhe KPA WIOs from the
undersigned at the KRU point of receipt.
8. The undersigned shall be responsible for the costs of all PBU NGLs supplied by it
hereunder, including, but not limited to, the purchase price, royalties, and taxes. Transportation
shall be handled as follows:
X Option A
CHECK OPTION (A) OR (B)
Operator, as agent for the undersigned, shall arrange for transportation of the PBU NGLs through
OPC's pipeline to the KRU point of receipt. The charges for such transportation shall be charged
to the Joint Account and funded by the undersigned. The undersigned shall indemnify, defend,
and hold the Operator harmless from and against any and ali claims and Liabilities arising out of
said transportatiotl, services.
Option B
The undersigned shall arrange for tran.qportation of the PBU NGLs through OPC's pipeline to the
KRU point of receipt and shall be responsible for ali such transportation charges:
The undersigned may change the above election at any time during the Delivery Period upon 60
days prior written notice to the Operator.
9. In the event the undersigned, by reason of an event of force majeure, is rendered unable
wholly or in part, to perform its obLigation hereunder, then upon the undersigned's giving notice
and particulars of such event, its obligation to perform shall be suspended or correspondingly
reduced during the continuance of any inability so caused, but in no greater amount than required
by the event of force majeure and for no longer period. The effect of such event shall, so far as
possible, be remedied with all reasonable and prompt dispatch. Force majeure means any event
beyond the control of the undersigned and which by the exercise of due diligence the undersigned
is unable to prevent or overcome, including, but not limited to, an act of God, fire, flood, volcano,
· EXHIBIT C
Page 3
earthquake, explosion, sabotage, and act of the public enemy, civil or military authority, including
court orders, injunctions and orders of governmental agencies of competent jurisdiction,
insurrection or riot, an act of the elements, failure of equipment, or the inability to obtain or ship
equipment or materials because of the effect of similar causes on carriers or shippers. Strikes,
lockouts, and other labor disturbances shall be considered events of force majeure, and nothing
herein shall require the undersigned to settle a labor dispute against its best judgment.
10. This election and the obligations hereunder are subject to the LSEOR Operating
' 'Procedures.
KPA WORKING iNTEREST OWNER
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RE:
ALASKA OIL AND GAS CONSERVATION COMMISSION
PUBLIC HEARING
JULY 20, 1995, 9:00 O'CLOCK A.M.
TRANSCRIPT OF PROCEEDINGS
THE APPLICATION OF ARCO ALASKA, INC. FOR APPROVAL
TO INITIATE A LARGE SCALE ENHANCED OIL RECOVERY
PROJECT IN THE KUPARUK RIVER UNIT
HELD AT THE
ALASKA OIL AND GAS CONSERVATION COMMISSION
3001 PORCUPINE DRIVE
ANCHORAGE, ALASKA
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P R O C E E D I N G S
CHAIRMAN JOHNSTON: I'd like to call this
hearing into session, please. I'd note the time is
approximately seven after nine o'clock. The date is July 20,
1995. We are located in the offices of the Alaska Oil and Gas
Conservation Commission, 3001 Porcupine Drive, at Anchorage,
Alaska. The head table consists of Tuckerman -- Commissioner
Tuckerman Babcock, Commissioner Russ Douglass, and myself,
Commissioner Dave Johnston. A transcript will be made of the
proceedings. It is currently being recorded by Joe Kolasinski,
of R & R Court Reporters, and if you wish to obtain a
transcript of these proceedings, we ask that you contact R & R
Court Reporters directly. I understand that we are hooked up
to a teleconference. Are we coming through for those
people .....
COMMISSIONER DOUGLASS: We won't be able to
hear them.
CHAIRMAN JOHNSTON: Oh, they can't respond?
COMMISSIONER DOUGLASS: She already checked --
well, yeah, but we can't hear it from over here, 'cause there's
no speaker.
CHAIRMAN JOHNSTON:
can hear us or not then?
COMMISSIONER DOUGLASS:
says she checked and they can't.
So we have no idea if they
According to Diane, she
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CHAIRMAN JOHNSTON: Okay. Well, we'll make the
assumption that they can hear us, and if they can't, I guess
they lose out.
The purpose of this hearing is to consider a request by
the operator of the Kuparuk Oil Field to pursue a EOR project
in Kuparuk that would involve the sale of NGLs as a miscible
injectant to the Kuparuk Oil Field.
The public notices that were provided for this hearing
were dated -- what were they -- they were dated June 17, 1995,
which provided an opportunity for a public hearing. The second
public hearing notice was dated July 12, 1995 that established
the hearing date of July 20th.
At this time I'd like to move that these two notices be
entered into the record in these proceedings. I would suggest
that the June 17th notice be entered as AOGCC Exhibit Number 1,
and the July 12th notice as AOGCC Exhibit Number 2. Are there
any objections?
IN UNISON: No objections.
CHAIRMAN JOHNSTON: Okay. No objections.
Those two exhibits are entered into the record as noted as
AOGCC Exhibit 1 and AOGCC Exhibit 2.
MR. RODGERS: We have numbered exhibits that
start with 1, 2, 3, and 4.
CHAIRMAN JOHNSTON: We will consider yours ARCO
Exhibits, Number 1 through whatever.
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MR. RODGERS: Okay.
CHAIRMAN JOHNSTON: So distinguishing there
would be AOGCC as opposed to ARCO exhibits.
These proceedings will be held in accordance with 25 --
or excuse me, 20.AAC.25.540. Basically, I think, everybody is
familiar with those regulations, but we will be taking either
sworn testimony or unsworn statements. As you come up before
the Commission we ask that you state your name and who you
represent. If you wish to provide sworn testimony, we will
swear you in. If you wish to be considered an expert witness
in this matter, we'd ask that you state your qualifications; we
will then rule. Members of the audience will not be permitted
to ask questions directly of the individual testifying, but if
you do have a question, we ask that you write it down, send it
forward to the end table here, and if we feel it germane, we
will then ask that question of the person testifying.
As I indicated earlier, a written transcript will be
made and will be considered a part of this public record in
these proceedings.
At this time then I would like to invite the applicant
to step forward and identify themselves and the individuals
that will be testifying on your behalf.
MR. RODGERS: Thank you. My name is
Dan Rodgers. I'm a senior attorney for ARCO Alaska. Also here
from ARCO this morning are Frank Brown, Senior Vice President
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for Kuparuk and Cook Inlet Business Unit; Scott Kerr, the
Kuparuk Development Manager; Shaun Hoolahan, the LSEOR Project
Supervisor; and Greg McDuffie, LSEOR Engineer.
ARCO is operator of the Kuparuk River Unit. We will be
presenting one witness, Shaun Hoolahan, in support of the
application for injection for the Kuparuk LSEOR project. After
Mr. Hoolahan has gone over his resume, we request that he be
recognized as an expert witness on this subject. And right now
I'll turn the floor over to Mr. Hoolahan.
CHAIRMAN JOHNSTON: So before we start with
Mr. Hoolahan, it's my understanding that he will be the only
witness for ARCO, but you have these other people available to
answer questions in the event that is appropriate?
MR. RODGERS: Primarily Mr. Hoolahan will be
available as our only witness and to answer the questions.
CHAIRMAN JOHNSTON: Okay. So there will be no
need to swear in Scott Kerr or Greg McDuffie or any of the
other individuals?
MR. RODGERS: Correct.
CHAIRMAN JOHNSTON: Okay.
COMMISSIONER DOUGLASS:
your right hand?
(Oath administered)
MR. HOOLAHAN:
do.
COMMISSIONER DOUGLASS:
Would you please raise
Thank you. Would you
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please state your name and spell your last name for the record?
MR. HOOLAHAN: My name is Shaun Hoolahan, and
the last name is spelled H-o-o-l-a-h-a-n.
COMMISSIONER DOUGLASS: Thank you.
CHAIRMAN JOHNSTON: And, Mr. Hoolahan, do you
wish to be considered an expert witness in this matter?
MR. HOOLAHAN: Yes, I do.
CHAIRMAN JOHNSTON: Please state your
qualifications.
MR. HOOLAHAN: My qualifications are submitted
as ARCO Exhibit 1. I've received a bachelor's degree in
petroleum engineering from the Montana College of Mineral
Science and Technology in 1982, and joined ARCO here in Alaska
that same year. I received a master's of science degree in
engineering management from the University of Alaska in 1987.
In 1990 I became a professional petroleum engineer, registered
with the state of Alaska.
During my 13 years with ARCO the vast majority of my
experience has been in the area of reservoir engineering,
having worked in both the Prudhoe Bay and Kuparuk reservoir
engineering organizations. While in Prudhoe my work was
primarily focused on gas cycling process in support of the
Prudhoe Bay gas handling expansion projects. My most recent
experience has been in the Kuparuk organization where I have
been responsible for the technical evaluation, economic
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justification and project execution of EOR related projects
since the end of 1992. I was directly involved in the recent
expansion of the Kuparuk EOR pilot program, and am pleased to
be here today to discuss the next phase of EOR development in
Kuparuk.
COMMISSIONER BABCOCK: I move we recognize
Mr. Hoolahan as an expert witness.
COMMISSIONER DOUGLASS: No objections.
CHAIRMAN JOHNSTON: There being no objection,
the Commission will recognize Mr. Hoolahan as an expert witness
in these proceedings.
Before we proceed with your testimony, you indicated
that your resume was Exhibit Number 17
MR. HOOLAHAN: Yes. We have a set of exhibits.
CHAIRMAN JOHNSTON: Okay. How does that
correspond with your application for injection that has Exhibit
Number 1 through 8?
MR. RODGERS: They're a different numbering
system.
CHAIRMAN JOHNSTON: Okay. So .....
MR. RODGERS: We'd request that the application
be ARCO Exhibit Number 5 in this hearing.
CHAIRMAN JOHNSTON: Okay. Including the
attached exhibits to that .....
MR. RODGERS: Right.
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CHAIRMAN JOHNSTON: ..... we'll include that as
-- those exhibits will be subsets of ARCO Exhibit Number 5,
which is the application for a large scale EOR project.
MR. HOOLAHAN: At the end of my testimony I do
have a copy which has the color slides in it. The copies
before you are in black and white.
CHAIRMAN JOHNSTON:
Please proceed.
Thank you, Mr. Hoolahan.
MR. HOOLAHAN: During my testimony today I will
be providing information that demonstrates the hydrocarbon
enriched gas EOR process at KuParuk works. We have
verification both in the laboratory and in the field.in the
form of two successful pilot programs.
The first of these pilot programs is the original small
scale EOR or SSEOR project that was implemented in 1988. The
second is a project we call SSEORX, with the X signifying that
this project is an expansion of the original small scale pilot.
I will also be giving a brief overview showing how a
major expansion of EOR Kuparuk fits into the logical
progression of Kuparuk's field development.
As currently proposed, the large scale EOR project will
increase current miscible gas injection capacity by more than a
factor of three. Our ability to take full advantage of the
existing facility infrastructure is a key contributing factor
in the project's viability, but in order to significantly
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expand EOR Kuparuk, we will need more solvent than can be
generated from enriching fluid sources indigenous to Kuparuk.
This is why we are looking at enriching fluid import in the
form of Prudhoe Bay NGLs.
While other solvent sources may or may not become
available at some point in the future, Prudhoe Bay NGLs are the
only substantial source available at this time. Fortunately,
the strong condensing character of the miscibility mechanism at
Kuparuk is well suited to an NGL based solvent.
As part of my testimony today, I'll briefly be touching
on some of the laboratory data that has been generated over the
course of the last 10 years. Results confirm our ability to
create a miscible injectant or MI from a wide range of
enriching fluid compositions. This range far exceeds any of
the variations we might expect to see within this project.
Another point I'll be touching on is the relationship
between infield drilling and EOR recovery. The bottom line
here is that infield drilling provides for increased contacting
of oil within the reservoir. It is by improving reservoir
sweep-out or tapping into areas of reservoir isolation between
injection wells and their corresponding production wells. When
you couple this with MI injection, you end up exposing more of
the reservoir to the EOR recovery process, thereby increasing
ultimate recovery.
Pulling these factors together, you end up with a
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project that is expected to recover over 200 million barrels of
incremental oil. That's a significant amount of oil. That's
like finding two-thirds of the Pt. McIntyre hiding within the
Kuparuk field. But this is a significant project. When
completed, Kuparuk's large scale EOR project will be among the
largest of its type in the world. But before putting 200
million barrels in the bank .....
COMMISSIONER BABCOCK: Excuse me, Mr. Hoolihan.
Mr. Chairman, would you rather me save questions till the end
of his testimony?
CHAIRMAN JOHNSTON: Well, we've -- you know,
we've conducted hearings both ways, but ~I think in this
particular case you're going to be the person that will be
speaking throughout the morning.
MR. HOOLAHAN: Yes.
CHAIRMAN JOHNSTON: And how long do you
anticipate that your testimony -- your direct testimony will
take?
MR. HOOLAHAN: My direct testimony should take
on the order of an hour.
COMMISSIONER BABCOCK: An hour; I'd be happy to
wait then. But either way.
CHAIRMAN JOHNSTON: Well, I think it might be
more helpful right now just to go ahead and ask questions as
they come up, you know, rather than wait, because oftentimes we
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will overlook the question that comes to mind at the time, and
it may be somewhat disruptive for you, but I also think there
is benefit in asking questions as we currently think of them.
So .....
COMMISSIONER BABCOCK: But the question that
Is that 200 million barrels net of the NGLs
comes to mind:
injected?
MR. HOOLAHAN:
EOR -- incremental EOR oil.
That is 200 million barrels of
We also expect to recover -- to
get that we expect to import 100 million barrels of NGLs of
which we expect to recover about a third.
CHAIRMAN JOHNSTON: And when would you recover
that, basically the third of the NGLs that you would be putting
into the reservoir?
MR. HOOLAHAN: That would be recovered
continuously over the course of the project as the miscible
injectant that's injected into the reservoir gets returned and
gets recycled.
COMMISSIONER DOUGLASS: So you would actually
not be sending this recovered NGL down any pipeline, you'd be
recycling that, or would there be a mix?
MR. HOOLAHAN: There will be a portion in the
returned miscible injectant as part of the separation process
at the surface. There will be a portion of that that will just
stabilize into the oil as part of the normal separation. And
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3
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that portion of the oil will be entrained in the crude oil
will be going -- being sold as of the Kuparuk crude
stream.
COMMISSIONER DOUGLASS: Okay. But that's only
a portion of the 30 percent, so you're not really necessarily
recovering one-third?
MR. HOOLAHAN: The 30 percent relates to the
net after the entire project is completed. Of the total volume
we import we expect to ultimately recover about a third of
that. There's a bootstrap process that's involved in this.
COMMISSIONER DOUGLASS: But as you say
recovered, that means sent down a pipeline?
MR. HOOLAHAN: Sent down a pipeline.
COMMISSIONER DOUGLASS: Fine.
CHAIRMAN JOHNSTON: For the record, I'd like to
note that Laurel Evenson, of R & R Court Reporters, has just
taken over the transcript in these proceedings. Please
proceed, Mr. Hoolahan.
MR. HOOLAHAN: Before putting the 200 million
barrels in the bank, there are a few things I need to point
out. The magnitude of this incremental recovery number is
predicated, first, on the import of approximately 100 million
barrels of Prudhoe Bay NGLs during Kuparuk's anticipated field
life. We also expect to get a portion of these NGLs back, and
I'll touch on that later.
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Second, it involves implementation of the drilling
program that we've outlined in our application.
Third, we will need to have sufficient well injection
capacity. While this third item is not expected to be a
problem, I am including it for completeness.
And, fourth, we will need to expand into all of the
drill sites that we plan to expand into as part of the large
scale project.
With that I would like to briefly touch on a couple of
objectives before moving on to the outline for the remainder of
my testimony.
The information in Exhibit 2-C is the same as what is
contained under the requested decision section of our
application. If you don't mind, I'll just read this verbatim:
As the first item states, ARCO Alaska, Inc., as KRU
operator, respectfully requests that the Commission issue an
order authorizing the underground injection of miscible
enriched natural gas for enhanced oil recovery in the expanded
area of the proposed KRU large scale EOR project.
And as stated in the second item, ARCO, Alaska, Inc.,
as KRU operator, respectfully requests that the Commission
endorse 1) the areal expansion of the enriched gas EOR process
via the proposed KRU large scale EOR project and, 2) additional
drillings within the EOR expansion area.
Over the course of the next hour or so, I'll be giving
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you a high altitude introduction to the large scale EOR project
in the form of a cartoon type schematic, followed by a little
bit of background on Kuparuk development history to help set
the overall frame of reference. I'll follow that with an
overview of the performance of our small scale and small scale
expansion projects and the success we've seen and intend to
build upon.
The brief overview of our supporting lab data that I
mentioned earlier will be covered in this section. After that
I'll jump right into the large scale project itself, followed
by a summary of the six topics the Commission specifically
requested be addressed.
With your indulgence, I would like to cover these six
topics after I've had a chance to go through the supporting
details. However, if the Commission has a strong desire to
pull this forward, we can do that.
CHAIRMAN JOHNSTON: Just a quick question for
you, Mr. Hoolahan. Is it ARCO's belief or would it be ARCO's
belief also in terms of the objectives that you would be
seeking Commission approval to sell NGLs to Kuparuk?
MR. HOOLAHAN: I'll cover that in the six
questions that we address, in terms of the transfer of NGLs.
And, finally, I will be closing with a section on
findings and conclusions.
As I promised, I'm going to start out with a fairly
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high level, with a simplified schematic. On the right-hand
side on Exhibit 2-C is a simplified representation of Prudhoe
Bay. On the left-hand side is Kuparuk. We're going to be
sticking to the left-hand side of this.
The large scale project basically involves modifying
the currently idle Oliktok pipeline to enable transport of NGLs
from Prudhoe Bay to Kuparuk and making a number of
modifications to the Kuparuk facility that I'll be touching on
a bit later.
Once the NGLs arrive at Kuparuk, they will be mixed
with enriching fluids indigenous to Kuparuk and blended with
Kuparuk lean gas to make MI. The MI will be injected into the
reservoir, mobilizing incremental oil which is produced and
sold. Although a portion of the MI will be trapped in the
reservoir, a portion of the MI will also be produced. We refer
to the produced MI as returned MI or RMI. A portion of the
liquids associated with the RMI will also end up stabilized in
the oil and be sold with the Kuparuk crude stream. The
remainder will end up as bootstrap, which essentially means we
get to use it to make more MI. The curved arrow on my slide is
intended to represent the bootstrap process. The degree of
bootstrap, when couPled with the desired level of MI enrichment
and pump capacity constraints directly influences the volume of
NGL import required. The higher the bootstrap the lower
required import, and visa-versa.
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CHAIRMAN JOHNSTON: And what -- when you say
the higher the bootstrap the less you have to import, what kind
of numbers are you attaching to this bootstrap?
MR. HOOLAHAN: Of the 100 million barrels that
we intend to import, we'll basically get to use that as 140
million. So we're able to extend that 100 to 140, roughly.
CHAIRMAN JOHNSTON: Please proceed.
MR. HOOLAHAN: Now let me give you a little
background information on Kuparuk's development history. I'm
not going to walk through every item on Exhibit 2-F, but there
are a number of items I would like to bring out.
The first item is start-up of the 16-inch pipeline
between Kuparuk and Pump Station 1 in 1981. We would increase
development and higher oil rates than originally expected. The
16-inch line was replaced with the current Kuparuk pipeline in
1984. Other than being used to transport gas for a number of
years in the late 1980s, this line has been sitting idle. We
intend to change that.
The second item worth noting is IWAG start-up in 1985.
IWAG stands for immiscible water alternating gas, and is the
process of alternating immiscible separator off-gas injection
with water injection. IWAG has historically placed an
important role in Kuparuk's gas management strategy, providing
a relatively efficient means of gas storage in the absence of a
gas cap. Through a series of expansion to new drill sites, the
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IWAG project currently provides high pressure gas injection to
17 drill sites. Expansion to an 18th drill site is currently
under way.
The IWAG project provides the piping infrastructure for
large scale which would also be conducted using a water
alternating gas process. Having this infrastructure in place
dramatically reduced the amount of up-front capital required
for the project, increasing the project's viability and
reducing its financial risk.
The last two items I would like to draw to your
attention are start-up of the original small scale EOR pilot on
Drill Sites 1-Y and 2-Z in 1988 and the subsequent expansion of
that pilot to Drill Site 1-A in 1993.
Two Commission orders authorize EOR work that has been
conducted to date; Area Injection Order Number 2 authorizes
injection -- authorizes injection for EOR and disposal purposes
on an areawide basis. The area being the Kuparuk River Unit
and the strata being the Kuparuk West Sac Reservoirs. Large
scale EOR injection activities will be conducted in accordance
to Area Injection Order Number 2.
The small scale and small scale expansion projects were
authorized by Conservation Order Number 198.3, which approved
EOR at Drill Sites 1-Y and 2-Z, with expansion to Drill Sites
l-A, l-F, i-G, l-Q, 2-C, 2-D, 2-X, and 2-W. Today we are
seeking Commission approval to expand EOR beyond the drill
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sites identified in Conservation Order 198.3.
Later on in my testimony I will be showing you a map
that depicts both the currently authorized drilling sites and
the ones for which authorization is being sought.
So where do we stand?
CHAIRMAN JOHNSTON: Let me interrupt. Often we
get the Air Force doing their fly-bys, so when that happens it
makes it very difficult for the people in the back to hear, so
if you could kind of raise your voice, if you could, please?
MR. HOOLAHAN: So were do we stand? Exhibit
2-H is a map that provides an overall status of each of the
drill sites in the field in terms of fluids being injected.
The two areas in blue depict drill sites that are under
waterflood only. The area in yellow is the current gas storage
area. The area in orange is our drill sites that are under
IWAG. The 18th drill site to be converted to IWAG, that I
mentioned a few moments ago, is Drill Site 2-T, which will join
the orange area following conversion. The red area represents
a small scale and small scale expansion drill sites.
The main distinction I would like to draw between the
small scale and small scale expansion pilots is that while the
small scale pilot immediately follow waterflood, the small
scale expansion followed IWAG. Given that all of the planned
expansions for the large scale project are to be in areas that
have previously seen IWAG, we initiated a field test to
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evaluate this process.
I'm happy to say that the field performance we've seen
to date is consistent with what we were expecting. There were
no surprises. Both pilot programs clearly demonstrate that the
EOR process at Kuparuk works.
We will review the pilot performance in just a few
minutes. But first I want to build on that success. As I
touched on earlier, expansion of EOR at Kuparuk using only
indigenous solvent is limited. Without import of an outside
enriching fluid, expansion is limited to between two and five
additional drill sites. Without site enriching fluid, that
number grows to 18.
Acquiring additional enriching fluid would seem to be a
logical next step. In taking this step you have to ask
yourself four basic questions:
The first question is: Does the project make sense
from a facilities investment standpoint? For large scale
maximizing the utilization of the existing infrastructure makes
sense both from a project viability and investment risk
standpoint.
The second question is: Can I find the solvent, that
is available today, compatible with my needs and can be
acquired in the volumes that I desire? The answer is, yes,
Prudhoe Bay NGLs. Even if an alternative solvent source is
identified at a later date, it is important to get the project
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underway now because of the third question:
Can I flood to maturity the areas I want to flood
within anticipated field life? Barring any major disruptions
in solvent supply, the large scale project should be able to do
just that.
And last, but probably most important: Do I have
sufficient confidence in the recovery estimates to go forward
with the project? Obviously, as we are before you here today,
the answer is, yes.
Now, let's review what we've seen from the pilots. To
date we have recovered 15 to 20 million barrels of incremental
oil out of Drill Site 1-Y and 2-Z that can be attributed to the
EOR process. This represents 3-1/2 to 5 percent of the
original oil in place or OIP. We expect to ultimately recover
30 to 40 million barrels of incremental EOR oil from these two
drill sites. That corresponds to seven -- between seven and 10
percent of the original oil in place.
COMMISSIONER BABCOCK: Mr. Hoolahan, are those
numbers part of your 200 million?
MR. HOOLAHAN: No. These numbers are not part
of the 200 million. The 200 million is for the 18 additional
drill sites we intend to expand to.
COMMISSIONER BABCOCK: How do you go about
identifying that portion of oil produced that you attribute to
EOR at Kuparuk?
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MR. HOOLAHAN: There's a combination of ways.
Part of it is we run reservoir simulators to establish what the
production would be without the EOR process in place, and we
also run same type models with the EOR process in place. We
have those models tuned to the field data that we've seen so
we're able to simulate the incremental recoveries -- recoveries
that we expect. And as I'll be showing you in a couple of
these slides, you can also see the response, fairly
dramatically, just looking at the field data itself.
COMMISSIONER BABCOCK: Do you identify a
returned MI as an important component of the variables that go
into the simulator?
MR. HOOLAHAN: Returned MI is one of the
variables that we use to determine the amount of NGL import, so
that variable works on the -- in establishing the volumes of
import that we need.
COMMISSIONER BABCOCK: How important a role
does it play in identifying how much oil you attribute to EOR?
MR. HOOLAHAN: In terms of the recovery,
obviously if the returned MI was very high, that may indicate
that the process isn't working, that we're basically cycling MI
through the reservoir and it's not contacting and swelling the
oil. So the level of returned MI is an indicator on how well
the flood is doing on an efficiency standpoint. It's one of
the variables that we monitor in terms of observing the --
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observing the floods, and we'll use in the process of
optimizing that in the future.
COMMISSIONER BABCOCK: Thank you.
MR. HOOLAHAN: I would now like to take the
focus in a bit closer and look at actual EOR performance data
for the small scale and small scale expansion pilot projects.
I'll start out with Drill Sites l-Y, then 2-Z, and then 1-A.
For each drill site I've identified a block of patterns that
correspond to that portion of the drill site that has been on
injection the longest. This information is presented on the
upper half of the exhibit. The performance within these blocks
is presented on the lower half of the exhibit. The area in red
is the estimated incremental EOR recover above the base decline
rate, with the yellow areas representing any adjustments
necessary to account for non-EOR impacts.
Starting with Drill Site l-Y, if you look at the lower
portion of Exhibit 2-L you can see from the red shaped area
that the EOR response is fairly obvious.
established decline tends to level out.
characteristic of an EOR type response.
You will note how the
This is fairly
Because infield
drilling was initiated on Drill Site 1-Y concurrent with the
EOR flood, an estimate of the incremental black oil or non-EOR
rate from the infield wells is depicted separately in yellow.
Moving to Drill Site 2-Z, you see the same
characteristic response as in the previous exhibit for Drill
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Site 1-Y. In this case the effect of fracture stimulation work
are depicted separately in yellow.
As you can see from Exhibit 2-N, the same
characteristic response is again observed for Drill Site 1-A.
This is very encouraging, particularly since the flood was
extended into this region specifically to test the miscible
after immiscible process. What we are seeing is entirely
consistent with the mechanistic, fully compositional
simulations we have conducted to address this issue.
In summary, we have direct field evidence that the Eon
process 'at Kuparuk works.
COMMISSIONER DOUGLASS: Going back to 2-N, when
did you start the immiscible on that; do you know?
MR. HOOLAHAN: Yeah, I was thinking when we
started the immiscible. I don't have that number right off the
top of my head. I believe it was 1-A is one of the more mature
immiscible drill sites. So I believe it was one of the early
ones.
COMMISSIONER DOUGLASS: Mid- to late '80s?
MR. HOOLAHAN: It would have been in the mid-
to late '80s.
In addition to having direct field evidence an
extensive site specific reservoir stimulation study at Drill
Site -- of the Drill Size 2-Z area, as well as numerous
mechanistic studies have been conducted. Results from these
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studies, such as the excerpt presented here in Exhibit 2-0,
have served to bolster our confidence in the benefits of the
large scale project. The confidence of the Kuparuk owners is
exemplified by the fact that the project has been funded and is
proceeding forward.
As I mentioned earlier in my testimony, I intended to
keep my discussion on laboratory data fairly brief. I would,
however, like to enter Exhibits 3-A through 3-G covering
specific aspects of the lab program into the record. You'll
find those to the back of the notebook.
To support Kuparuk's EOR evaluations, a tremendous
amount of data has been gathered and analyzed. In excess of 75
experiments have been conducted over a 10-year period, ranging
from static PBT cell measurements to sophisticated flow
experiments. This data has provided significant insight into
the miscible process at Kuparuk and has given additional
confidence in our predicted EOR performance. This data also
forms the basis for our minimum miscibility pressure or MMP
correlation which is instrumental in establishing the
appropriate level of enrichment for a given enriching fluid
composition.
Up to this point I have covered how the large scale
project fits into the logical progression of Kuparuk's field
development and how field simulation and laboratory evidence
supports the conclusion that the enriched gas EOR process at
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Kuparuk works. I would now like to provide some definition to
the project.
As I have already covered, a major expansion of EOR at
Kuparuk will require import of an outside solvent. I posed a
couple of questions earlier: Can I find a solvent that is
available today, is compatible with my needs and can be
acquired in the volume that is desired? Can I flood to
maturity the areas I want to flood within anticipated field
life?
These questions provide the basis for sizing the
project and setting two of the solvent criteria listed in this
exhibit.
Another solvent selection criterion is minimal CO2
content. This is because the Kuparuk fluid system has very
little indigenous CO2. Introducing CO2 into the system could
potentially trigger significant corrosion mitigation costs.
Should a C02 solvent -- based solvent become available at some
point, this risk may warrant careful evaluation.
As you can see from the map in Exhibit 2-S, the areas
that were previously orange, which signified all the IWAG drill
sites, are now shaded red to indicate they will become EOR
drill sites. Drill Site 2-T which, if you will recall, is in
the process of being converted to IWAG, is also shaded red.
That brings the total number of EOR drill sites at
Kuparuk to 21, including the three pilot drill sites.
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The drill sites with black lettering are those that
were approved for MI injection under Conservation Order 198.3.
CHAIRMAN JOHNSTON: Do you consider this then
to be the full extent of the proposed EOR project?
MR. HOOLAHAN: For the current project.
CHAIRMAN JOHNSTON: For the current project.
MR. HOOLAHAN: The exist- -- the extent .....
CHAIRMAN JOHNSTON: So it could evolve over
time then, depending on the results that you obtain from this
activity?
MR. HOOLAHAN: Yeah, it's possible.
CHAIRMAN JOHNSTON: Okay.
MR. HOOLAHAN: The expected incremental
recovery of over 200 million barrels from the large scale
project is based on reservoir simulation tuned to small scale
field performance. To calculate recoveries on a project basis
We first need to know how many wells we can have on EMI
injection for a given MI supply volume. This requires an
estimate of individual well injectivities, which we can develop
from historical IWAG data and expected WAG ratios.
To determine how many drill sites we can have on MI
injection, we next need to know how many injection wells,
including infield drilling, are expected to be on each drill
site. The drill sites can then be logically grouped, taking
into consideration surface piping constraints and the desire to
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keep the flood area as contiguous as possible. Once we have a
handle on well injectivities and drill site sequencing, a
scale-up tool, using dimensional recovery curves, can be
applied to generate expected rate profiles.
This next exhibit represents the level of recovery we
can expect as a function of MI slug size. Diminishing returns
are clearly evident above 30 percent hydrocarbon pore volume
injected. Due to the differing physical characteristics
between the A-sand and the C-sand, we do not expect to be able
to flood both sands to the same level of throughput. In
general, a 30 percent slug size for the dominant or more
permeable horizon is being targeted.
CHAIRMAN JOHNSTON: Does this type curve
represent a unit consensus or is it just an ARCO curve?
MR. HOOLAHAN: That curve was developed in
conjunction with work done by both ARCO and BP.
CHAIRMAN JOHNSTON: So it does represent a unit
consensus?
MR. HOOLAHAN: It's -- yeah, it is the curve
that was used to develop the project economics, so I guess it
would be a unit consensus. There are some of the owners, Exxon
and minor owners, that haven't been directly involved in the
technical evaluations.
CHAIRMAN JOHNSTON: Have each one of he working
interest owners of the Kuparuk Field approved this project?
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MR. HOOLAHAN:
(ph) the AFC -- the funding.
supply the solvent in-kind.
Not all of them have assigned
Ail of the owners have elected to
COMMISSIONER BABCOCK: When you say elected to
supply the solvent cut, do you mean the Kuparuk owners for that
-- for the 14,000 barrels a day of enriching fluid that you
expect from Kuparuk, or are you referring to the Prudhoe Bay
owners?
MR. HOOLAHAN: I'm referring to the Kuparuk
owners that have an obligation -- a solvent supply obligation
or an enriching fluid supply obligation, and each owner has
elected to supply their obligation in-kind. Each owner of the
Kuparuk Unit has elected to supply their obligation in-kind.
COMMISSIONER BABCOCK: Okay. We'll probably
get into more detail with that when we get to the six .....
CHAIRMAN JOHNSTON: That may be. Why don't we
go ahead and hold off on any further questions.
MR. HOOLAHAN: At this point I would like to
focus on the incremental recovery that can be attributed
directly to the import of the 100 million barrels of
Prudhoe Bay NGLs. As you may recall from earlier in my
testimony, the NGLs imported from Prudhoe will be mixed with
the enriching fluids indigenous to Kuparuk and blended with
Kuparuk lean gas to make MI. I also indicated that without the
import of enriching fluids from an outside source, EOR
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expansion would be limited to only 2 to 5 more drill sites
beyond the current pilot area. While over 200 million barrels
are expected to be recovered by large scale, only 180 million
of that total can be attributed to the import of NGLs. The
remainder corresponds to recovery from the two to five drill
sites that we could expand to using only indigenous enriching
fluids from Kuparuk. And it's also worth noting that of the
100 million barrels of Prudhoe Bay NGLs we expect to import,
roughly a third of that volume will drop out of the returned MI
and be stabilized in the oil and sold as part of the Kuparuk
crude stream.
Going through an incremental analysis to separate out
the benefits attributed solely to the NGL import, solvent
utilization factors for the Prudhoe Bay increment can be
determined. For MI made from Prudhoe Bay NGLs, it will take
4.6 thousand cubic feet of MI injected to recover one barrel of
EOR oil. We expect to get 1.3 barrels of EOR oil for each
barrel of Prudhoe Bay NGLs injected.
How this contrasts to the efficiency of Prudhoe will be
covered in the next section of my testimony.
CHAIRMAN JOHNSTON: So what kind of
efficiencies are you going to be obtaining on your conversion
of NGLs to MI?
MR. HOOLAHAN: We get about 5.9 thousand cubic
feet per barrel of NGLs.
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CHAIRMAN JOHNSTON: 5.9 thousand cubic feet per
barrel. Okay.
MR. HOOLAHAN:
infield drilling for a moment.
Now I would like to touch on
Infield drilling is related to
the EOR recovery process at Kuparuk in a couple of ways.
First, it improves -- it provides improved reservoir
sweep-out from under-performing patterns and increased
reservoir contacting in areas of partial or total structural
isolation. The more reservoir oil we contact with MI, the
higher the recovery potential.
Second, it provides for increased injectivity on a
given drill site, allowing us to reach our target slug size in
a shorter period of time.
To avoid any confusion, I want to make it clear that
although infield drilling is integral to the EOR recovery
estimates being provided in my testimony, these estimates do
not include the non-EOR benefits of infield drilling.
Exhibit 2-X shows existing and proposed well ~tocations
within the large scale EOR project area. Wells depicted in
blue are wells intended to be drilled on the periphery of the
field and pattern infield wells intended to improve reservoir
sweep-out from under-performing patterns.
Wells depicted in red are wells drilled in areas where
there is partial or total structural isolation between an
existing injection well and one of the offset producers.
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The infield wells included in this exhibit were
included in the determination of project benefits.
CHAIRMAN JOHNSTON: Now, before we leave that,
the shading on that, is that a dark blue that I'm looking at or
the light blue up there when you refer to blue or .....
MR. HOOLAHAN: The blue I'm referring to are
the individual well dots.
CHAIRMAN JOHNSTON: So could you -- I mean when
you say light blue are you referring .....
MR. HOOLAHAN: Let's see if I can highlight
one.
CHAIRMAN JOHNSTON: ..... to this shade down
here or is that black?
MR. HOOLAHAN: Like here -- here's one here and
one here. They show up a little bit better in the color copy.
And then this is the original project area here.
CHAIRMAN JOHNSTON: Okay.
COMMISSIONER BABCOCK: They don't show up at
all in the black and white copy.
MR. HOOLAHAN: They show up, they're just all
black.
The fault map in this exhibit should give you a feel
fro the degree of faulting at Kuparuk and the role that infield
drilling plays in improving areal sweep-out.
Exhibit 2-Z lists some of the details associated with
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the large scale project scope from a facilities standpoint.
This information is presented schematically on my next exhibit,
so rather than reading through each component of the project,
I'll give you a quick visual walk-through.
As I walk through Exhibit 2-AA, I will be starting on
the right-hand side and moving to the left. New facilities
being added are major modifications to existing facilities are
in color. We start out by making necessary tie-ins at
Prudhoe Bay Skid 50 that will allow a portion of the Prudhoe
NGL stream to be diverted to the Oliktok pipeline.
Modifications will be made to the Oliktok pipeline to allow
flow from Prudhoe to Kuparuk. That line originally was set up
to flow from Kuparuk to Prudhoe.
Remote operation capability will be added to the valves
on each side of the Kuparuk River, and other modifications as
necessary to prepare the line for NGL service will be made.
On the Kuparuk side, three pipeline pumps will be
installed at CPF-1 to boost the pressure of the incoming NGLs
for transport to CPF-2 via new 8-inch NGL pipeline and for
entry into the new collection drums installed at both CPF-1 and
CPF-2. The NGLs will be combined with indigenous enriching
fluids from Kuparuk within these collection drums.
At CPF-1 the indigenous enriching fluids are comprised
of NGLs from the CPF-1 NGL plant, scrubber liquids from the
artificial lift gas compression system and naphtha diverted
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MR. HOOLAHAN: I guess I would like clarify.
You know, we're not attempting to knock out the components out
of the RMI; actually, quite to the contrary. As part of the
small scale project and part of the small scale expansion we're
continually looking for ways to make as much solvent indigenous
to Kuparuk as we can. That's part of the reason that we are,
for instance, diverting naphtha from the topping plant. That
number offsets for every barrel that we wind up stabilizing,
that means it's another barrel that we have to import to make
solvent. And so if we can alter our operating conditions to
basically internally generate as much MI as possible, that's
what we intend to do.
COMMISSIONER BABCOCK: Do you know what the
current vapor pressure is at the Kuparuk stream?
MR. HOOLAHAN: Not off the top of my head, no,
sir.
COMMISSIONER BABCOCK: Or what effect this
additional NGL turned into MI, produced and sold with the oil,
what effect that would have on the vapor pressure?
MR. HOOLAHAN: The expectation is that the
components that do stabilize in the oil will be the heavier end
of the NGL barrel, but I can't speculate as to the actual
numbers that that will result in in terms of vapor pressure,
but it should be the bottom end of the more stabile end of the
barrel that winds up getting~stabilized, not so much the -- I
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would expect less of the -- say the butane level and expect
more of the heavier end of pentanes .....
COMMISSIONER BABCOCK:
MR. HOOLAHAN: .....
COMMISSIONER BABCOCK:
Uh-huh.
-- heavier.
Are the components --
the enriching fluid components being produced at -- being
produced from Kuparuk, are those salable?
MR. HOOLAHAN: There's a portion of those that
are salable and a portion that aren't. If you look at a barrel
of enriching fluid at Kuparuk, it's a rather broad band of
components. There's probably about half that that would be
pipeline stable, and the other half that would be non-pipeline
stable.
COMMISSIONER BABCOCK: So that would be
according to Exhibit 5, page 6, that would then be 7,000
salable barrels from Kuparuk injected?
MR. HOOLAHAN: That would be an approximate
number.
COMMISSIONER BABCOCK: Would you be able to
provide the Commission with an estimate of the effect on vapor
pressure of the Kuparuk stream as a result of the LSEOR and the
change in the composition of the production?
MR. HOOLAHAN: We could attempt to pull
together an estimate of that.
COMMISSIONER BABCOCK: And what it is
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currently?
to do that.
MR. HOOLAHAN: Yes, we can -- we will endeavor
COMMISSIONER BABCOCK: Okay.
CHAIRMAN JOHNSTON: In terms of the 100 million
that you're proposing to import from Prudhoe Bay, is that a
maximum number or minimum number, is it a goal, is the goal
likely to be achieved or likely to be exceeded or -- how do you
view that?
MR. HOOLAHAN: I like your references as a goal
would be probably a good way to reference that. The amount
that we're intending to import is -- meets kind of those
criteria that I described in the questions that I presented
earlier. The recovery at Kuparuk is more dependent on the
cumulative volume of solvent than it is on the timing and how
that solvent is brought in. Obviously, that -- the timing
affects economics, but the ultimate recovery numbers are more
tied to the absolute volume that's brought in.
CHAIRMAN JOHNSTON: So do you think it's
realistic then that eventually as this EOR process plays out
that you'll be importing more NGLs from Prudhoe Bay than the
100 million?
MR. HOOLAHAN: Right now the 100 million gets
us our targeted recovery and allows us to flood the drill sites
that we currently have in the plan. If, in the future, we
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identify additional opportunities to expand, that may, of
course, change.
CHAIRMAN JOHNSTON: So potentially then if you
did expand beyond your current scope, you would potentially be
looking at importing additional quantities of NGLs from
Prudhoe?
MR. HOOLAHAN: Yes.
CHAIRMAN JOHNSTON: And on the average how --
your yearly average of importation would be about what?
MR. HOOLAHAN: We start out at about 25, 26,000
barrels a day, and then that declines as the amount of
bootstrap increases, and we eventually taper off to where at
the end of the project we're bringing in very little outside
solvent.
CHAIRMAN JOHNSTON: And project life is
estimated to be how long?
MR. HOOLAHAN: We had worked the 15 to 20 years
is what the project that we -- the life that we base this on.
COMMISSIONER BABCOCK: Do you have any
estimates of the composition of the NGLs that you anticipate
getting from Prudhoe?
MR. HOOLAHAN: Maybe I can turn that around a
little bit. We tend to be somewhat insensitive to the
composition.
COMMISSIONER BABCOCK: That's what I see.
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MR. HOOLAHAN: Because the -- from our
laboratory studies we found that over a wide range of enriching
fluids, we can make miscible injectant. What the change in
composition -- any change in composition would impact would be
the level of enrichment that we would have to get to. So the
5.9 number would go up or down and require -- would require us
to import a little more or a little less. But we're still able
to make the solvent that meets our MMP criteria.
COMMISSIONER BABCOCK: Well, presumably since
the composition at Prudhoe of the NGLs changes significantly,
depending on how much the CGF is producing, that would also
have an impact on what components were available to be knocked
out to establish your 35 percent recovery by mixing it with oil
at your separators at Kuparuk.
MR. HOOLAHAN: Uh-huh.
COMMISSIONER BABCOCK: What sort of
compositional changes have you considered in making that 35
percent estimate?
MR. HOOLAHAN: We haven't examined the -- in
great detail, that range. What we have looked at is the -- our
ability to make MI from NGL based or NGL type solvents, and the
uncertainties that are out there didn't appear to be sufficient
to alter the project decision. So while it will potentially
impact the solvent -- or the conversion factor, so to speak,
NGLs to MI at Kuparuk, if we can still get the amount of
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solvent we need over the course of field life, the impact on
the project could be minimal to not at all.
COMMISSIONER BABCOCK: So what relationship did
the composition of the NGLs from Prudhoe have on your estimate
of recovering 35 percent of the NGLs by mixing it with your oil
at the separators when it comes back up?
MR. HOOLAHAN: Could you rephrase the question?
MR. HOOLAHAN: What can you show me about your
consideration of how the composition of NGLs secured from
Prudhoe may affect your estimate of 35 percent recovery of the
NGLs injected by mixing the NGLs recovered .....
MR. HOOLAHAN: Of the stabilization into the
crude?
COMMISSIONER BABCOCK: ..... at the
stabilization, uh-huh.
MR. HOOLAHAN: The only -- I could speculate or
guess as to what that would be.
COMMISSIONER BABCOCK: Well, no. What I'm
asking for is what you used as a compositional basis in order
to predict to us that you'll recovery 35 percent.
MR. HOOLAHAN: We used an internal estimate as
to the volume or the compositions to generate a -- the
conversion factors that we used.
COMMISSIONER BABCOCK: I think we'd like to
have that established since we've heard a lot of testimony in
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another hearing regarding the critical importance of
predictions based on -- or compositional analysis. So if you
would provide the Commission with what the basis for your --
compositional basis for the 35 percent prediction?
MR. HOOLAHAN: Yeah. The main point I would
like to make there is that our -- let me have a slide that may
help us -- may help here. This slide is from -- is in the
back-up data, and this is the result of slimtube experiments --
slimtube displacements in the laboratory. And what the
slimtubes are used for is to establish the -- we run two kinds
of different slimtubes. We have what are called MME or minimum
miscibility enrichment, and we have MMP, which are minimum
miscibility pressure. The MME experiments are run to determine
the level of enrichment needed to reach miscibility at a given
pressure. The slimtubes run, one through nine, were run on a
wide variety of different solvents -- enriching fluids from
some very, very lean enriching fluids that we would require
over 75 percent of enrichment down to a synthesized Prudhoe Bay
NGL, which is on the order of about 21 percent enrichment.
These are a Kuparuk type enriching fluids here. As you can see
the variation between variations in the composition of the NGL
don't seem to have a significant impact on the level of
enrichment required. So that's not an area that we have spent
a great deal of time working sensitivities. What we were
primarily working toward was the uncertainty in this level of
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enrichment, sufficient to change or alter the decision to
pursue forward with the process. Obviously as you get -- as
you move forward into the optimization process, down the road
that information will become more useful, but at this point we
haven't spent a lot of effort nailing that down.
There's another slide. This is basically what you're
looking at when you have a slimtube series where you're looking
at the level of enrichment needed to provide a recovery in the
slimtube. And this is a -- it's a single -- the sandpacked
tube that's very thin that you displace the miscible solvents
through the oil. It's kind of a one dimensional, no
dispersion, ideal recovery; if you contact it you get it. And
what you see from here, as well, is that we don't see a sharp
breakover at the miscibility point, it's a gradual breakover
until you get quite a ways below. And so, you know, that
insensitivity around the level of enrichment, even in our
laboratory experiments if we're slightly under-enriched, that
doesn't have -- would appear to have that great of an impact on
our projected recoveries.
COMMISSIONER BABCOCK: That's protected recover
of EOR?
MR. HOOLAHAN: Right. Or projected recoveries
of the EOR process.
COMMISSIONER BABCOCK: Well, could you then
just -- in response to my question you had suggested that
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during the stabilizing process you'd be knocking out the
heavier component rather than the butanes, and what I'd like to
know is what was the compositional basis or compositional model
that you used to make that estimate?
MR. HOOLAHAN: We're -- and there are probably
some assumptions that we would need to go into for what that
basis is.
COMMISSIONER BABCOCK: Well, that's what
I eee®e
MR. HOOLAHAN: We didn't work that problem
extremely rigorously, given the insensitive nature that we saw
in terms of what our blending quantities would have to be.
So .....
COMMISSIONER BABCOCK: But insofar as you felt
comfortable making a prediction about how much NGL would be
recovered by stabilizing with the oil, I would like to know if
you didn't do any, that's fine; if you did -- not a rigorous,
that's fine, but I would like to know what it is that you did
in order to analyze the composition of NGLs and its
relationship to that stabilization. Whatever that was, if you
could submit that as an exhibit after the hearing, that would
be what I'm asking for.
MR. HOOLAHAN: We will endeavor to do that.
COMMISSIONER BABCOCK: Okay. That's all I had.
MR. HOOLAHAN: Are you read to move on to .....
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Mr. Hoolahan.
CHAIRMAN JOHNSTON: Yes.
MR. HOOLAHAN: ..... question 2?
CHAIRMAN JOHNSTON: Please continue,
COMMISSIONER BABCOCK:
take a 10 -- 5-minute break?
Mr. Chairman, may we
CHAIRMAN JOHNSTON: Let's take a 5-minute or
10-minute break and let everybody stretch their legs.
(Off record - 10:17 a.m.)
(On record - 10:35 a.m.)
CHAIRMAN JOHNSTON: I'd like to call this
hearing back in session. We just took a -- oh, I guess a
15-minute break. The time is about 25 to eleven o'clock. So,
Mr. Hoolahan, if you'd care to proceed.
MR. HOOLAHAN: Yes. One point of clarification
I'd like to -- or distinction I'd like to draw is probably
between the facility differences between Kuparuk and Prudhoe.
One of the things at Kuparuk is we don't have a CGF type
process at Kuparuk, and in terms of the -- like I alluded to
earlier is we're trying to draw every barrel of enriching
fluids out that we can, because for each of those barrels that
we knock out of the liquid stream or the gas stream that we can
take out, we can increase the recovery at Kuparuk.
With that do you want to move on to question 2?
CHAIRMAN JOHNSTON: Any other questions?
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COMMISSIONER BABCOCK: No.
CHAIRMAN JOHNSTON: Okay. Please,
Mr. Hoolahan, if you'd go ahead with question 2 then.
MR. HOOLAHAN: All right. Question 2 is: What
is the scope and timing of the EOR project?
The scope, the LSEOR project will significantly expand
the small scale EOR -- SSEOR project beyond Drill Sites i-A,
l-Y, and 2-Z, and is designed to ultimately cover 18 additional
drill sites -- KRU drill sites.
NGLS from Prudhoe Bay will be combined with Kuparuk
enriching fluids and blended with Kuparuk lean gas for
injection as MI. Specifically the planned LSEOR project
involves expansion of enriched gas EOR project -- process
beyond Drill Sites l-A, l-Y, and 2-Z to Drill Sites l-F, i-G,
l-Q, l-R, 2-A, 2-B, 2-C, 2-D, 2-F, 2-G, 2-H, 2-K, 2-N, 2-T,
2-U, 2-V, 2-W, and 2-X.
The basis for scope -- the scope for the LSEOR project
is dictated by a number of factors, including an existing
infrastructure, anticipated field life, MI slug size, reservoir
performance, and availability of solvent. In order to maximize
economic recovery and minimize investment risk, the LSEOR
project is designed to fully utilize existing Kuparuk IWAG
infrastructure. Thus, the project contemplates relatively few
additional facilities.
The existing IWAG infrastructure can support expansion
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up to 18 additional drill sites. Reservoir modeling of the --
and the SSEOR project show that the optimum MMI slug size is 20
to 30 percent of a given drill site's hydrocarbon pore volume.
In order to flood 18 additional drill sites with the optimum MI
slug, approximately 1 trillion standard cubic feet of MI will
be required over the life of the LSEOR project. This is
expected to produce an additional 200 million barrels of EOR
oil. To reasonably ensure this recovery within the expected
remaining life of the Kuparuk River Field, the injectant -- the
injection of 1 trillion cubic feet of MI is planned to be
completed within the 15 to 20 years of project start-up.
The 1 trillion cubic feet of MI will be comprised of
outside enriching fluid, indigenous Kuparuk enriching fluid,
and indigenous Kuparuk lean gas. As stated previously, the KRU
Working Interest Owners currently plan to use Prudhoe Bay NGLs
as the outside enriching fluid. Over the life of the project
approximately 100 million barrels of Prudhoe Bay NGLs will need
to be blended with indigenous Kuparuk enriching fluid to
produce 1 trillion cubic feet of MI at Kuparuk.
The expected recovery from the project can be achieved,
notwithstanding reasonable variations in the rate of Prudhoe
Bay NGL deliveries, so long as 100 million barrels of Prudhoe
Bay NGLs are injected within the life of the project.
Timing. The SSEOR project was approved by the
Commission in June 1987, and miscible enriched gas EOR
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operations have been conducted in several patterns at Drill
Sites l-A, l-Y, and 2-Z since that date. Due to the success of
the SSEOR project, the LSEOR project was approved by the
working interest owners of the KRU in March 1995.
Start-up of the facilities integral to this project is
scheduled to begin on or about November 1, 1995, and to be
completed by late 1996. Upon completion of start-up, 12 to 15
Kuparuk drill sites, including one 1-Y -- i-A, 1-Y and 2-Z will
be flooded with MI. The remaining six to nine planned EOR
drill sites will commence MI injection as maturity EOR patterns
are converted back to water or lean gas injection. The
expected duration of the LSEOR project is 15 to 20 years.
Question 3: What are the proposed volumes and
composition of the NGL sold to KRU?
Preliminarily, it should be noted that .....
COMMISSIONER BABCOCK: Oh, excuse me. I'm
sorry, I did have a question on Number 2. Do you have any
estimate for the volumes of the -- over the 15 to 20-year life
of the project of Kuparuk enriching fluid and Kuparuk lean gas?
MR. HOOLAHAN: Not right off the top of my
head.
COMMISSIONER BABCOCK:
you provide those figures?
those.
Well, we've got -- could
MR. HOOLAHAN: Yes, we could; we could provide
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COMMISSIONER BABCOCK: Thank you.
MR. HOOLAHAN: Preliminarily, it should be
noted that the Prudhoe Bay Unit will not be selling NGLs to the
Kuparuk River Unit. The Prudhoe Bay Unit is not a business
entity capable of selling NGLs as a unit. Although ARCO, as
operator of the Kuparuk River Unit, is authorized under the
Kuparuk River Unit Operating Agreement to purchase materials on
behalf of the Kuparuk Working Interest Owners for use in
Kuparuk River Unit operations, all of the Kuparuk Unit Working
Interest owners have elected to supply NGLs to the LSEOR
project in-kind.
The LSEOR project is expected to acquire 100 million
barrels of NGLs from Prudhoe Bay during the expected 15 to
20-year life of the project. Consistent with the project
scope, as described above, the KRU currently plans to acquire
up to 26,000 barrels per day upon completion of start-up
activities in 1996. This rate will decline over time as the
volume of returned MI increases.
The MI used in the LSEOR project will be comprised of
Prudhoe Bay NGLs, indigenous Kuparuk enriching fluid, and
indigenous Kuparuk lean gas. The composition of Prudhoe Bay
NGLs will vary, depending on actual CGF operating conditions.
The Kuparuk enriching fluid is comprised of several light
hydrocarbon streams produced by the KRU facilities.
Specifically, the CPF-1 enriching fluid is comprised of
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scrubber liquids from the CPF-1 artificial lift gas compression
system. NGLs from the CPF-1 NGL plant and naphtha, from the
Kuparuk River Unit topping plant.
The CPF-2 enriching fluid is comprised of scrubber
liquids from the CPF-2 artificial lift gas compression system,
and NGLs from the CPF-2 fuel gas stripping unit.
Laboratory core flood experiments indicate that MI with
these constituents is fully compatible with the Kuparuk River
formation. Based on the results of the experiments, simulation
studies and the SSEOR project, the LSEOR project expected to
have sufficient flexibility to handle reasonable variations in
enriching fluid volume and composition.
CHAIRMAN JOHNSTON: Could you more fully
explain what you mean by the Kuparuk River Unit Working
Interest Owners have elected to supply NGLs to the project
in-kind?
MR. HOOLAHAN: From the Kuparuk operator
standpoint, the operator has the option to either purchase on
behalf of the individual owners or can allow he owners to
supply material in-kind. That option has been made available
to the owners at Kuparuk, and all of the owners have elected to
supply their NGLs in-kind.
So, from Kuparuk's standpoint and from an operator
standpoint, we know where the NGLs are coming from, but
individual companies will be making their own arrangements to
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bring those NGLs to -- or to acquire those NGLs for use at
Kuparuk.
CHAIRMAN JOHNSTON: For example, of that 26,000
barrels per day that you'd propose to start, you know, the full
scale project with, how many of those barrels per day are ARCO
barrels per day?
MR. HOOLAHAN: They would be Kuparuk's share of
that 26,000 -- Kuparuk Working Interest shares, so it would be
55 percent roughly of that volume.
CHAIRMAN JOHNSTON: So, presumably, assuming
that was -- you're importing that then 55 percent of the stream
that you're importing would be ARCO .....
MR. HOOLAHAN: Yes.
CHAIRMAN JOHNSTON: ..... NGLs?
MR. HOOLAHAN: That's correct.
CHAIRMAN JOHNSTON: Okay. The if ARCO is
providing 55 percent of the NGLs, then do you also acquire 55
percent of the EOR oil?
MR. HOOLAHAN: With -- notwithstanding
royalties and all that, yes, .....
CHAIRMAN JOHNSTON: Right. But that .....
MR. HOOLAHAN: ..... we would get our .....
CHAIRMAN JOHNSTON: ..... that's in a
simplistic .....
MR. HOOLAHAN: ..... Kuparuk share of the
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benefits from this.
CHAIRMAN JOHNSTON: Okay. So the benefits
really are one to one. If you supply one barrel of the -- or
one percentage of the NGL, you will get one percentage of the
EOR oil, less the royalties and such?
MR. HOOLAHAN: That is correct.
CHAIRMAN JOHNSTON: Okay.
MR. HOOLAHAN: Question 4?
COMMISSIONER BABCOCK: Would you just briefly
go over the other owners and their percentages at Kuparuk?
MR. HOOLAHAN: BP owns roughly 39 percent;
Unocal owns roughly 5 percent; and the remaining three owners
combined own roughly one percent. And the remaining three
owners are Exxon, Chevron and Mobil.
COMMISSIONER DOUGLASS: And do all of those
owners have in-kind NGLs to provide the Kuparuk River Unit?
MR. HOOLAHAN: All of the owners will be
providing NGLs in-kind. Where they obtain those NGLs or how
they obtain those NGLs, is outside of the Kuparuk -- out of the
Kuparuk boundary area sphere.
CHAIRMAN JOHNSTON: But you've ascertained that
each one of these working interest owners has the ability to
supply the appropriate volumes or their designated volume of
NGLs in-kind?
MR. HOOLAHAN: Right. Are there any further
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questions before we move on to question 4?
CHAIRMAN JOHNSTON: How will you determine what
exactly is EOR oil compared to your oil produced through
primary means?
MR. HOOLAHAN: The oil, when it's produced, is
indistinguishable. That will be based on simulation results.
You can see it from declining curve observations.
CHAIRMAN JOHNSTON: And is there agreement
among the working interest owners relative to the process that
you will undergo in order to arrive at the allocation of EOR
barrels among the working interest owners?
MR. HOOLAHAN: The EOR barrels, there won't be
a distinct allocation of EOR barrels among the owners. There
will be barrels allocated among the owners. The volume that is
shipped down out of Kuparuk is in total is distributed among
the owners. There's not a separate allocation for EOR oil
versus waterflood oil versus primary depletion oil.
COMMISSIONER BABCOCK: And you said earlier
that ARCO and BP, at least, had concurred regarding your
simulation results?
MR. HOOLAHAN: Yes.
COMMISSIONER BABCOCK: Is there a document that
exists that gives ARCO, as operator at Kuparuk, confidence that
all the working interest owners are going to be able to provide
their share of NGLs in-kind?
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MR. HOOLAHAN: We have the Sullivan election
notifications that each company has provided, where they have
indicated that they are -- they will be supplying in-kind. I'm
presuming that if they are electing to supply in-kind that they
have made the necessary arrangements to be able to do so. In
the event that they are unable to do so, then there are
provisions for the operator to supply on their behalf.
CHAIRMAN JOHNSTON: In which case then you
would make an adjustment to the amount of oil that they are
allocated?
MR. HOOLAHAN: There would be an adjustment for
the -- our expense incurred for acquiring solvent. It would be
through a -- arranged through a competitive bid process.
COMMISSIONER BABCOCK: I would like a copy of
that agreement, submitted for informational purposes to the
Commission.
MR. HOOLAHAN: All right. Question 4: What is
the relative efficiency of the injectant as an EOR agent in the
KRU as compared to the PBU?
The Kuparuk LSEOR project is expected to recover an
average of 1.3 barrels of incremental EOR oil for each barrel
of Prudhoe Bay NGL injectant. With respect to Prudhoe Bay, the
Prudhoe Bay operators present different values to the
Commission as part of the recent Phase I Prudhoe Bay hearings.
ARCO's base case for Prudhoe was an average of 0.3 barrels
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incremental EOR oil for each barrel of NGL injected. BP's base
case for Prudhoe was an average of 0.6 barrels.of incremental
EOR oil for each barrel of NGLs injected.
There are a number of generic reasons why the
efficiency of EOR projects will vary from reservoir to
reservoir. The Kuparuk efficiency is expected to be above
Prudhoe's for the following reasons:
One, the Kuparuk flood is less mature than the Prudhoe
flood; i.e., starting at the front end of the recovery curve.
Two, the Kuparuk reservoir is thinner than Prudhoe's; i.e.,
less gravity override. Three, Kuparuk has a higher target
residual oil saturation following waterflood than Prudhoe; and,
four, Kuparuk is able to make more standard cubic feet of MI
per barrel of NGL because the Kuparuk reservoir temperature is
lower than Prudhoe's. The NGLs will be blended into a richer
lean gas at Kuparuk, and the reservoir fluid characteristics
are different.
Question 5: What is the effect of sales to KRU on
recovery from PBU?
None. NGLs from the Kuparuk -- NGLs for the Kuparuk
LSEOR project are those that would have otherwise have been
transported down TAPS. As such, the NGLs being recovered --
the NGLS being removed downstream of the Prudhoe recovery
system.
Question 6: What is the effect of sales to KRU on the
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disposition of NGLs from PBU?
Because NGLs for the Kuparuk LSEOR project are those
that would have otherwise been transported down TAPS, there
will be a reduction in the volume of NGLs transported down
TAPS. In addition, there could be tariff impacts due to
differences in throughput, quality bank, and pumpability.
COMMISSIONER BABCOCK: On question number 6,
since the NGL pipeline and the CGF in combination are able to
produce up to 100,000 barrels of NGL a day, what would make you
assume, in answering this question, that all the NGLs
transported to Kuparuk would otherwise have been transported
down TAPS?
MR. HOOLAHAN: Within the current contractual
architecture within Prudhoe the NGLs that are available for
take in-kind are from the barrels that you would otherwise put
down TAPS. At least that's my understanding.
CHAIRMAN JOHNSTON: So it's your testimony then
that the Kuparuk project would not translate into more NGL
barrels being produced out of Prudhoe Bay, that Prudhoe Bay
will produce the same volume of NGLs regardless of whether your
project goes forward or not?
MR. HOOLAHAN: That's my understanding. The
last topic of my presentation deals findings and conclusions.
As outlined in our application, we have proposed a number of
findings and conclusions which we would like for the Commission
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to adopt. We are also seeking the Commission's endorsement of
areal expansion of MI injection and infield drilling within the
EOR areas.
As a point of clarification, I would like to qualify
proposed finding number 9 to recognize factors that could
impact the estimated incremental recovery from the LSEOR
project. These qualifications are listed in Exhibit 2-FF, and
are the same as presented here in my testimony today.
The concludes my presentation. At this point I would
like to ask that the application for the project be submitted
to the -- that was submitted to the Commission on June 7th be
made a part of the record, which I believe was done at the
beginning, if I'm not mistaken, and I also have a color copy of
the exhibits as the official record.
CHAIRMAN JOHNSTON: Very good.
MR. RODGERS: Let me ask that Exhibits -- ARCO
Exhibits 1 through 5 be made part of the record.
CHAIRMAN JOHNSTON: Yes. ARCO Exhibits 1
through 5, noting that exhibit number 5 is the application, are
made part of the record. Thank you.
We do have a couple of questions from the audience.
COMMISSIONER BABCOCK: Mr. Chairman, before we
get to that, on Exhibit 5 there was included a map. Is that
included in the Exhibit 5 -- in what has been described as
Exhibit 5 that the Commission received there's a map. The map
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also is in the Exhibit 5 that the Chairman has in his hand.
That map -- does ARCO wish that map to have any confidentiality
associated with it?
MR. HOOLAHAN: Let me check with our legal
folks. (Pause) Yes, we would like to make that part of the
exhibit.
CHAIRMAN JOHNSTON: So we'll note that the ARCO
Exhibit Number 5 includes the map that was included in that
packet. Thank you. Any other comments before we go to
the .....
COMMISSIONER BABCOCK: No.
CHAIRMAN JOHNSTON: Okay. Let me just read
down through these questions. Number one, what is the
projected capital cost for drilling?
MR. HOOLAHAN: I don't have that number right
off the top of my head.
CHAIRMAN JOHNSTON:
MR. HOOLAHAN: Yes.
estimate of that.
CHAIRMAN JOHNSTON:
Can you provide that?
I think we can get an
Two, what is the Kuparuk
River Unit field life with and without this particular EOR
project?
MR. HOOLAHAN: The way that we approached the
evaluation of this project was from the standpoint of does it
fit within our anticipated field life. The evaluations for
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what it does to field life we haven't worked in any detail.
CHAIRMAN JOHNSTON: So you don't know whether
it does or does not extend field life?
MR. HOOLAHAN: I would expect it to extend
field life, but I don't have the analyses right off that verify
that.
CHAIRMAN JOHNSTON: So conversely then you
wouldn't -- how would you comment then whether you believe
field life would end at the end of this particular project?
MR. HOOLAHAN: The assumptions we -- within the
other owners involved in the analysis of this we had agreed to
assume a 20/20 type field life for evaluation purposes.
CHAIRMAN JOHNSTON: Okay. Do you plan any
efforts to pursue gas cycling after this particular project?
MR. HOOLAHAN: That will obviously be one of
the optimizations that we'll likely look at after we get
through the project through the implementation phase.
CHAIRMAN JOHNSTON: So that may be something
that you may be addressing in the future .....
MR. HOOLAHAN: Yes.
CHAIRMAN JOHNSTON: ..... but you have not
really flushed out anything along those lines at this time?
MR. HOOLAHAN: Right now we are concentrating
our efforts on implementation. It looks like a go with what we
have, so the optimizations are obviously something that are a
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little further down the road.
CHAIRMAN JOHNSTON: And, finally, can you
provide the state with projected production profiles with and
without the EOR project?
MR. HOOLAHAN: The production profiles -- I
could probably provide an ARCO profile providing a unit
profile. Maybe somewhat difficult, given that we all have
different projection as to import rates and field performance
evaluations.
CHAIRMAN JOHNSTON:
have you provide the ARCO profiles.
other .....
COMMISSIONER BABCOCK:
Perhaps if we could just
Okay. Thank you. Any
Has there been any loss
in ultimate recovery by this project starting now instead of
three years ago or four years ago?
MR. HOOLAHAN: Well, without the project
starting, I don't think we're really losing recovery, as we
haven't really initiated the -- installed the project yet. The
project is designed to get to all of the drill sites that we
see as currently available, so the recoveries, I would suspect,
would be what we're currently seeing. Again, the controlling
factor there is being able to import the volume of solvent that
we need within field life. If we delay going forward -- if we
were to delay going forward much longer what that may do is put
the recovery more at risk due to field life considerations.
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CHAIRMAN JOHNSTON: Do you have any concern
relative to the overall timing of the project? In other words,
is timing a matter of importance for you; do you gain by
beginning the flood and actually pursuing it as quickly and as
rapidly as you can or is it something that you do not lose any
recovery is the project is delayed, you know, a year or two?
MR. HOOLAHAN: From a recovery standpoint, we
don't currently see -- the recovery tends to be more controlled
by the cumulative volume injected rather than by the timing or
the rate at which that is injected.
CHAIRMAN JOHNSTON: So you don't have concerns
relative to corrosion within the Kuparuk field? How about the
maturity of the waterflood?
MR. HOOLAHAN: Part of the reason for
initiating the project now, as well as -- you know, as the
C-sand starts to mature we want to be able to get into those
areas before it reaches maturity. But the current scope of the
project is certainly compatible with that -- with those levels
of maturity.
CHAIRMAN JOHNSTON: So in that particular case
you may be better off getting the solvent into the reservoir
sooner than later then?
MR. HOOLAHAN: That's possible. The -- it may
structure it, which drill sites we go to, in what order and the
sequencing would be potentially impacted by that.
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CHAIRMAN JOHNSTON: Do you see any application
of using this solvent in any oil pools overlying the Kuparuk?
MR. HOOLAHAN: I haven't evaluated that.
CHAIRMAN JOHNSTON: You haven't looked at that.
Okay. Any other questions?
COMMISSIONER BABCOCK: No.
CHAIRMAN JOHNSTON: Any other questions?
COMMISSIONER DOUGLASS: None.
CHAIRMAN JOHNSTON: Okay. Apparently we're
done with our questions, Mr. Hoolahan. I want to thank you.
MR. HOOLAHAN: Thank you.
CHAIRMAN JOHNSTON: I'd ask are there any other
members of the audience wishing to appear before the Commission
in this matter, make any statements or anything? Okay. There
being none, we'll recess for the day. I believe we have some
information that you've indicated that you will provide us.
Why don't we keep the hearing record open for at least two
weeks in order to allow that information to come in to us, and
once we get that information and after the two weeks, then we
are likely then to close the hearing record or during that time
if we have additional questions we can contact you and ask for
clarification.
MR. RODGERS: We'll try to get you the
information within the next week.
CHAIRMAN JOHNSTON: Pardon me?
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extension.
in a week.
MR. RODGERS: I don't think we need a two-week
We anticipate being able to make these submissions
CHAIRMAN JOHNSTON: Okay. I think I still
would prefer to keep the hearing record open two weeks to allow
that assurance and get that. That will not necessarily affect
our ability to issue the order in this thing. We realize that
you are chomping at the bit to get this project underway, and
we appreciate that.
Any other comments then before we recess for the day?
There being none, this hearing is in recess.
(Off record - 11:05 a.m.)
(END OF PROCEEDING)
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CERTIFICATE
UNITED STATES OF AMERICA)
) ss
STATE OF ALASKA )
I, Laurel L. Evenson, Notary Public in and for the
State of Alaska, residing at Anchorage, Alaska, and reporter
for R & R Court Reporters, Inc., do hereby certify:
THAT the annexed and foregoing Public Hearing of the
Alaska Oil and Gas Conservation Commission was taken before me
and Joseph Kolasinski on the 20th day of July 1995, commencing
at the hour of 9:00 o'clock a.m., at the offices of the Alaska
Oil and Gas Conservation Commission, 3001 Porcupine Drive,
Anchorage, Alaska, pursuant to Notice;
THAT this Transcript, as heretofore annexed, is a true
and correct transcription of the testimony given at said Public
Hearing, taken by me and Joseph Kolasinski and thereafter
transcribed by me;
THAT the original of the Transcript will be lodged with
the Alaska Oil and Gas Conservation Commission, 3001 Porcupine
Drive, Anchorage, Alaska;
THAT I am not a relative, employee or attorney of any
of the parties, nor am I financially interested in this action.
IN WITNESS WHEREOF, I have hereunto set my hand and
affixed my seal this 24th day of July 1995.
Notary Public in and for Alaska
~ STATE OF ALASKA~ ~
i . __NOTARY PUBLIC ' ~
~ IJ%URI~I, £. I:VI~NSON j
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from the Kuparuk copying plant. At CPF-2, the indigenous
enriching fluids are comprised of scrubber liquids from the
artificial lift gas compression system and NGLs from the fuel
gas conditioning skid.
At CPF-1 we will be re-wheeling the small scale
expansion -- the small scale expansion project's injection pump
which was just recently installed from 220 gallons per minute
to 360 gallons per minute. At CPF-2 we will be replacing the
existing 180-gallon per minute small scale injection pump with
a new 800-gallon per minute injection pump.
Finally, the addition of this equipment increases the
electrical command at CPF-1 to ensure that we have adequate
power supply available at CPF-1, especially during winter
months when demand is at its peak. The CPF-1 and CPF-3 power
systems will be linked.
The timing of these various .....
COMMISSIONER DOUGLASS: Before you leave that
one could you address where the NGLs will be metered, leaving
Prudhoe Bay?
MR. HOOLAHAN: They'll be metered within Skid
50, and then they'll also be metering on the Kuparuk entry
side; so there's metering in both places.
The timing of these various facility modifications
leads to a stage start-up of the project. We are currently on
schedule to commission the Oliktok pipeline, the pipeline pumps
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at CPF-1 and the CPF-1 facility upgrades by November of this
year. That will enable import of between two to 4,000 barrels
per day of Prudhoe Bay NGLs, bumping our MI injection capacity
from its current level of 65 million cubic feet per day to
90 million cubic feet per day. This will allow us to convert
two or three of the current IWAG drill sites to MI injection.
During the first quarter of next year we will remove
the current small scale injection pump at CPF-2, replace it
with a higher capacity, large scale injection pump. We intend
to continue NGL import to CPF-1 during this time with MI
injection capacity dropping back to 65 million cubic feet per
day during the CPF-2 construction work.
By late next year we expect to have full start-up of
the remaining project elements and to be importing 20 to 30,000
barrels per day of Prudhoe Bay NGLs. Our average MI injecting
capacity is expected to be on the order of 220 million cubic
feet per day. This will allow us to convert an additional
seven to 10 drill sites to MI injection.
CHAIRMAN JOHNSTON: Now, when you refer to two
to four million barrels per day of Prudhoe Bay NGLs .....
MR. HOOLAHAN: Two to 4,000.
CHAIRMAN JOHNSTON: Excuse me. Two to 4,000
barrels per day of NGLs, does that translate to standard cubic
feet at 5.9?
MR. HOOLAHAN: Yes, that would create 5.9
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thousand cubic feet per barrel of NGL imported.
COMMISSIONER BABCOCK: Back on Exhibit 2-AA --
you don't need to really put it back up -- what have you
estimated the cost of those facility upgrades that you identify
in that exhibit?
MR. HOOLAHAN: Yeah, the total project for --
there's three different components. There's a component that's
a Prudhoe Bay component; there's a component that's an Oliktok
component; and a component that's a Kuparuk Unit component.
The three of those together is somewhat under $40 million. And
that doesn't include any of the facility hookups for the
infield wells that will be needed.
COMMISSIONER BABCOCK: Right. Are all of those
costs being incurred by the Kuparuk owners?
MR. HOOLAHAN: No. The portion of the costs,
about $32 million, are being incurred by the Kuparuk owners,
and there's about another 2-1/2 or so that is being incurred by
Oliktok, and then the remainder is being incurred by ARCO and
BP as -- on the Prudhoe Bay site.
COMMISSIONER BABCOCK: Okay. Thank you.
MR. HOOLAHAN: The remaining drill sites will
be converted to MI injection as the existing ones mature. In
terms of operating the large scale EOR project in the field,
there are certain data that we intend to collect, both on a
routine basis and on an as needed basis. This data will aid in
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conducting current operations and will serve as a guide for
future operation optimization efforts.
The primary objective is to maximize EOR benefits from
the overall project while minimizing NGL imports. The data we
collect will be helpful in establishing the optimum enrichment
level WAG ratios, MI slug sizes, pattern conversion, timing,
et cetera.
This brings us to the six topics that the Commission
specifically requested be addressed. We have taken the liberty
of stating the topics in question form and have prepared
written responses to be entered into the record as Exhibit 4.
With respect to those matters specific to Prudhoe Bay,
the Prudhoe Bay operators were consulted and have agreed to the
response provided.
I will now read these responses:
On June 7, 1995, ARCO Alaska Inc, ARCO, as operator and
on behalf of the Kuparuk River Unit Working Interest Owners,
filed an application for injection for the Kuparuk River Unit
Large Scale EOR Project. By public notice and by letter dated
July 11, 1995, the Commission indicated that information on six
topics would be helpful at the public hearing scheduled for
July 20, 1995.
At least three of the indicated topics pertained to
Prudhoe Bay Unit NGL production and recovery issues, topics 4
through 6. ARCO, as operator of the Eastern Operating Area of
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the Prudhoe Bay Unit, and BP Exploration Alaska Incorporated,
BP, as operator of the Western Operating Area of the Prudhoe
Bay Unit, are in a better position to respond to topics 4 to 6.
Therefore, the Working Interest Owners of the Kuparuk River
Unit have consulted with the Prudhoe Bay operators for
information regarding topics 4 through 6.
Question 1: What is the additional recovery from KRU
anticipated?
As stated in the application for injection, incremental
oil recovery from the 18 additional LSEOR drill sites is
expected to range from 4 percent to 10 percent of the original
oil in place, resulting in over 200 million barrels of
additional Kuparuk oil reserves.
Recovery of these reserves, pursuant to the LSEOR
Project Plan, is conditioned upon, one, the acquisition of
approximately 100 million barrels of NGLs within the
anticipated field life; two, infield drilling, as outlined in
the application; three, sufficient injection well capacity;
and, four, expansion to all the proposed drill sites. In
addition to the incremental oil recovery described above,
approximately one-third of the acquired NGLs are expected to
stabilize out of the returned MI and be exported as part of the
Kuparuk crude stream.
The NGL injection rate will affect the timing of
recovery but not affect the amount of additional reserves
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recovered provided that the above conditions are met.
Question 2: .....
COMMISSIONER BABCOCK: Before you get to
question 2, Mr. Hoolahan, if we go back to the -- helping me
understand the relationship of the 35 percent -- the
bootstrapping of 40 million barrels of NGL, could you help
explain what the actual RMI is that you're expecting from every
thousand -- what percentage of a thousand cubic feet of
injectant do you expect to be RMI?
MR. HOOLAHAN: The easiest way to probably
explain that is to start with as we inject a barrel of NGL in
the form of MI into the reservoir about 40 percent of that, on
the first pass through the reservoir, becomes trapped. So we
have 60 percent of that barrel comes back to the surface.
COMMISSIONER BABCOCK: Okay.
MR. HOOLAHAN: Of that 60 percent of a barrel
that comes to the surface about 40 percent of that is dropped
into the oil stream, and the remainder is used to make
additional MI. The next pass through the reservoir there's
further trapping, although to a lower extent, and then there's
-- the same process comes back up on the surface again, but the
fluids partitioning between the oil stream and the gas stream.
So that is as you pass through the reservoir and are able to --
we estimate that we're able to take the Prudhoe Bay NGLs and on
an average through the reservoir about 2-1/2 times, it takes
R 8, R COURT REPORTERS
810 N STREET 1007 WEST THIRD AVENUE
277-0572/Fax 274-8982 272-7515
ANCHORAGE, ALASKA 99501
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
39
you from 100 million barrels to about 140 million barrels.
COMMISSIONER BABCOCK: Okay. That does help
clear it up for me. What do you anticipate the -- once this
process is fully underway and you are getting your returned MI
and 40 percent of the 60 percent -- that's how you mean to
describe it, 40 percent of 60 percent goes into the oil?
MR. HOOLAHAN: Right.
COMMISSIONER BABCOCK: What would then be their
resulting vapor pressure of the Kuparuk stream tendered at Pump
Station 1 or tendered -- mixes with Milne at that point then?
MR. HOOLAHAN: Oh, I don't have that right off
the top of my head. It -- the amount that we're talking about
stabilizing is what, based on the facility operations that we
have that would be consistent with the vapor pressure specs.
That's assuming the current facilities' operations.
COMMISSIONER BABCOCK: I guess what I was
getting at is that you can run your separators to knock out
more of the NGL components that come up or less, depending on
what you want to do with those components, and when you knock
out the components in the separator you can end up with less
overall volume than if you returned it to the stream after
processing it through gas processing and returning it at NGLs,
which is a justification for doing it the way that they do at
Prudhoe; the total recovery is enhanced, but rather than trying
to knock out components at the original separators.
R & R COURT REPORTERS
810 N STREET 1007 WEST THIRD AVENUE
277- 0572/F ax 274 - 8982 272 - 7515
ANCHORAGE, ALASKA 99501
ALASKA OIL AND GAS CONSERVATION COMMISSION
KUPARUK-
Public Hearing - July 20, 1995
SIGN IN PLEASE
NAME - COMPANY - PHONE
Testify/yes or no
(PLEASE PRINT)
AR(o
B?
A ONR
],3O
,,~'7o ~' cc_.
JUL-19-95 WED 17'06
Oil & Gas Operatione
909 West 9th Avenue, Re, Box 198247
Anchorage, Alast~a 99519-6247
Telephone (907) 263-7672
276-7600
Facsimile (9071 263-7628
P, O1
Christopher A. Costelloe
Asset Manager
Cook Inlet Olf~hore/Nonh Slope
Alaska
July 19, 1995
Mr. Scott I. Kerr
Manager, Kuparuk Development
ARCO Alaska, Inc.
P.O. Box 196105
Anchorage, Alaska 99519-6105
Dear Scott:
Kuparuk Unit NGL Supply In-Kind
Please be advised that Union Oil Company of California will suppy in-kind its
Kuparuk Unit LSEOR NGL needs through contractual arrangement with a
Prudhoe Bay Unit working interest owner.
Very truly yours,
Christopher A. Costelloe
Post-it' Fax Note 7671
./Dept.
...... i ...................... , ....... . ..................... , .......
Phone #
ALASKA OIL AND GAS
'CONSERVATION COMMISSION
July 11, 1995
TONY KNOWLE$, GOVERNOF~
3001 PORCUPINE DRIVE
ANCHORAGE, ALASKA 99501-3192
PHONE: (907) 279-1433
FAX: (907) 276-7542
Scott I. Kerr
Kuparuk Development
ARCO Alaska, Inc.
P.O. Box 100360
Anchorage, Alaska 99510-0360
Re: Kuparuk EOR
Dear Mr. Kerr:
The Alaska Oil and Gas Conservation Commission (AOGCC) will hold a public hearing
July 20, 1995 to examine conservation issues related to your proposal to initiate a large
scale enhanced oil recovery project in the Kupamk.River Unit (KRU). Information on
· the following topics will be helpful for our determination:
1) 'the additional recovery from KRU anticipated,
2) the scope and timing of the EOR project,
3) the proposed volumes and composition of the NGL sold to KRU,
4) the relative efficiency of the injectant as an EOR agent in the KRU as compared
to the PBU,
5) the effect of sales to KRU on recovery from PBU,
6) the effect of sales to KRU on the disposition o£NGLs from PBU.
The hearing will be held at the offices of the Alaska Oil and Gas Conservation
Commission, 3001 Porcupine Drive, Anchorage, Alaska 99501 at 9:00 AM on July 20,
1995.
Chairma :
Notice of Public Hearing
STATE OF ALASKA
Alaska Oil and Gas Conservation Commission
Re:
The application of ARCO Alaska, Inc. for approval to initiate a large scale enhanced
oil recovery project in the Kuparuk River Unit.
In an application dated June 6, 1995, ARCO Alaska; Inc. has applied to the Commission for
permission to significantly expand injection of an enhanced oil recovery solvent into the Kuparuk
River Oil Pool within the Kuparuk River Unit on the North Slope.
A person who may be harmed if the requested order is issued may file a written protest prior to
4:00 p.m. July 6, 1995, with the Alaska Oil and Gas Conservation Commission, 3001 Porcupine
Drive, Anchorage, Alaska 99501, and request a hearing on the matter. If the protest is timely
filed and raises a substantial and material issue crucial to the Commission's determination, a
hearing on the matter will be held at the above address at 9:00 a.m. on July 20 1995, in
conformance with 20 AAC 25.540. If a hearing is to be held, interested parties may confirm this
by calling the Commission's office, 907-279-1433 after July 6, 1995. 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 279-1433 no later than July 17, 1995.
Commissioner
Published June 17, 1995
914163
STOF 0330
A0-02151456
$55.O0
AFFII AVIT OF PUBLiCATiON
STATE OF ALASKA, )
THIILD JUDICIAL DISTRICT. )
Eva M. Kaufmann
being first duly sworn on oath
deposes and says that he/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
June 17, 1995
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.
Subscribed and sworn to before
Notary Public in and for
the St~te of Alaska.
Third Dfviston.
Anchorage, Alaska
MY COMMISSION EXPIRES
.~~-_~. ...... ~ .................. 19.~..7
- CLIP -
· Notice of Public Heorlng-
:::,~: STATE-OF. ALASKA.,~--:",'1
:~<;~',.Alaska. Oil.and G~s.:Tr~7~','~
.~' cO~servofion C0mmisst0n .~-'j
~..-...;, ~ ..,. ,:.: .~....5...: .~. ,..' ' '..? :'-
Alaska;: .Inc.. :for) opproval' '.~Ol
.initiate: d" Iorg~ .'scale enhanced
0il: ;recogery -Project :in". the:'l
Kuparuk' Rive~;"Unif-'.~!:i~!k-i;'.- ;["
I h{?6n ~ppllcotion .dot '.ecl~ June~:.
I ~ws, i ARCO .'Ams~P.~.'4 n.ci..;:,.~I
/ .~}l!ed lo:ll~e 'C4)lTImtsSjOn
· ,,; ?.~ 'ir.e¢.Jl'.~ GJ on i~D~*,"-.~%'-t~.
. .... k ' i~t" 0,1 P~;
bl.~.,,... R .. .
:re K,~:..:uK' Ri,er ~jp,I
::;:rlh S:ulx...j '.' ~ ~;'.""
· . ~ .' :~, ,.
' ' "" '" bi.' llgrrn¢'.':
;., Ih?r,.:n '&l':) II:CY '
· '.~ I'¢"JU~;%J~ i~,"~er i% i~.i'.:J
· . j ,. ~.,. ·
.-. i'1. '.ul¥ · ~.' .%w;:h ~.....mt ~..~
· ,,t:,;,c' O.I ----d Go:,.Ccr,JL, m,c:
:.on .~' Cnmf,~b.",~or..:"" '
· "or' ;;~1'~: l.~'",~'l', ,",ncr"'r'.:'.;"'l
qa......rq I;r I"L~ .,,",31','. · ,, .~J
' ,.",:.~.-.~t 'is" :..mew -h,,..a '.~r".a/
:..L..", ,~ ....... ,..nt:e! '.:".: .:-,.3ter~,j
...., ..,su..~ ,.r,c',:J Id the.~
-'"..,..,,,, ,:.,, , di,,i,,,.,-'..t:t,°n,.'.aJ
:'~:...:i:..,;.',.:;..:.,".~:~, .... ...hi.:
:':~ .: ¢1! I"L" ~'.:4.'.'.'"': :;,':~'gSS'Ot
,;' '. dm C: JtA'.' .':~ '"95',;inJ
Iconformance' wire, 20 '.AAC
J 25.540,. It: o hearJhg. is'.t0 be held,
j inferest~'.Porties mo,~ 'confirm'J
~ this '~ !%'/:~:Culling..- the
j sion,s'[ioffice," ~07-279-1433"ofter'J
J July ' 6;,.,.i~95. flf..:no 'protest'.,.ist
| timely., filed,.', the .con{missionq
J Will 'Co,sider'the isguance"of theJ
0rde~?~'ilh0uflb':ih~aring2('~'''~ i
/ iU.~i'~:Ore ~d:~'person"
~ ;iai.' ~iti¢Otion. 'i,:: .order..t.o,
~ comment.o.r. Ao dttend the puo.c I
J hearing,t~:13jeo{~_:~'~0nfact i;:Olanc~.l
· ' ~ i 'no':latei" than'.
Notice of Public Hearing
STATE OF ALASKA
Oil.and Gas Conservation Commission
/ko ( cc
Re: The application of ARCO Alaska, Inc. for approval to initiate a large scale
enhanced oil recovery project in the Kuparuk River Unit.
Notice is hereby given that the Alaska Oil and Gas Conservation Commission (AOGCC)
will hold a public hearing July 20, 1995 to examine conservation issues related to the
ARCO Alaska, Inc. proposal to initiate a large scale enhanced oil recovery project in the
Kuparuk River Unit (KRU). The ARCO Alaska Inc. proposal will entail the purchase of
natural gas liquid (NGL) from the Prudhoe Bay Unit (PBU) to serve as an enhanced oil
recovery (EOR) solvent in the KRU. Testimony will be sought concerning:
1) the additional recovery from KRU anticipated,
2) the scope and timing of the EOR project,
3) the proposed volumes and composition of the NGL sold to KRU,
4) the relative efficiency of the injectant as an EOR agent in the KRU as compared
to the PBU,
5) the effect of sales to KRU on recovery from PBU,
6) the effect of sales to KRU on the disposition of NGLs from PBU.
The hearing will be held at the offices of the Alaska Oil and Gas Conservation
Commission, 3001 Porcupine Drive, Anchorage, Alaska 99501 at 9:00 AM on July 20,
1995.
If you are a person with a disability who may need a special modification in order to
comment or to attend the public hearing, ploase-~ ~Ji'a'na, Fleck at 279-1433 no later
than July 17, 199~ ~~.
David ston, ( mmissioner
s wtion Commission
Published July 12, 1995
~14163
STOF 0330
AFFIDAVIT
$55.00
STATE OF ALASKA, )
THIRD JUDICIAL DISTRICT. )
Eva M. Kaufmann
being first duly sworn on oath
deposes and says that he/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
June 17, 1995
OF
,,
PUBLICATION
CLIP -
I~.','~ Notice of Public Heorlng
~.:~ STATE OF ALASKA
:~ii' ' AlaSka 011 orKI G~s
::' Conservation Commission
n.'e:The apolicalion o!
ARCO
Ioska, Inc. for approval lo
Itiate a large scale enhanced
~)11 recovery project in .the
Kuporuk River Unit.
~tlon dated June 6,
Alaska, Inc. ~has
the Commisslonr for
to slgnlficontly~ ex-
md tniecl 6n0f an enhanced
, solvent into~'the
/er OII Pool w[tllir
Rivet'Unit o~ the
if
the :;
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
individ~Js.
Subscribed and sworn to ~e~ore
me this ~.i.~. day o~.~.~.~ .....
19.~...~. .... -~ ,
· .;... .
Notary Public In and for
the State of Alaska.
Third Division.
Anchorage, Alaska
MY CONVvtlSSION EXPIRES
...... ..................
3~
SHAUN P. HOOLAHAI~,
Engineering Superviso~
ARCO Alaska, Inc.
EDUCATION
· B.S. Petroleum Engineering; Montana College of Mineral
Science and Technology; 1982
· M.S. Engineering Management; University of Alaska,
Anchorage; 1987
EMPLOYMENT HISTORY
· ARCO Alaska, Inc.
June 1982. Present
- 10/91-Present: Senior Area Engineer/Engineering Supervisor,
Kuparuk Engineering
Supervisory responsibilities covering the areas of planning, reservoir
management, and EOR. Planning responsibilities have included
preparation of the Kuparuk Five Year Plan, Unit Plan of Development,
and Long Range Plan. Reservoir management responsibilities have
included field wide surveillance. EOR responsibilities (12/92-
present) have included reservoir surveillance and management of
the Small Scale EOR (SSEOR) Pilot, initiating the Small Scale EOR
Expansion (SSEORX), Large Scale EOR (LSEOR), and immiscible water-
alternating-gas (IWAG) expansion projects. My most recent
assignment has been to supervise a multi-disciplinary engineering
group whose primary focus is the design, procurement, construction,
and start-up of the Kuparuk LSEOR and SSEORX projects.
- 6/82-10/91; Prudlaoe Bay Engineering
Advanced from Junior Engineer to Senior Area Engineer with
increasing levels of responsibility in Reservoir and Operations
Engineering groups. Junior engineer (6/82-6/83) on ARCO's one year
Engineering Development Program. Reservoir responsibilities (6/83-
9/90) were primarily focused on technical evaluations of the gas
cycling process in support of gas handling expansion projects.
Operations responsibilities (9/90-10/91) were primarily focused on
reservoir surveillance.
Exhibit 1 - Page 1
SHAUN P. HOOLAHAN
Engineering Superviso{
ARCO Alaska, Inc.
PROFESSIONAL AFFILIATIONS AND HONORS
· Member of Society ~)f Petroleum Engineers
· 95/96 Strathmore's Who's Who Registry of Business Leaders
PUBLISHED MATERIAL
· Kriel, W.A., Spence, A.P., Kolodziej, E.J., Hoolahan, S.P.:
*'Improved Gas Chromatographic Analysis of Reservoir Gas and
Condensate Samples," paper SPE 25190 presented at the 1983
SPE International Symposium on Oilfield Chemistry, New
Orleans, March 2-5.
PROFESSIONAL QUALIFICATIONS
· Alaska Registered Professional Petroleum Engineer
Exhibit 1 - Page 2
Kuparuk LSEOR Hearing
SUMMARY
EOR Process at Kuparuk Works. Verified Both in the Lab and by the
SSEOR and SSEORX Field Pilot Programs.
Expanding EOR to a Large Scale Program Fits Well into the Logical
Progression of Field Development. '
Proposed Project Maximizes Utilization of Existing Facility Infrastructure,
Resulting in a Three-Fold Increase in MI Injection Capacity.
External Enriching Fluid Needed for Major EOR Expansion.
Strongly Condensing Character of EOR Reservoir Mechanism
Well Suited to an NGL Based Solvent.
Able to Achieve Miscibility Over a Wide Range of Enriching Fluid
Compositions.
Infiil Drilling Required to Improve Reservoir Contact.
July 20, 1995 Exhibit 2A
Kuparuk LSEOR Hearing
I
BOTTOM LINE
· Expected Incremental Recovery of Over 200 MMBBL is
Significant. Ultimate Recovery is Tied to: ~
(1)
Acquisition of Approximately 100 MMSTB of NGLs within the
Anticipated Field Life;
-(2) Infiil Drilling as Outlined in the Application;
(3)
(4)
Sufficient Injection Well Capacity; and
Expansion to all the Proposed Drill Sites
July 20, 1995 Exhibit 2B
Kuparuk LSEOR Hearing
OBJECTIVES
ARCO Alaska, Inc., as KRU Operator, respectfully
requests that the Commission issue an order
authorizing the underground injection of miscible
enriched natural gas for enhanced oil recovery in the
expanded area of the proposed KRU Large Scale EOR
Project.
ARCO Alaska, Inc., as KRU Operator, respectfully
requests that the Commission endorse: 1) the areal
expansion of the enriched gas EOR process via the
proposed KRU Large Scale EOR Project and 2)
additional drilling within the EOR expansion area.
July 20, 1995 Exhibit 2C
Kuparuk LSEOR Hearing
PRESENTATION OUTLINE
Introduction/Background
July 20, 1995 Exhibit 2D
!
KRU LARGE SCALE EOR PROJECT
Schematic
PBU NGLs to Kuparuk
Oliktok Pipeline
Kuparuk Pipeline
Kuparuk
NGLs
Lean Gas
Separator
Off-Gas
SLP
Prudhoe
Bay
Miscible
Gas
O
Exhibit 2E
Kuparuk LSEOR Hearing
DEVELOPMENT HISTORY
Discovery Well Drilled
Decision to Develop
CPF-1 and 16" Pipeline Start-up
1969
1979
1981
Waterflood Start-up
1983
CPF-2 and Kuparuk Pipeline Start-up
CPF-3 Start-up
1984
1985
1986
A-Sand Refracture Program and SSEOR Start-up (1Y & 2Z)
1988
SSEOR Expansion (DS lA)
1993
July 20, 1995
Development Costs to Date 4.7 Billion Dollars
Exhibit 2F
KUPARUK RIVER UNIT
CURRENT DEVELOPMENT STATUS
(1/~/9S)
KPA BOUNDARY
[] WATERFLOOD (20)
I~! IMMISCIBLE WAG (17)
[] SMALL SCALE EOR (3)
I--]GAS STORAGE (2)
-- KPA BOUNDARY
Exhibit 2G
Kuparuk LSEOR Hearing
CURRENT COMMISSION AUTHORIZATIONS
Area Injection Order No. 2- June 6, 1986
· Authorizes Injection for Enhanced Recovery and Disposal
· Authorizes Injection into Kuparuk and West Sak Reservoirs
within Boundaries of Kuparuk River Unit
Conservation Order 198.3-June 3, 1987
· Approves Small Scale EOR Project and Expansion
- Original Project: 1Y & 2Z
- Expansion: lA, 1F, 1G, lQ, 2C, 2D, 2W, & 2X
July 20, 1995
Exhibit 2H
Kuparuk LSEOR Hearing
EOR PROGRESSION
EOR Pilot is Successful
Verification of EOR Process via Original Pilot Program
(DS-1Y&2Z)
Pilot Expansion to Test MWAG after IWAG Process
(DS-lA)
Logical Next Step
Expansion Opportunities Limited with Indigenous Solvent
External Enriching Fluid Needed for Significant Expansion
Key Scope Considerations
July 20, 1995
Existing Infrastructure
Solvent Availability
Kuparuk Field Life
Reservoir Performance
Exhibit 21
Kuparuk LSEOR Hearing
PRESENTATION OUTLINE
~n
I1.
Pilot Performance
~¥o
July 20, 1995 Exhibit 2J
Kuparuk LSEOR Hearing
SSEOR PILOT PERFORMANCE
(Drill Sites 1Y & 2Z)
15-20 MMBBL Incremental EOR Oil to Date
(3.5-5 %OOIP)
30-40 MMBBL Incremental EOR Oil Ultimately Expected
(7-10 %OOIP)
July 20, 1995 Exhibit 2K
Original MI Injection Patterns
Drill Site 1Y EOR Region
1Q.436
1%23
·
1%05
2Z-20
2Z-21 · 1%24
1Y-34
100,000
Decline Curve Analysis
Drill Site 1Y EOR Region
Incremental Oil due
Oil Rate ~ Start MI / to EOR
(BOPD)I Injection /
lO,OOO
Incremental Oil
due to Infill Drilling
1,000
1987 1988 1989 1990 1991 1992 1993 1994 1995
Year
1996
Exhibit 2L
Original MI Injection Patterns
Drill Site 2Z EOR Region
2Z-20 1 Y-24
2Z-21 ·
2Z--05
2Z-16 2Z-.04 2Z-09 ·
2Z-22
2Z-19 2Z-18
2Z-03 2Z-15 2Z-08 2Z-10
2Z-23 A A A r~l~-...~
· , ..;.;.;.;,;.;.;.:.........,...........;.:.:.:.;.;.;.;.;.;.;.:.;i~
.L'C~O..9 :.:. :.:. ·........ :... :. :.~ 0~.:.:.:.:.:.:.:.:.:.:.:.:.:.:.:.:.,i
): · :. :. :. :.'.2Z;-1.4: ':': ·: ':': ': · ' · ': ': ': ': ': ' ~7~-~'.1': ': ': ': ·: ': :,~_'~-~
..,...,... :...,.:.;. :. :. :. :. ;.:21 i.;.:.:.:.:.:.....:. :.;. :.:.:. ~.~_~,.
,.:.:.:.:.:.:.~.:.:.:.:.:.:.:.: :. :.:. :.:, :. :.,A,; :.:. :. :. :,,.:.:. ;.·:
::::::. ~.i..'..',i/.,i:i':'.' ............
~: i~':::: :' :' :' :~z.~2:. :. :. :. :. :. :. :. :. :. :. :. :. :.'.'.'.'.'.'.'.' '
.:..'-===============================================================
:::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::: ·
.:.:.:.:.:.:.;.:.:.:.:.:.:.:.;.:.'.:.:.:.:.:.:.:.;...:.:.;.:.:.:.:.:
10,000
Oil Rate
(BOPO)
Decline Curve Analysis
Drill Site 2Z EOR Region
Start of
· · IncrementmlOil
MI Inject;on. ~,._ due to EOR
due to Well Work
1,000 i,, . ·
1987 1988 1989 1990 1991 1992 1993 1994 1995 1998
Year
Exhibit 2M
Initial MI Injection Patterns
Drill Site lA EOR Region
1A-02
1Y-:34
1A-19
1A,-23
1A.03
:::::::::::::::::: :::::::::::::::::::::::
:::::::::::::::::' :::::::::::::::::::::::
::::::::::::::::: ::::::::::::::::::::::::
~':':':':':': i:i:i:i:i:i:i:i:i:i:i:i:
:. :. :. :. :. :. :. :.: .~4 '
..... i:i:i:i:i:i:i:i:i:i~!'
1A.05
1A-12
1A.25
1A-10 1A-07 1A-06 1A-11
1A-20
10,000 -~
Oil Rate
(BOPD)
Preliminary Decline Curve Analysis
Drill Site lA EOR Region
Start of M!
Injection
Incremental Oil
due to EOR
1,000 ,
1992 1993 1994 1995
Year
1996
Exhibit 2N
EOR Dimensionless Curve
(DS-2Z C-Sand Performance vs. Simulation)
>
0
15
10
0
0.0
Waterflood Acceleration
Ultimate EOR
Additional Recovery
WAG RATIO 1:1
30% GAS SLUG SIZE CASE
El SIMULATION
· FIELD DATA
0.5 1.0 1.5 2.0
MI + Water Injection
(%HCPV)
Exhibit 20
Kuparuk LSEOR Hearing
Summary of Laboratory Program
· Extensive Experimental Analysis
- In Excess of 75 Experiments over a Ten Year Period
- Ranging from Static PVT to Sophisticated Flow Experiments
· Benefits:
- Insight into
- Confidence
Miscible Gas Process at Kuparuk
in Simulation Results
· Applications:
- Predict EOR Performance
Establish Level
Composition
of Enrichment for a given Enriching Fluid
July 20, 1995 Exhibit 2P
Kuparuk LSEOR Hearing
PRESENTATION OUTLINE
I][Io
Iil.
Project Definition
July 20, 1995
Exhibit 2Q
Kuparuk LSEOR Hearing
LARGE SCALE EXPANSION OF KUPARUK EOR
Requires Outside Enriching Fluid
- Only 2-5 Drill Sites Beyond lA, 1Y, & 2Z can be Flooded with
Indigenous Kuparuk MI
- Currently Using all MI Kuparuk can Make.
Key Enriching Fluid Criteria:
- Immediately Available
- Significant Quantity (Expected to be 20-30 MBPD)
- Contains Minimal CO2 (< 1 mole %)
LSEOR Project has been Sized to Flood all Existing IWAG Drill Sites
with MI within Kuparuk's Anticipated Life
Minimizes New Facility Investments
Maximizes Project's Economic Efficiency
Expands the Ultimate MWAG Area to 21 Drill Sites
Assuming 20-30 MBPD PBU NGLs are Imported and
an Additional Pump is Installed, MI Injection Capacity Increases
More than Three-Fold
July 20, 1995 Exhibit 2R
KUPARUK RIVER UNIT
FUTURE DEVELOPMENT WITH LSEOR
KPA BOUNDARY
· WATERFLOOD (19)
~-I GAS STORAGE (2)
~ KUPARUK EOR (21)
~ APPROVED FOR MI INJECTION BY
ADMINISTRATIVE APPROVAL NO. 198.3
~ KPA BOUNDARY
Exhibit 2S
Kuparuk LSEOR Hearing
LSEOR EVALUATION METHODOLOGY
Incremental Oil Recovery and Returned MI Rates Based on Reservoir
Simulation Tuned to SSEOR Performance ~
Each Drill Site's MI I'njection Rate Based on Historical IWAG Data
- Adjustments Made for Future Infill Wells and Expected WAG
Ratios
Scale-up Tool Calculates the Project Rate Profiles Based on:
- Generalized ("dimensionless") Recovery Curves
- Drill Site Specific MI Injection Rates
- Drill Site Pore Volumes
- Projected MWAG Expansion Sequence
July 20, 1995 Exhibit 2T
LSEOR "Type'" Curves
12.00%
10.00%
8.00%
6.00%
4.00%
2.00%
0.00%
O%
--e-- A-Sand Recoveq/
~ C-Sand Recove~j
10% 20% 30% 40% 50%
MI Slug Size
(%HCPV)
Exhibit 2U
Kuparuk LSEOR Hearing
LSEOR PROCESS EFFICIENCY
Over 200 MMBBL Anticipated Incremental Oil Recovery due to
Indigenous Enriching Fluid plus Approximately 100 MMBBL of
Imported PBU NGLs
180 MMBBL Anticipated Incremental Oil Recovery Attributed to
PBU NGLs
Ultimate Recovery Directly Linked to Cumulative Volume of
NGL Import
As a Consequence of the EOR Process, Approximately 1/3 of
Imported PBU NGLs Expected to Stabilize out of the Returned
MI and be Exported with Kuparuk Crude
Gross Solvent Utilization of PBU NGL 4.6 MSCF of MI Injected per BBL of Oil Recovered
1.3 BBL of Oil Recovered per BBL of NGLs Injected
July 20, 1995 Exhibit 2V
Kuparuk LSEOR Hearing
INFILL DRILLING
Primary Focus of Infill Drilling Program
Under-Performing Patterns
Areas of Partial or Total Structural Isolation
EOR Benefits of Infili Drilling
Infill Drilling will Provide Incremental Tertiary Reserves by
Providing a Means for MI to Contact Additional Pore
Volume
July 20, 1995
Exhibit 2W
·
1~'-412 ~l~4J,1 ·
, .".. "
,~-~ ,....~
~..?
.
, ~ '2. '.'~
CURRENT ENRICHED GAS EOR PROJECT AREA
;ED LARGE SCALE EOR PROJECT AREA
ProP°s'~l' W'~J-l-S--~Vi~'hin i-",~E-(3R Area: 13 Peripheral
19 Pattern Infiil
34 Structural Infiil
STRTUTE MILES 0 1 2 STRTUTE MILES
FEET 0 10000 20000 FEET
KUPRRUK RIVER FIELD
TOP KUPRRUK WELL LOCRTIONS
FOR EXISTING RNO PROPOSED WELLS
Exhibit 2X
OF KUPARUK FAULT MAP
ExhibH: 2Y
Kuparuk LSEOR Hearing
LSEOR FACILITY SCOPE
Project Design Maximizes Utilization of Existing Infrastructure - Existing IWAG Infrastructure to be used for. MI Distribution
- Oliktok Pipeline (Currently Idle) to be used for PBU NGL Transportation
- Existing SSEOR and SSEORX Facilities will be Integral to the Project
+NGL Injection Pump at CPF-1
+MI Tie-Line between CPF-1 & CPF-2
+Enriching Fluid Collection Systems at CPF-1 & CPF-2
Overview of LSEOR Facilities - Re-Commission Oliktok Pipeline to Transport PBU NGLs from Skid 50 to CPF-1
- Install NGL Pipeline Pumps at CPF-1
- Install Tie-Line to TranSport PBU NGLs from CPF-1 to CPF-2
- Install Receiving Vessels at CPF-1 & CPF-2 to COmmingle KRU
Enriching Fluid and PBU NGLs
- Upgrade SSEORX Injection Pump at CPF-1
- Replace Injection Pump at CPF-2
- Link Electrical Distribution Systems between CPF-1 & CPF-3
- Surface Facilities for EOR Infill Wells
July 20, 1995 Exhibit 2Z
LSEOR Facility Schematic
CPF-2
EFfmm
CPF-i
\D~-IR ta~KV
DS-IH
CPF-1
I-
Kuparuk
E~
Exhibit 2AA
Kuparuk LSEOR Hearing
LSEOR Implementation Schedule
· November 1995 Partial Start-Up
CPF-1 Injection Pump
- Import 2-4 MBPD of PBU NGLs
- MI Injection Capacity = 90 MMSCFD
- 2 or 3 Current IWAG Drill Sites will be Converted to MWAG
Commission the Oliktok Pipeline, Pipeline Pumps, and Upgraded
· First Quarter 1996 CPF-2 EOR Facility Shutdown - Remove'and Replace the CPF-2 Injection Pump
- Continue Importing 2-4 MBPD of PBU NGLs
- MI Injection Capacity = 65 MMSCFD
· Full Project Start-Up by Late 1996
- Commission New CPF-2 Injection PumP & NGL Tie-Line
- Import 20-30 MBPD of PBU NGLs (25 MBPD Annual Avg.)
- MI Injection Capacity = 220 MMSCFD
- 7-10 Additional Drill Sites will be Converted to MWAG
· As MWAG Patterns Mature, Remaining IWAG Drill Sites will be
Converted to MWAG
July 20, 1995 Exhibit 2BB
Kuparuk LSEOR Hearing
LSEOR OPERATION
Monitor:
MMP characteristics of MI
+ Gas, Enriching Fluid, and MI Compositions
+ Reservoir Pressures and Temperatures in EOR Regions
EOR performance
+ Produced Oil & Gas Rates and Compositions.
+ EOR Pattern Maturities (Cumulative MI Injected)
+ EOR Pattern Efficiencies (% Returned MI)
MI distribution among sand layers
+ Spinner Data
+ Single Zone Flow Tests
Control:
- MI Enrichment to Maximize EOR Benefits while Minimizing NGL
Imports
WAG Ratios and MI Slug Sizes to Maximize Economic Recovery
from Entire Project Area
July 20, 1995 Exhibit 2CC
Kuparuk LSEOR Hearing
PRESENTATION OUTLINE
}[3
IV.
Requested Hearing Topics
~n
July 20, 1995 Exhibit 2DD
Kuparuk LSEOR Hearing
PRESENTATION OUTLINE
~n
·
Vm
July 20, 1995
Findings and Conclusions
Exhibit 2EE
Kuparuk LSEOR Hearing
FINDINGS AND CONCLUSIONS
LSEOR Application Proposed Finding Number 9:
Expected Incremental Recovery of
Significant. Ultimate Recovery is Tied to:
Over 200
MMBBL, is
(1) Acquisition of Approximately 100MMSTB of
NGLs within the Anticipated Field Life;
(2)
(3)
(4)
Infill Drilling as Outlined in the Application;
Sufficient Injection Well Capacity; and
Expansion to all the Proposed Drill Sites
Proposed Findings as Outlined in Application
Recommended Conclusions as Outlined in Application
Injection Order
Project Endorsement
- Areal Expansion of MI Injection
- Infill Drilling within EOR Areas
July 20, 1995 Exhibit 2FF
Kuparuk LSEOR Hearing
DATA GATHERED TO ASSESS KUPARUK EOR
DATA TYPES
NUMBER OF
EXPERIMENTS
Saturation Pressures, Saturation
Temperatures, Densities
12
Injectant Properties
14
Single Cell Solvent/Oil Contacts
· Swelling
· Titration
· Single Contacts
· Multiple Contacts
3
6
21
3'
Solvent Displacement
· Slim Tube 12b
· Core Floods 2
· Micromodel 2
One Experiment is Underway
One Experiment Planned for This Quarter
UTILITY
Black Oil Endpoint; Correct Component Volatility
Proper Phase Behavior after Injection; Ensure
Single Phase when Injected
Examine Condensing Mechanism
Examine Vaporization Mechanism
Tune to Specific Conditions; Viscosities
Extension of Single Contact Utility
Low Dispersion; Multi-Contact Miscibility
Higher Dispersion; Multi-Contact Miscibility
Visual Observation of Miscible Process
July 20, 1995 Exhibit 3A
Kuparuk LSEOR Hearing
VALIDATION OF GAS EOR PREDICTION TOOLS
MECHANISM
Interphase partitioning
Fluid Movement
· Densities
· Saturations
· Viscosities
In!ectant
· Target Composition
All Above Processes
TOOLS
DATA USED FOR TOOL VALIDATION
Single
Fluid Cell ' Slim Tube
Properties Contacts Displacements
EOS Characterization
EOS Characterization
Rel Perm Model
Viscosity Correlation
MMP Correlation
Reservoir Simulation
Rel Perm
Measurements
' Field
Performance
Data
July 20, 1995
Exhibit 3B
Kuparuk LSEOR Hearing
~nriched Fluid
SLIM TUBE DISPLACEMENTS
Oil + Gas
Objectives
For a Given Injectant, Record oil recovery at 1.2 pore volumes injected
· Determine MMP: Vary pressure at constant injectant composition
· Determine MME: Vary injectant enrichment at constant pressure
Utility
· Demonstrate that for a given injectant, maximum recovery can' be achieved
· Validate EOS characterization for use in simulation studies
· Validate MMP correlation for use in determining target Injectant
composition
July 20, 1995
Exhibit 3C
Siimtube Displacements
For a Variety of Solvents
8O
7O
60
50
o
fi 4O
uJ
~ 30
2O
10
Experimental
4500
Slimtube Series
MME [] Predicted MME [] Experimental MMP [] Predicted
4OO0
3500
3000
2500
2000
1500
1000
500
MMPI
Series Number 7 is most relevant because a synthetic PBU NGL enriching fluid was used.
Expected variations in PBU compositions are significantly smaller than the variations in composition studied in the
laboratory. Thus, the target enrichment level can be determined for expected variations in PBU NGL compositions.
Exhibit 3D
Effect of Enrichment Level
$1irntube Experiment Number ?
100
~ 90
7o
~ 60
~ ~o
3O
;?./~f;..__': .;-. ;.: ~..~-:_,..:.:':.-~ '..::~:~.:, i:-...?F..:_:'.:::,:_:.?'..z-:,..?..=..".~:,.. .._.. :- ;...,: -.-_ .:-_...-:: :'..~:.__ ..:_,__::...~":".,!::.-:.~::'...:::.,:~: -..,_-
-.-'--:..-';'"" ...... "--~ ..". - ":_~; '.~--.:'~1- ~ - -. '. - '::-' '--":_--'-'. '-.-'~:"-"~-" '='..-'
?~?!;":'~?%'"ii:"-'.-: :;~:i.;;..~;`:..~:...~.~.~..:z~:`~i~.~i;:;~.~:~.~.......i;:;...~i.~..:...~;!-~:-'- ? i:ll ovel of enrichment ll
:.:-'-'.':.;.~;'..:.'27'.;"-.'.:~';';'_-:._-'"-;'.=A?.":..."-'.';--;' ?--:/'."-'.:~ ~?'.'--._; '.. ;.".)":'.'-. ~'"-: -~ : '
~;}~-E----;-';_~}~:~:.~':i:::_:)-~.~:.-_-;:-_;-:! ]required to recover Il
---.~-,.:,~:~.,..,, ~_.-,~,.. ......... .,.::,:~:......._,..-.:,.::~:::,::.:-:,.-~-_;. ,..-.- - .. .. l i maxlmurn amount of
-.-:..;.--'¢¢~ ._-'-~¥.~--_.:.:_:.:-:_::'.,- ~-~-z'-:,-;:-:-~;-.~_?_~-~;.::~.:-z. ~-:.' .;/' '_/-:'-.-.. '---_-,- ..... . _,.,~., -
._:_.~--~?_-...'~-.::.E _~:;2.-;-:-::.-;:~ ~4,C~-:'.-:'.'.' i~::," ..-."-_';~;... ~-,-'. ~ ;. -~.,:"-:'-':.-- -' ~.-'"'_:-' :':.-'-3 ..:.--:_-:?,- ?;:~::~---:.~::.'-:::'-' ~ !
z-:;.';:'-;."~:::~:-'.- ~ ;.:._;~Y'~;~.:.:./.'.'-:._.;~.~';.--~_:...':?"--...' '.:..:.. '. '..-' - - ' ::. ~ -. -:.-:':-- . '..- .':~':: ./-'-:_ ": 'G-.- ~.
: ~'"' ~':c:~:-'-';~::~~ ~'~";~-:'~'-::::'-~-":"---:':'~ ! :~ :':--?~':::'::- -:~' "-"~/:::"~'-'-'::-"e~::"--'-~-z'::-::';:'--"--":-1
; :-- i '_ 'i; - ~-' _'- ~-:"_~' --:',, _:---':_"~;:E -~' -C i _:' · '..' ~ - - ~' --~ · ' ':' ~, -' ' ~": '--i ~': ~," . I
10 15 20 25 30
Injectant Enrichment Level (mole %)
· Enrichment above MME does not increase recovery
· Recovery is not significantly sensitive to' enrichment level
slightly below the MME
Exhibit 3E
Minimum Miscibility Correlation
Applied in Field
Relates oil and Injectant properties to minimum pressure required to achieve maximum recovery
from slimtube experiments
Fit t¢ $!imtlJbe exr~eriment$
· average error is 140 psi (experimental error is 200 Psi)
Applied to CPF1 and CPF2 Anticipated Injectant Compositions:
25%
24%
23%
22°/0
21%
20%
MMP
:~_-:':.:"-~ '._'-: -: 4/ '-~.-'-'-~:~' ' ,-.:-_-'-:~..":':?.:'.',,-~: ~F-": ': .- '-~'- '~'~ '-'.:"_ - -'?'; ...... "'"~:'":" ............ -- '-:'---b~
:=~.:,,.~::~:.:..,.'.~.--':-:..~ -_ .~:._:..'....~ .- .'!:~ :'..:.y'..--.-:.?!._,--.:-..-~[ '. :: - _:.. _:._-'.. ': ....'.-::.. ....~..::
:4 ~ . · -. ..................... "'.'-' .
~-:-~!~-:-:.-.i.:-_:_~i ~ ~.,_-~i~-.'-_'.!:.-'-'-:'~,:~. !.'-~--:.~?:-~..~-ii-.'-:-'-~.'~- ',!~-,~-~'.'-'-'?-~ '-~:;:."' ~'-."' ' ' CPF2
· -~_:--. -~_,. _~ - -~.~,~ ~ ~P - ~..__ --.. ;~,-~_... --...~-.~---..
' :-'-:;'~- :~-:.'-"~"-:--":::'~X".~:-:-
~ '.-:.':.,.:'--'.'.:"'.-'_:-'.-'-?.:"
,.'.2.-:-~?_:'.:~.?-.~',--x'.:.~-'-. - t:.- '-.:-.:..:-.~'-':-: :-:[:--.'.:,'~'.: -..:/-.,':-.::.:-).:~.'-..~.'..~.. '-. :.'..- i '-...-..:-... :._._.-:- --.-...~_-::: .._' ..._.'_r....-....: .... - ~ ~~ :?.:..;.._...._..~:.-.:_.:.. ~-.;-...
............... '.~/..7,~x/,,~
': ~:'.:~47~-~':--:.~-.:L~--:~----~_~..:'-~_'_-.:-~.::_--'--t.:~:~,--'.. . --..~:.~:.:_..~F.':-::/,~-:.~_i._'.~-...._-.._:.,_. :.:..:..: :-:..?-ii~ -'-'- .
. : - -. :-,.-,----.:-:-:.- -:-: - --,
..-.-_-....:-.:.:.:~ i-!_._ '-?.: ;-_.
.-~_,,---:~'-'_,~'--'--:'.i,_-, '~-'-~--:,.-':-',: ','_:',_' .--~-~ ---:,-'-.-_. :,'- :--,:_-, ,.-'_,'- _, . '-,' -,_
2700 2750 2800. 2850 2900 2950 3000 3050 3100
Pressure (psig)
Exhibit 3F
Kuparuk Injectant/Oil System is a Condensing/Vaporizing System
With a Pronounced Condensing Component
Single Cell Multi-Contacts for Miscible Systems
2.5
o 2.0
.il
0.5
0.0
~Preliminary Results from~
~ Kuparuk Multi-Contact
~ ~~ ~_xperiment '
II_.L._ I
0 5 10 15 20 25 30 35 40
Injected Pore Volumes of Miscible Injectant
Exhibit 3G
REQUESTED
HEARING TOPICS
On June 7, 1995, ARCO Alaska, Inc. ("ARCO"), as Operator and on behalf
of Kuparuk River Unit Wor.king Interest Owners, filed an Application for Injection
for the Kuparuk River Unit Large Scale EOR Project. By public notice and by
letter dated July 11, 1995, the Commission indicated that information on six
topics would be helpful at the public hearing scheduled for July 20, 1995.
At least three of the indicated topics pertain to Prudhoe Bay Unit NGL
production and recovery issues (Topics 4-6). ARCO, as Operator to the Eastem
Operating Area of the Prudhoe Bay Unit, and BP Exploration (Alaska) Inc.
...... ("BP"), as Operator of the Western Operating Area of the Prudhoe Bay Unit, are
in a better position to respond to Topics 4-6. Therefore, the Working Interest
Owners of the Kuparuk River Unit ("KRU") have consulted with the Prudhoe Bay
Operators for information relating to Topics 4-6.
Q 1: What is the additional recovery from KRU anticipated?
A-'
As stated in the Application for Injection, incremental oil recovery from the
18 additional LSEOR drill sites is expected to range from 4% to 10% of
the Odginal Oil in Place, resulting in over 200 MMSTB of additional
Kuparuk oil reserves. Recovery of these reserves, pursuant to the
LSEOR Project plan, is conditioned upon: (1) the acquisition of
approximately 100 MMSTB of NGLs within the anticipated field life; (2)
infill drilling as outlined in the application; (3) sufficient injection well
capacity; and (4) expansion to all the proposed drill sites. In addition to
the incremental oil recovery described above, approximately one-third of
the acquired NGLs are expected to stabilize out of the returned MI and be
exported as part of the Kuparuk crude stream.
The NGL injection rate will affect the timing of recovery, but will not affect
the amount of additional reserves recovered, provided that the above
conditions are met.
Exhibit 4 - Page 1
Q 2: What is the scope and timing of the EOR project?
A:
Scope.
The LSEOR Project. will significantly expand the Small Scale EOR
("SSEOR") Project beyond Ddil Sites lA, 1Y, and 2Z, and is designed to
ultimately cover 18 additional KRU drill sites. NGLs from Prudhoe Bay
will be combined with Kuparuk enriching fluids and blended with
Kuparuk lean gas for injection as MI. Specifically, the planned LSEOR
Project involves expansion of the enriched gas EOR process beyond Drill
Sites lA, 1Y, and 2Z to Drill Sites 1 F, 1 G, 1 Q, 1 R, 2A, 2B, 2C, 2D, 2F, 2G,
2H, 2K, 2M, 2T, 2U, 2V, 2W, and 2X.
Basis for Scope.
The scope of the LSEOR Project is dictated by a number of factors,
including existing infrastructure, anticipated field life, MI slug size,
reservoir performance, and availability of solvent. In order to maximize
economic recovery and minimize investment risk, the LSEOR Project is
designed to fully utilize the existing Kuparuk IWAG infrastructure. Thus,
the Project contemplates relatively few additional facilities.
The existing IWAG infrastructure can support expansion up to 18
additional drill sites. Reservoir modeling and the SSEOR Project show
that the optimum MI slug size is 20% to 30% of a given drill site's
hydrocarbon pore volume. In order to flood 18 additional drill sites with
the optimum MI slug, approximately one trillion SCF of MI will be required
over the life of the LSEOR Project. This is expected to produce an
additional 200 MMSTB of EOR oil. To reasonably ensure this recovery
within the expected remaining life of the Kuparuk River Field, the
injection of the I TCF of MI is planned to be completed within 15 to 20
years of Project start-up.
The 1 TCF of MI will be comprised of outside enriching fluid, indigenous
Kuparuk enriching fluid, and indigenous Kuparuk lean gas. As stated
previously, the KRU Working Interest Owners currently plan to use
Prudhoe Bay NGLs as the outside enriching fluid. Over the life of the
Project, approximately 100 MMSTB of Prudhoe Bay NGLs will need to be
Exhibit 4- Page 2
blended with indigenous Kuparuk enriching fluid to produce 1 TCF of MI
at Kuparuk. Expected recovery from the Project can be achieved,
notwithstanding reasonable variations in the rate of Prudhoe Bay NGL
deliveries, so long as the 100 MMSTB of Prudhoe Bay NGLs are injected
within the life of the Project.
Timing,
The SSEOR Project was approved by the Commission in June 1987,
and miscible enriched gas EOR operations have been conducted in
several patterns at Drill Sites at lA, 1Y, and 2Z since that date. Due to
the success of the SSEOR Project, the LSEOR Project was approved by
the Working Interest Owners of the KRU in March 1995. Start-up of the
facilities integral to this project is scheduled to begin on or about
November 1, 1995 and to be completed by late 1996. Upon completion
of start-up, 12 to 15 Kuparuk drill sites (including lA, 1Y, and 2Z) will be
flooded with MI. The remaining six to nine planned EOR drill sites will
commence MI injection as mature EOR patterns are converted back to
water or lean gas injection. The expected duration of the LSEOR Project
is 15 to 20 years.
Exhibit 4- Page 3
Q 3:
What are the proposed volumes and composition of the NGL
sold to KRU?
A-'
Preliminarily, it shou..Id be noted that the Prudhoe Bay Unit will not be
"selling" NGLs to the Kuparuk River Unit. The Prudhoe Bay Unit is not a
business entity capable of selling NGLs as a Unit. Although ARco, as
Operator of the Kuparuk River Unit, is authorized under the Kuparuk
River Unit Operating Agreement to purchase materials on behalf of the
Kuparuk Working Interest Owners for use in Kuparuk River Unit
operations, all the Kuparuk River Unit Working Interest Owners have
elected to supply NGLs to the LSEOR Project in kind.
The LSEOR Project is expected to acquire 100 MMSTB of NGLs from
Prudhoe Bay during the expected 15 to 20 year life of the project.
Consistent with the Project scope as described above, the KRU currently
plans to acquire up to 26 MBPD upon completion of start-up activities in
1996. This rate will decline over time as the volume of retumed MI
increases.
The MI used in the LSEOR Project will be comprised of Prudhoe Bay
NGLs, indigenous Kuparuk enriching fluid, and indigenous Kuparuk lean
gas. The composition of Prudhoe Bay NGLs will vary depending on
actual CGF operating conditions. The Kuparuk enriching fluid is
comprised of several light hydrocarbon streams produced by the KRU
facilities. Specifically, the CPF-1 enriching fluid is comprised of scrubber
liquids from the CPF-1 artificial lift gas compression system, NGLs from
the CPF-1 NGL plant, and naphtha from the Kuparuk River Unit Topping
Plant. The CPF-2 enriching fluid is comprised of scrubber liquids from
the CPF-2 artificial lift gas compression system and NGLs from the CPF-
2 fuel gas stripping unit. Laboratory core flood experiments indicate that
MI with these constituents is fully compatible with the Kuparuk River
Formation.
Based on the results of experiments, simulation studies, and the SSEOR
Project, the LSEOR Project is expected to have sufficient flexibility to
handle reasonable variations in enriching fluid volume and composition.
Exhibit 4- Page 4
Q 4:
A'-
What is the relative efficiency of the injectant as an EOR
agent in the KRU as compared to the PBU?
·
· The Kuparuk LSEOR Project is expected to recover an average of 1.3
barrels of incremental EOR oil for each barrel of Prudhoe Bay NGL
injected.
With respect to Prudhoe Bay, the Prudhoe Bay Operators presented
different values to the Commission as part of the recent Phase I Prudhoe
Bay hearings. ARCO's base case for Prudhoe was an average of 0.3
barrels of incremental EOR oil for each barrel of NGL injected. BP's base
case for Prudhoe was an average 0.6 barrels of incremental EOR oil for
each barrel of NGL injected.
There are a number of generic reasons why the efficiency of EOR
projects will vary from reservoir to reservoir. The Kuparuk efficiency is
expected to be above Prudhoe's for the following reasons: (1) the
Kuparuk flood is less mature than the Prudhoe flood (i.e., starting at the
front end of the recovery curve); (2) the Kuparuk reservoir is thinner than
Prudhoe's (i.e., less gravity override); (3) Kuparuk has a higher target
residual oil saturation following waterflood than Prudhoe; and (4)
Kuparuk is able to make more SCF of MI per barrel of NGL because the
Kuparuk reservoir temperature is lower than Prudhoe's, the NGLs will be
blended into "richer" lean gas at Kuparuk, and the reservoir fluid
characteristics are different.
Exhibit 4- Page 5
Q5: What is the effect of sales to KRU on recovery from PBU?
A.'
None. NGLs fOr the Kuparuk LSEOR Project are those that would have
otherwise been transported down TAPS. As such, the NGLs are being
removed "downstream" of the Prudhoe recovery system.
*Q6:
What is the effect of sales to KRU on the disposition of NGLs
from PBU?
A.'
Because NGLs for the Kuparuk LSEOR Project are those that would have
otherwise been transported down TAPS, there will be a reduction in the
volume of NGLs transported down TAPS. In addition, there could be tadff
impacts due to differences in throughput, QualitY Bank, and Pumpability.
Exhibit 4- Page 6
ARCO Alaska, Inc.'
Post Office Box 100360
Anchorage, Alaska 99510-0360
Telephone 907 276 1215
Scott I. Kerr
Manager
Kuparuk Development
263-4348
June 6, 1995
Mr. David W. Johnston
Chairman
Alaska Oil and Gas Conservation Commission
3001 Porcupine Drive
Anchorage, AK 99501
Dear Mr. Johnston:
Enclosed is the Kuparuk River Unit (KRU) Large Scale Enhanced Oil
Recovery (LSEOR) Project Application for Injection. The application was
prepared in accordance 'with 20 AAC 25.402 (Enhanced Recovery
Operations) and Area Injection Order No. 2, issued June 6, 1986. ARCO
Alaska, Inc., as Operator of the KRU, seeks Commission endorsement and
authorization for the proposed significant expansion of the KRU Enriched Gas
EOR Project, which is currently active at Drill Sites lA, 1Y, and 2Z.
In the event that a public hearing is held under 20 AAC 25.540, we request
that it be scheduled to commence between July 10, 1995 and July 21, 1995.
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 S. P. Hoolahan (263-4238) or G. S. McDuffie (265-1634) if you
have any questions or require additional information.
Sincerely,
~ott I. Kerr
SIK/GSM:tg
enclosure
Mr. Brad Berg
Mr. Ken Boyd
Mr. Jerry Brossia
Mr. Don Puckett
Mr. Ron Swanson
Ms. Nancy Welch
Kuparuk Pipeline Company
Alaska DNR
Alaska DNR
Oliktok Pipeline Company
Alaska DNR
Alaska DNR
R .C IV[D
.,JUN -7 1995
Gas cons. commission
ARCO Alaska, Inc. i~ · ,~JbekllaW of Atla~ttcRioh~eldCompany
KUPARUK RIVER UNIT
LARGE SCALE EOR PROJECT
Application for Injection
June 6, 1995
RECEIVED
JUN -7 1995
Alask~ 0il .& Gas Cons. Commission
· ~chorage
Reference
20 AAC.25.402(c)(1)
20 AAC.25.402(c)(2)
20 AAC.25.402(c)(3)
20 AAC.25.402(c)(4)
20 AAC.25.402(c)(5)
20 AAC.25.402(c)(6)
20 AAC.25.402(c)(-7)
20 AAC.25.402(c)(8)
20 AAC.25.402(c)(9)
20 AAC.25.402(c)(10)
20 AAC.25.402(c)(11)
20 AAC.25.402(c)(12)
20 AAC.25.402(c)(13)
20 AAC.25.402(c)(14)
TABLE OF CONTENTS
Subject
Introduction
Plat of Project Area
Operator & Surface Owners
Affidavit
Project Description
Pool Description
Formation Geology
Injection Well Logs
Injection Well Casing Description
Injection Fluids
Injection Pressures
No Fracture Propagation
Formation Water Analysis
Freshwater Exemption
Incremental Hydrocarbon Recovery
Proposed Findings
Recommended Conclusions
Requested Decisions
Page
4
10
10
10
10
11
12
12
KRU LSEOR Project Application -2-
Exhibit 1 '
Exhibit 2
Exhibit 3
Exhibit 4
Exhibit 5
Exhibit 6
Exhibit 7
Exhibit 8
LIST OF EXHIBITS
Plat of the Kuparuk River Unit '
Affidavit & List of Surface Owners
LSEOR Project Schematic
Type Log - West Sak River State No. 1
Stratigraphy - Kuparuk River Formation
Injection Wellbore Schematic
Miscible Injectant Compositions
Water Analyses
KRU LSEOR Project Application
Introduction
This application seeks Alaska Oil and Gas Conservation Commission
(Commission) authorization and endorsement of the proposed Kuparuk River
Unit (KRU) Large Scale Enhanced Oil Recovery (LSEOR) Project. This
application has been prepared in accordance with 20 AAC 25.402 (Enhanced
Recovery Operations) and Area Injection Order No. 2, issued June 6, 1986.
The LSEOR Project is a significant expansion of the KRU Enriched Gas EOR
Project which waS approved by the Commission in June 1987 and was initiated
in several patterns at Drill Sites 1Y and 2Z in 1988. Consistent with the
Commission's Administrative Approval No. 198.3, the original KRU Enriched
Gas EOR Project was expanded to the remaining patterns at Drill Sites 1Y and
2Z in 1991 and to Drill Site lA in 1993. The enriched gas EOR process would
likely be expanded to at least two additional Kuparuk drill sites within the
expected field life even if the LSEOR Project were not implemented.
Whereas the scope of the approved KRU Enriched Gas EOR Project is limited
by the volume of Miscible Injectant (MI) which can be manufactured from
enriching fluids indigenous to the Kuparuk River Oil Pool, the LSEOR Project
involves the acquisition of Natural Gas Liquids (NGLs) from the Prudhoe Bay
field. Such NGLs will be transported to the Kuparuk River Field via the Oliktok
Pipeline, mixed with Kuparuk enriching fluid, pumped to injection pressure,
blended with Kuparuk produced gas at Central Production Facilities No. 1 and 2
(CPF-1 and CPF-2), and distributed as MI to a total of 21 Kuparuk EOR drill
sites, including those within the current KRU Enriched Gas EOR Project.
The LSEOR Project was approved by the Working Interest Owners of the KRU in
March 1995. Start-up of the facilities integral to this project is scheduled to
begin in late 1995 and to be completed by late 1996. Under the approved
scope of the LSEOR Project, the KRU plans to acquire up to 26 MBPD of
Prudhoe Bay NGLs upon completion of start-up activities. The actual volume of
NGLs acquired will depend on Kuparuk's facility limits and Prudhoe Bay's
volume of NGLs available. These NGLs will be combined with approximately
14 MBPD of Kuparuk enriching fluids and injected as MI at 12 to 15 Kuparuk
drill sites (including Drill Sites lA, 1Y, and 2Z). The remaining six to nine
planned EOR drill sites will commence MI injection as mature EOR patterns are
converted back to water or lean gas injection.
Incremental oil recovery from the 18 additional LSEOR drill sites is expected to
range from 4% to 10% of the Original Oil In Place (OOIP), resulting in over 200
MMSTB of additional Kuparuk oil reserves. Recovery of these reserves,
pursuant to the LSEOR Project plan, will require the acquisition of
approximately 100 MMSTB of NGLs, but approximately 35% of the acquired
NGLs are expected to ultimately be produced as part of'the Kuparuk crude
stream.
KRU LSEOR Project Application -4-
Additional LSEOR Project details are addressed within the 14 specific
requirements of 20 AAC 25.402(c). ARCO Alaska, Inc.'s proposed findings,
recommended conclusions, and requested decisions of the Commission are
included at the end of this application.
Plat of Project Area
20 AAC 25.402(c)(1)
A plat of the Kuparu'k River Unit showing the bottom hole locations of all
proposed and existing injection wells, production wells, abandoned wells, dry
holes, and any other wells that penetrate the injection zone within the Unit is
included as Exhibit 1. The boundaries of the Kuparuk Participating Area (KPA)
and the proposed LSEOR Project area are displayed on the KRU plat. The
planned LSEOR Project involves expansion of the enriched gas EOR process
beyond Drill Sites lA, 1Y, and 2Z to Drill Sites 1 F, 1 G, lQ, 1 R, 2A, 2B, 2C, 2D,
2F, 2G, 2H, 2K, 2M, 2T, 2U, 2V, 2W, and 2X. The KPA will be expanded to
include the bottom hole locations of any wells proposed for drilling beyond the
current KPA boundary adjacent to Drill Sites 2M and 2T prior to injection into, or
production from, these wells.
Operator & Surface Owners
20 AAC 25.402(c)(2)
The LSEOR Project is located within the Kuparuk River Unit, which is operated
by ARCO Alaska, Inc.' The owners of surface rights within the LSEOR Project
area and extending one-quarter mile beyond the project area boundary are
listed in Exhibit 2.
Affidavit 20 AAC 25.402(c)(3)
An affidavit showing that the operators and surface owners within a one-quarter
mile radius have been provided a copy of this application for injection is
included in Exhibit 2.
Project Description 20 AAC 25.402(c)(4)
The LSEOR Project will significantly expand the miscible enriched gas EOR
process beyond Drill Sites lA, 1Y, and 2Z and is designed to ultimately cover
21 KRU drill sites during the expected 15 to 20-year life of the project. Without
this project, the current KRU Enriched Gas EOR Project would likely be limited
to two or three additional drill sites using MI manufactured from enriching fluids
indigenous to the Kuparuk River Field. As depicted in Exhibit 3, the proposed
LSEOR Project will involve the acquisition of NGLs from the Prudhoe Bay
Central Gas Facility (CGF) for blending with Kuparuk lean gas to significantly
increase MI injection within the Kuparuk River Field. A discussion of the facility
requirements for this project follows.
KRU LSEOR Project Application
The Oliktok Pipeline will be used to transport NGLs from Skid 50, the Prudhoe
Bay NGL/oii blending facility, to Kuparuk's CPF-1. This 16-inch pipeline was
last in service in 1988 as a natural gas pipeline. It is currently being prepared
for recommissioning in NGL service.
Since NGLs will be required to blend with lean gas at both CPF-1 and CPF-2, a
new NGL tie-line will.be installed between these facilities. At CPF-1, a new
module will be installed with facilities to receive the NGLs from the Oliktok
Pipeline and pumP them into new vessels at CPF-1 and CPF-2 (via the NGL tie-
line) where the NGLs will be mixed with indigenous Kuparuk enriching fluid.
These liquid hydrocarbon mixtures will then be pumped to injection pressure
(above 4,000 psi) by an existing pump at CPF-1 and a new pump at CPF-2 and
blended with compressed lean gas at each CPF. The mixing of gas and liquid
will be controlled to produce MI with a minimum miscibility pressure of
approximately 2,900 psi with the reservoir oil.
The other significant facility modification is an expansion of the electric power
distribution system which will allow excess power at CPF-3 to be utilized by the
new electric driven NGL transfer pumps at CPF-1. No significant MI distribution
system modifications will be required, as high pressure gas piping has
previously been installed for lean gas injection at all of the planned LSEOR
Project drill sites.
To fully utilize the equipment planned for the LSEOR Project, up to 26 MBPD of
Prudhoe Bay NGLs will be required upon start-up completion in late 1996. The
actual volume of NGLs acquired will depend on the ultimate capacity of the
LSEOR Project equipment and the volume of NGLs available at Prudhoe Bay.
When these NGLs are blended with approximately 14 MBPD of Kuparuk
enriching fluid, the total Kuparuk MI injection rate is expected to increase from
about 65 MMSCFD to nearly 220 MMSCFD. This rate of MI will be sufficient to
flood 12 to 15 Kuparuk drill sites with MI, and the remaining six to nine planned
EOR drill sites will be phased in as MI injection is reduced in mature EOR
patterns. The expected MI injection rate contemplates that, in future years, MI
returned from Kuparuk EOR drill sites will supplement NGLs imported from
Prudhoe Bay. We expect that the daily rate of NGLs acquired from Prudhoe
Bay will decline over time.
Both the A and C sandstone units (see Formation Geology below) within an
EOR pattern will be flooded with MI, provided that both sands are expected to
remain open to flow for several years. MI injection will be alternated with water
injection to improve the sweep of the MI. Because the injectivities of the A and
C intervals within a well differ, the ultimate MI slug size injected into the A and C
intervals of an EOR pattern will also differ. Therefore, the ultimate MI slug size
injected within the LSEOR Project area is expected to range from 10% to 30%
of a pattern's hydrocarbon pore volume. Similarly, the expected incremental oil
recovery varies from 4% to 10% of a pattern's OOIP.
KRU LSEOR Project Application -(~-
Finally, additional drilling is planned for certain areas of the LSEOR Project drill
sites. Potential drilling opportunities have been identified where a peripheral
well or a structurally isolated infill well is expected to recover incremental
tertiary reserves by providing a means for MI to contact additional pore' volume.
A few pattern infill locations have also been identified where a significant
change in fluid flow path within the reservoir is expected to improve MI sweep.
Pool Description 20 AAC 25.402(c)(5)
The A and C intervals of the Kuparuk River Pool will be affected by the LSEOR
Project. The Kuparuk River Pool is defined by Rule 2 of Conservation Order No.
173 as the strata that are common to, and correlate with, the accumulation
found in the Atlantic Richfield Company West Sak River State No. 1 Well
between the depths of 6,474 and 6,880 feet, measured depth, or 6,387.9 and
6,793.9 feet, subsea. The West Sak River State No. 1 type log is shown in
Exhibit 4.
Formation Geology
20 AAC 25.402(c)(6)
The stratigraphy of the Kuparuk River Formation is depicted in Exhibit 5. The
Kuparuk River Formation was deposited on a shallow marine shelf during Early
Cretaceous time and is divided into Lower and Upper Members, which are
separated by a regional Lower Cretaceous unconformity. Each member is
subdivided into lithostratigraphic units; the A and B in the Lower Member and
the C and D in the Upper Member. Units A and C are further divided into
stratigraphic intervals based upon well log response.
Reservoir sands are located in Units A and C. The A sands are a sequence of
interbedded marine sandstone, siltstone, and mudstone. The sandstone is
quartzose, very fine- to fine-grained and generally well sorted. Reservoir
sandstone in Unit A averages 23% porosity and 100 md permeability. Unit C is
composed of bioturbated marine sandstone which is quartzose, fine- to coarse-
grained, and poorly- to moderately-sorted. The sandstone contains trace to
abundant amounts of glauconite and secondary siderite cement. Porosity and
permeability in Unit C is highly variable but averages 23% and 130 md. Unit D
is composed of primarily mudstone and siltstone, while Unit B is comprised of
thinly-interbedded very fine-grained sandstone, siltstone, and mudstone.
The Kuparuk River Field is a combination structural and stratigraphic trap. The
main structure is a broad anticline which plunges to the southeast. The
shallowest depth to the top of the Kuparuk Formation within the project area is
5,611 feet subsea in Well 2T-11. The deepest penetration of the top of the
Kuparuk in the area is 6,515 feet subsea in Well 1R-22. Along the western
margin of the field, Unit A is truncated by the unconformity at the base of the
Upper Member and the Unit C sandstone pinches out. The southern extent of
the field is delineated by decreasing reservoir quality in both units. To the north
KRU LSEOR Project Application -7-
and east, the limit of the oil pool is determined by the intersection of the
reservoir sands and local oil-water contacts that range in depth from 6,530 feet
subsea to 6,710 feet subsea.
,.
The confining interval above the Kuparuk River Formation consists of more than
2,000 feet of Cretaceous shale. The lower confining interval is the Kingak
shale, which exceeds 1,500 feet in thickness.
Injection Well Logs 20 AAC 25.402(c)(7)
All injection well logs have been submitted to the AOGCC in accordance with
Conservation Order 173.
Injection Well Casing Description
20 AAC 25.402(c)(8).
Typical completion designs used for injection wells within the LSEOR Project
area are shown in Exhibit 6. The completion design selected for a specific well
is dependent on the productivity of the A and C sandstone units encountered by
the well and the separation between these sands.
The typical casing program used for production and injection wells within the
LSEOR Project area utilizes three strings of casing:
1) 16", 62.5 lb casing from surface to -100 ft measured depth;
2) 9-5/8", 36 lb or 10-3/4", 45.5 lb casing from surface to a measured
depth of 2,000-4,000 ft; and
3) 7", 26 lb casing from surface to bottom.
Well completion data, including casing, cementing, and testing programs, have
been, and will continue to be, submitted for each injection well in accordance
with 20 AAC 25.030.
Each producing well which is converted to injection service is re-tested in
accordance with 20 AAC 25.412.
To demonstrate the mechanical integrity of all injection wells in the Kuparuk
River Field, annulus pressures are monitored and reported monthly to the
AOGCC.
Injection Fluids 20 AAC 25.402(c)(9)
As previously mentioned, the MI required for the proposed expansion of
Kuparuk's enriched gas EOR process will be manufactured at CPF-1 and CPF-2
KRU LSEOR Project Application -8-
by blending lean gas from the Kuparuk River Reservoir with NGLs acquired
from the Prudhoe Bay CGF. Upon full LSEOR Project start-up (late 1996), up to
26 MBPD of PBU NGLs, combined with approximately 14 MBPD of Kuparuk
enriching fluid, will be blended with up to 170 MMSCFD of Kuparuk lean gas to
produce nearly 220 MMSCFD of MI with a minimum miscibility pressure of
approximately 2,900 psi. The expected composition of MI produced at each
CPF in late 1996 is presented in Exhibit 7.
The composition of Prudhoe Bay NGLs will vary depending on actual CGF
operating conditions. The Kuparuk enriching fluid is comprised of several light
hydrocarbon liquid streams produced by the KRU facilities. Specifically, the
CPF-1 enriching fluid is comprised of scrubber liquids from the CPF-1 artificial
lift gas compression system, NGLs from the CPF-1 NGL plant, and naphtha from
the Kuparuk River Unit Topping Plant. The CPF-2 enriching fluid is comprised
of scrubber liquids from the CPF-2 artificial lift gas compression system and
NGLs from the CPF-2 fuel gas stripping unit. Laboratory core flood experiments
indicate that MI with these constituents is fully compatible with the Kuparuk
River Formation.
Water will be injected alternately with MI in the EOR injection wells to improve
the MI sweep in the reservoir. Approximately 400 MBPD of water will be
injected into the proposed LSEOR Project area, including the three existing
EQR drill sites. However, not all of the drill sites in this region will be receiving
MI simultaneously. Those drill sites which are not initially converted to MI
injection will continue to inject lean gas alternately with water until MI injection
is initiated.
Beaufort Sea water and Kuparuk produced water will be injected in the
proposed LSEOR Project area. Both of these water sources have been
previously approved for injection under the AOGCC Conservation Order 198.
While these two types of water are compatible with the Kuparuk River
Formation, they tend to precipitate barium sulfate or calcium carbonate scale
when mixed. Therefore, within the Kuparuk facilities, sea water and produced
water are either handled by separate injection systems or treated with scale
inhibition chemicals.
Injection Pressures 20 AAC 25.402(c)(10)
The maximum MI and water injection pressures available at the plants will be
4,400 psi and 3,000 psi, respectively. Due to pressure losses in the distribution
systems, actual wellhead pressures will vary across the field. The average MI
and water injection pressures at the wellheads within the proposed LSEOR
Project area are expected to be 3,800 psi and 2,700 psi, respectively.
KRU LSEOR Project Application -~)-
No Fracture Propagation
20 AAC 25.402(c)(11)
The maximum injection pressures for the enhanced recovery wells will not
initiate fractures into confining strata and, therefore, will not allow injection or
formation fluid to enter any freshwater strata.
Injection into the Kuparuk River Formation at bottom hole pressures above the
formation parting pressure often occurs in water injection wells. However,
injection at such pressures does not breach the integrity of the confining zone.
The reservoir is separated from other producing horizons and water bearing
zones by over 2,000 feet of confining shales which act as an impermeable
barrier. These shales provide a substantially greater barrier than necessary to
contain fractures within the Kuparuk River Formation.
Formation Water Analysis
20. AAC 25.402(c)(12)
Produced water analyses from the Kuparuk River Formation are included in
Exhibit 8. Since the LSEOR Project includes drill sites across the CPF-1 and
CPF-2 areas, laboratory analyses are presented for produced water samples
from each of these production facilities.
Freshwater Exemption 20 AAC 25.402(c)(13)
All aquifers or portions of aquifers lying below and within one-quarter mile of the
KRU are exempted aquifers for Class II injection (reference 40 CFR
147.102(b)(3), 20 AAC 25.440(c), and Area Injection Order No. 2).
Incremental Hydrocarbon Recovery
20 AAC 25.402(c)(14)
The expansion to the Kuparuk enriched gas EOR process, in combination with
the proposed drilling, within the LSEOR Project area is expected to increase
KRU oil recovery by over 200 MMSTB. This represents incremental recovery of
4% to 10% of the OOIP within these 18 drill sites, based on total MI injection of
10% to 30% of the area's hydrocarbon pore volume. While approximately 100
MMSTB of Prudhoe Bay NGLs are required to achieve this recovery pursuant to
the LSEOR Project plan, approximately 35% of the acquired NGLs are expected
to ultimately be produced as part of the Kuparuk crude stream.
KRU LSEOR Project Application - ]. 0-
Proposed Findings
ARCO Alaska, Inc., as KRU Operator, respectfully proposes that the
Commission make the following findings.
1. The proposed LSEOR Project will add up to 59,000 surface acres
to the current KRU Enriched Gas EOR Project at Drill Sites lA, 1Y, and 2Z,
which covers about 8,700 surface acres.
2. With' this areal expansion of the enriched gas EOR process at
Kuparuk, the approximate OOIP in the project area will increase from 575
MMSTB up to 2,900 MMSTB.
3. To meet the projected MI requirements of this EOR project
expansion, it is expected that approximately 100 MMSTB of Prudhoe Bay NGLs
will be utilized during the project's life.
4. Implementation of the Kuparuk LSEOR Project will require facility
modifications and additions, including new NGL transfer pumps at CPF-1, a
new NGL injection pump at CPF-2, a new NGL pipeline between CPF-1 and
CPF-2, enriching fluid collection system modifications at CPF-1 and CPF-2, and
an electric power distribution system expansion between CPF-1 and CPF-3.
5. Injection of MI into the EOR expansion area is scheduled to
commence in late 1995, and the new facilities are scheduled to be fully
operational in late 1996.
6. Within the EOR expansion area, approximately 150 current water
and gas injection wells are expected to have MI injected. Furthermore, there
are currently over 180 producing wells within this expansion area.
7. There are up to 70 new production and injection wells planned for
the EOR expansion area. These wells, which are designated in red on Exhibit
1, are consistent with the Unit plan of development for the LSEOR Project. As
new production wells are drilled, some of the existing producers will be
converted to injectors and will receive MI alternated with water injection.
8. Additional drilling within the Kuparuk enriched gas EOR area is
expected to improve the distribution of MI in the reservoir and increase the EOR
reserves.
9. The expected increase in oil recovery from the expansion of EOR
acreage and additional drilling within this acreage is over 200 MMSTB.
KRU LSEOR Project Application
Recommended Conclusions
ARCO Alaska, Inc., as KRU Operator, respectfully requests that the Commission
make the following conclusions.
1. Expansion of the Kuparuk enriched gas EOR process via the
proposed LSEOR Project, in conjunction with additional drilling within the EOR
expansion area,' involves the application of a tertiary enhanced oil recovery
method in accordance with sound engineering principles.
2. The combination of expanding the Kuparuk enriched gas EOR
process and drilling additional wells within this expanded area is reasonably
expected to result in more than an insignificant increase in the amount of crude
oil that ultimately will be recovered.
3. The proposed areal expansion of Kuparuk's enriched gas EOR
process will be undertaken to recover oil from areas not substantially affected
by previously implemented tertiary recovery activities and will be applied to
acreage and reservoir volume to which tertiary activities have not been applied
previously.
4. The proposed additiOnal drilling within the EOR expansion area
will be undertaken to sweep areas of the reservoir previously unaffected by the
enriched gas EOR process and to recover oil from areas and reservoir volume
not substantially affected by previously implemented tertiary recovery activities.
5. MI enriching fluid (i.e., NGL) from outside the KRU is required to
increase the supply of MI for expansion of Kuparuk's enriched gas EOR
process.
6. Facility modifications and additions within the KRU are required to
manufacture and inject additional MI for expansion of Kuparuk's enriched gas
EOR process.
Requested Decisions
ARCO Alaska, Inc., as KRU Operator, respectfully requests that the Commission
issue an order authorizing the underground injection of miscible enriched
natural gas for enhanced oil recovery in the expanded area of the proposed
KRU Large Scale EOR Project.
ARCO Alaska, Inc., as KRU Operator, respectfully requests that the Commission
endorse: 1) the areal expansion of the enriched gas EOR process via the
proposed KRU Large Scale EOR Project and 2) additional drilling within the
EOR expansion area.
KRU LSEOR Project Application
-12-
EXHIBIT 1
KRU LARGE SCALE EOR PROJECT
Plat of the Kuparuk River Unit
EXHIBIT 2
KRU LARGE SCALE EOR PROJECT
Affidavit of Daniel G. Rodgers
~' and
List of Surface Owners
STATE OF ALASKA
THIRD JUDICIAL DISTRICT
I, Daniel G. Rodgers, declare and affirm as follows:
1: I am emPloyed as a Senior Attorney by the Atlantic Richfield
Company, and I serve as in-house council in Anchorage, Alaska for ARCO's
wholly owned subsidiary, ARCO Alaska, Inc.
2. On ,~,¢.. 0¢ , 1995, I mailed copies of the Kuparuk River Unit
Large Scale~R Project application for injection to the following owners of
surface rights within a one-quarter mile radius of the proposed Project area.
Mr. Ken Boyd
State of Alaska
Department of Natural Resources
3601 C Street.
Anchorage, AK 99503
Ms. Nancy Welch, Regional Manager
Alaska Department of Natural Resources
Division of Land
3700 Airport Way
Fairbanks, AK 99709-4609
Mr. Ron Swanson, Director
Alaska Department of Natural Resoumes
Division of Land
3601 C Street, Suite 1122
Anchorage, AK 99503-5947
-1-
Mr. Jerry Brossia
Alaska Department of Natural Resources
Pipeline Coordinator's Office
411 West 4th Ave~, Suite 2C
Anchorage, AK 99501-2343
Mr. Brad Berg
Kuparuk Pipeline
P. O. Box 100360
Anchorage, AK 99510-0360
Mr. Don Puckett
Oliktok Pipeline
P. O. Box 100360
Anchorage, AK 99510-0360
Dated: ~ ¢o , 1995
Daniel G. Rodgers
Declared and affirmed before me this ~'~
day of June, 1995.
fo~Alaska
Notary~Public in and
My commission Expires: ¢~ t' · ~- ~-' ~ t
-2-
KRU LARGE SCALE EOR PROJECT
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"'q:-": .-: ...... · ......... .......: .. · .........
................................... '~':.".'.::'11
'.-':L...:.:.:::::::".. ' ..: ................. .~.:.':"~.."~ .......................
..... · "5: i':; .' :. :!ii:::i$,ii,L! :.!$::.ii,ii::i::::::ii ...... i:. ii ..... . .............
. .. :~.:: ......... · .......................... ".-_..'.. .-'.. - ...........
.................................. :-..:.._-::..::..-_...... ..................... ":'~' :....:.-:: : ~
............. . ........ .~, ..... '" · · · ~ · .....' ....
--' ~'~-" '~ ' -I- ...... ~--- '!' --
,._. ............ o.. · ~ ..........................
.......... "'.'""7:: ...................... :.:::
· ·
... ............... ~ ..... o. ..........
~,. ...............
.......... ,i, ....... ~ ........ ~ ........ ~ ........ .i, ...... . ·
~ .:"
· ' '.='=.:=i=.ii-=-.:=;.=.-i='"":..:=: ='i-=.'= 22...'......2.'.. ' ' ........ '.....22:'. 'i!i-'='~
::~=.:=.'..... 22'!:7!"i .......................
................. :...:.':.:--..:.--.-.:: ::.: :.:-.- i: !!,:,.-:-:i.::'":'::.:.::::::v:. .... :.:i...:..: .....
· :.,_.. :.:.: ............. .: ::.:.::: .-: ...... · .......................................
· ~ ..... .~ · · ·. ....... . ..... . ................... ,i,...
· :': ":'". ...... : ..................... :" '-:':"'5':::.'!:..'::.5:::':: :!:. :...:-'.. ::':':-':
'F"::~::. ':. '::.' .. ":.: '.:: :..: :-.:::::..::: ::' · ..:.: ..... :.. :... :..: · ::.. :..-..
.'
........................ · .'--..:' :_-. :':.~.. . -_ .:.. ':..- .........
....~ · · . ,! ........... ~. .~ ~ ......
............................................... 2 '... :.'-'.. '"
· ~"
....~:.~..,.~ .................. :......:.:..:.:::... :.::i ..... i.:.:"~..:. 'i.. :..i' · .i":: -:
..... :' :.., ...... -_.' :...:
·
....... . ....... ~. .......
.... . ..................... . ....... ~. ........
· .-....... . . . _- .:~.o ........ :.'--'.- .... .-
2' ' ':. ':": ......:::' :::::'::.i:i:!:'q: ...... : ":"' ..
........ .7 -.. · .' ........................ : ..... : ". ...... .'. 'i' :.'" '
....
........ ;?.:'~!3'~ 7 ':::?.5 i;!.;iE;!".lL:.'.:.: .::.!..:::$i. ::?:. :'!.ii: :. :. :.'..:-::.. ~' '"....~ ~ ~-"~ .....
.............. ::..:.::.. ..... ::.:..:.::.:..:._...:..:.. ...... ..:.:....:.::,
;!:;:::::::::::::.... :..:: ........ :::::::: :.:.::::':::.:: :: .... · ........................
~-:::: ""::::" :,..:.:..:.: ::: :....:..:.:.:. :::::::::::::::::::::: .........
...............
~'"': ' " ': ............. : ........ "'":":: ...... I:':i' i.:i.:::::::':'::::':-:::"::'..:..:i'_:!: .........
:::.! ... 'v... · .......................
,='~.i:..::'..'::"':'..': :':2:'..'.:." ::2.! ""..:..!.. '"' = ':" =' :" "' ":" "'
I ':'.. '"'
......... o ..... o~ ....... ........ . .... .. .~.
! ~ , .....
KRU LARGE SCALE EOR PROJECT
Stratigraphy- Kuparuk River Formation
Gamma Resistivity Subsea IntervaI Unit Member Formation
0 RAY150 I 1000 Depth
· Kalubik
·
~ ~' "'"'"'1 'C' Sandstone
~' ~ / . Glauconitic, '
Siderite-cemented
- Sandstone
- -6000' 'i'~-~ C Upper
¢+-.2 / · Complex Mineralogy
& Pore Distribution
'"' ; · Pay Recognition on
Logs Difficult.
- -6100' ~= o.~-~O~o
k: 0.01 - 3000 md
Lower ·
- -6300'I Miluveach
,
[---] Sandstone ~ Mudstone [--] Interbedded Sandstone, Siltstone, and Mudstone
,
EXHIBIT 6
KRU LARGE SCALE EOR
PROJECT
Injection Wellbore Schematic
Selective
Production
cum.
Production/
Injection
Pm:~er
KUPARUI(
A
S~ND
Single Single
Blast Joint
-- Production/
Injection
EXmBIT 7 ~
KRU LARGE SCALE EOR PROJECT
Miscible Injectant Compositions
(Mole %)
Component CPF-1 CPF-2
N2
CO2
C~
C2
C3
iC4
nC4
nCs
C6
C7
Ce+
0.4 0.4
0.8 0.8
65.8 66.7
7.6 7.1
7.0 4.8
2.2 2.5
6.0 6.6
2.1 2.4
2.8 3.3
2.2 2.4
1.9 2.0
1.2 1.0
('
EXHIBIT 8
KRU 'LARGE SCALE EOR PROJECT
Water Analyses
F~om:
ARCO ALASKA, INC.
KUPARUK LABORATORY SERVICES
ANALYSIS REPORT
TO:
February 10, 1994
Corrosion NSK-39
CPF-1 Facility Engineer NSK-6
CPF-1 Supervisor NSK-6
The following analytical resuits have been obtained for the
indicated sample which was submitted to this laboratory:
Sample I.D. AA~78~4 Sample point: CIOPWTW
Sample description: CPF-1 Prod.. Water Tank Outlet ~
Sample collector: DML Sample collection date: 02/07/94
Lab submittal date: 02/07/94 Time: 17:11
Parameter Result
Sulfate by IC~- 113
Iron by AA~- 0.7
Sulfide~ 12
PH+ 7.9
.,Specific Gravity @ 60 degrees F 1.0185
Units
rog/1
mg/1
mg/1
MDL
1
0.1
1
0.1
0.0001
~onductivity 39692 micro-mhos/cm 1
42hloride 13684 mg/1 1
~Bicarbonate 2489 mg/1 1
~arbonate 0 mg/1 1
Barium~ o 39 mg/1 1
Calcium~ - 54 mg/1 1
Magnes ium~ - 67 mg/1 1
-- ~odium 9259 mg/1 1
~Strontium 5 mg/1 1
Potas s ium 36 mg/1 1
If there are any questions regarding this data, please call.
Completed By: .~P/~R Reviewed By: ~
From:
ARCO ALASKA, INC.
KUPARUK LABORATORY SERVICES
ANALYSIS REPORT
February 10, 1994
To: CPF-2 Super./Fac. Eng. NSK-14
Corrosion NSK-39
The following analytical results have been obtained for the
indicated sample which was submitted to this laboratory:
Sample I.D. AA17815 Sample point: C2OPWTW
Sample description: CPF-2 Prod..Water Tank Outlet ~ .....
Sample collector: DML Sample collection date: 02/07/94
Lab submittal date: 02/07/94 Time:.17:ll
Parameter Result
Sulfate by IC 206
Iron by AA 0.4
Sulfide 15
PH 8.0
Specific Gravity @ 60 degrees F 1.0198
Units MDL
mg/1 1
mg/1 0.1
mg/1 1
0.1
0.0001
Conductivity 40892 microLmhos/cm 1
Chloride 14876 mg/1 1
Bicarbonate 2244 mg/1 1
Carbonate 0 mg/1 1
Barium 30 mg/1 1
Calcium 69 mg/1 1
Magnesium 96 mg/1 1
Sodium 9564 mg/1 1
Strontium 8 mg/1 1
Potassium 40 mg/1 1
If there are any questions regarding this data, please call.
Completed By: ~-.~~/~_ Reviewed By
-2-
ARCO ALASKA
{" PRUDHOE BAY CENTRAL LAB~' '~TORY
· ANALYTICAL REPORT'~
,aRCH [UE NUMBER: ;'84 AP. CH IVE VOLUME
FACILITY:
SAMPLE NUMBER:
COMPANY: ARCO
SAMPLE DATE/TIME:
SAMPLE TYPE: SEAWATER
SAMPLE POINT/METER ~P: ERST SUPPLY LINE
SAMPLE DZSCR let I ON: S[AWA TEE (JJ
REQUE~TOR: R.STEPHRHS ~5
II~IIIIIlIIIlIllIIIIII~-IIIIIIIIIIIIIIIIIIIIIIIIIIIIIIIII~IIIIIIIIIIIIIIIII
DETERMINATION UALUE UNITS STATU~
hydrox.ul 0. Mg/L
Carbonate . 0. Mg/L
Bicarbonate
pH .
M~gnes ium i~40. Mg/L
P~t ass ~um 422. Mg/L
~od ium ll4~0. Mg/L
B~r ~um < [. 00 Hg/L
~t.ont ium 8. Mg/L
[ ~on ( i. Mg/L
Aluminum <1. O0 Mg/L
~i I icon
COPPER < l. Mg/L
Su I ~ e t · 22~ O. M~/L
Chlo.ide 210~4. Mg/L
Fluor ida l. Mg/L
S~eci~ic Gravity
Resistivity ~ ~8 degrees F. ~.212 OHM-H
COMMENTS:
SUL?ATE
Comp leted by .......... I ' '
Reviewed by .~_ ,
~TP OPERATIONS SUPERVISOR ~2~
F~ ~I/STP ~UPERINTEHDENT
StP FACILITY ENGINEER
S I P OPERAT[ ONS SUPERU I $OR
CORROS l ON SPEC I AL I ~T
OPERRT I OHS ENG. C00RD I NATOR 924
S. M. BUCRRUM PRC
H.G. BYARS PRC E212
MIKE BILL ATO
LAB F!LE
· "1
-3-
Notice of Public Hearing
STATE OF ALASKA
Oil and Gas Conservation Commission
Re: The application of ARCO Alaska, Inc. for approval to initiate a large scale
enhanced oil recovery project in the Kuparuk River Unit.
Notice is hereby given that the Alaska Oil and Gas Conservation Commission (AOGCC)
will hold a public heating July 20, 1995 to examine conservation issues related to the
ARCO Alaska, Inc. proposal to initiate a large scale enhanced oil recovery project in the
Kuparuk River Unit (KRU). The ARCO Alaska Inc. proposal will entail the purchase of
natural gas liquid (NGL) from the Prudhoe Bay Unit (PBU) to serve as an enhanced oil
recovery (EOR) solvent in the KRU. Testimony will be sought concerning:
1) the additional recovery from KRU anticipated,
2) the scope and timing of the EOR project,
3) the proposed volumes and composition of the NGL sold to KRU,
4) the relative efficiency of the injectant as an EOR agent in the KRU as compared
to the PBU,
5) the effect of sales to KRU on recovery from PBU,
6) the effect of sales to KRU on the disposition of NGLs from PBU.
The hearing will be held at the offices of the Alaska Oil and Gas Conservation
Commission, 3001 Porcupine Drive, Anchorage, Alaska 99501 at 9:00 AM on July 20,
1995.
If you are a person with a disability who may need a special modification in order to
comment or to attend the public hearing, ploase-~ ~'IJi'a~Fleck at 279-1433 no later
than July 17, 199~~~
David W~'nston, ( ~~
Alaska Oil a~kd, xGas Conservation Commission
Published July 12, 1995
#13231 ;
STOF 0330 ~
AFFIDAVIT
$65.00
STATE OF ALASKA, )
THIRD JUDICIAL DISTRICT. )
...~.v.a... ~.,.. ~..a..~.~ D.a..n. ~. ...................
being first duly sworn on oath
deposes and says that he/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
July 12, 1995
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.
signed
Subscribed and sworn to bi~'re
me this [..~... day of .~ ....
.....
Notary Public in and for
the State of Alaska.
Third Division,
Anchorage, Alaska
MY COMMISSION EXPIRES
....................
OF
PUBLICATION
I NotiCe M public Hearing
I"' STATE OF ALASKA
I Oil, ol~d Gas Conservation
/Re: Re application of ARCO,
J'Alaska,,IriC; for approval to
I initiate a, large scale enhancecl
.0il recovery pr0iect in the
Ku'POruk Riv.er unit.
N~tice is hereby given that 'the
~ask_o Oil and Gas Conserva-
on commission (AOGCC) w II
,alii' !a :rlublic. hearing JulY
995 tO examine conservation
issues."r, elofecl .to the ARCO
Ala.sk0, I,nc. prOPosal to initiate
a..'large:'scal'e..ehhanced oil re-
covery~l~roiect ih,the Kuparuk
River unit (KRU).' The ARCO
~,laskd',. Ihci proposal will entail
le .'PurChaSe' .'.o~'. natural gas
m.i~ ':',IGL) '-:'~ the Prudhoe
B:.'~ '?it ?'.~',." ": serve os an
enhanced,'!o]'l.' recovery (EAR)
s01.~ent~i~:,the KRU. Te~timon'
will be .sought concerning:
1.)'!ille.'0iJditionol ~ecovery f~or
'KRU. dnticipated,
2') the scope and timing of thi
'EOR prol, ect, · -:
3) the prbposed volumes anc
compositicm of the NGL sold
I~'RU, ' ' ' ' .
~;~.)' th~ r~lotive efficiency of' ih~
iniectont os bn EaR agent 'ir
the KRU as compared to t,h~
, I ,,rPB U, I I i Ii ''I: I
/
?,,'5~)',the'effm:t,of, Sale~ to KR'U, or~
'. ;~e'c0v~ry 'fr0m'., PB'U, ...." .' J
, ,I 6),~the effect of. s.ale to' KRU onJ
~i ~the' diSP0Sl,fi0n'',' Of, NGLs fr0mJ
',' 'mJu, :,:,, :' :,,,' J
' :'",' · : '".. ':-: '
i~:.' ""': ~' "..'~-' "' [ ': i: -"' '. .... 0'n,
' q0r,'
.~.';:". ':':'.'~.: ;;?' ':' : , ''. "on
,
With'..a
:~'~.:.":"".. ~: '"',. need a.spe-
· : ~ ':::--':::":" in' 0rderto'
' ' :: ..... :m''' :' ': : .... :,' ""? Public
':'.'":' .'..::.' ':" '. 'Diana
., ['Fleck. at .279,1433 no later :than
-~' 'J.'UlY". 17,~'1995, :.." .:. "" .
,, I.,lS,~,l~Civ'id W,, J ohrlSto~ :,,, ;. ,,' .:
,'Commiss'ioner '- , ,
. Alaska'Oi'J and Gas
conservation Commission
Pub: jU y 12, 1995
Notice of Public Hearing
STATE OF ALASKA
Alaska Oil and Gas Conservation Commission
Re:
The application of ARCO Alaska, Inc. for approval to initiate a large scale enhanced
oil recovery project in the Kuparuk River Unit.
In an application dated June 6, 1995, ARCO Alaska, Inc. has applied to the Commission for
permission to significantly expand injection of an enhanced oil recovery solvent into the Kuparuk
River Oil Pool within the Kuparuk River Unit on the North Slope.
A person who may be harmed if the requested order is issued may file a written protest prior to
4:00 p.m. July 6, 1995, with the Alaska Oil and Gas Conservation Commission, 3001 Porcupine
Drive, Anchorage, Alaska 99501, and request a hearing on the matter. If the protest is timely
filed and raises a substantial and material issue crucial to the Commission's determination, a
hearing on the matter will be held at the above address at 9:00 a.m. on July 20 1995, in
conformance with 20 AAC 25.540. If a hearing is to be held, interested parties may confirm this
by calling the Commission's office, 907-279-1433 after July 6, 1995. 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 279-1433 no later than July 17, 1995.
Commissioner
Published June 17, 1995
~14163
ii'
AFFIDAVIT
$55 .oo
STATE OF ALASKA, )
THIRD JUDICIAL DISTRICT. )
Eva M. Kaufmann
being first duly sworn on oath
deposes and says that he/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
June 17, 1995
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
i nd ivid ua. II s.
Subscribed and sworn to ~ore
Notary Public in and for
the State of Alas~.
~lrd D~ision.
Anchorage. Alaska
MY CO~ISSION ~PIRES
OF
PUBLICATION
CLIP
Notice of Public He,ring
STA~E' .OF. ALASKA ]
,,ii~. O:i~, a.O, G
Cofis~ion C~miss~on
"' ifiote o Iorge stole ennonce
oil re'covE~Y prolect
Kupo~k River Unit..'
' 'k , ·
J0p~li~: ~'[ ~"" :o,,~,is~c,' for
~r~b'..,' ::' 'e ,.~J:':: ,.::r ~ . ex-
Jp~nd injection of ~
JoB recover~' solvent into me
JKuparuK Rj~e~ Oil ~eol
/the Ku~aruk:.River'Unit on the
JNorth SldP~." : '.' '
,, ,~,~, ,,-,,"~ ,~,, ~,,,~ ,..,
~ A ,~r'San"'~6g':~9':~.harmed
me re~b~gJ~ or~r.: is. issued t
J maY ~lle. ~'~dtest ~rlor
/ p:m. · July ~' 1~:::, with .the.I
Alaska Oil flod ~S'~CO~servo'j
/ ...' .. · - ' f~
~.Porcu,~'Loe'.Dr ye, Ancheraoe,
J A ~'.'"" i950~ r:':':and' ' requeS~ a J
..... ?'/,~; ,~,' ~;+~, the
".L:.,': ~ . =,. ~' : ,
~'- ."' , ' ....... ; ........i-J
"' ~'~,, ':~ "".".." ' "e,
'~ ,,7': ....' .: : ..... .: a
x.~......:'.: ~....-. ..... ,. .').e
'. .:. '.. .~.: '.~::.... ....
'' ', ,,. ',,.
' .' ..:: .... ~'.." .,." '
...... .' :':, ."',,., , :.; ·
.... :Y":'.~ '~]~" .":".' ......
.: -'..'.' ,.. ..-.... ter
. : .. , : . :.,:.,. is
. .'.,
'~''~...., ,,., :?,........' .
Clol m0diflc0t on ' :...
commen~.o~: to ottend'the public
heoriflm'~'"~ieo's~ ..'.~onf.ocf. Dieno
'Flect o~'"'279-1433, no"lO~
Jul'y 17,~1~5. .' ' ' .'
Pu~; J~ 37,
Notice of Public Hearing
STATE OF ALASKA
Alaska Oil and Gas Conservation Commission
Re:
The application of ARCO Alaska, Inc. for approval to initiate a large scale enhanced
oil recovery project in the Kuparuk River Unit.
In an application dated June 6, 1995, ARCO Alaska, Inc. has applied to the Commission for
permission to significantly expand injection of an enhanced oil recovery solvent into the Kuparuk
River Oil Pool within the Kuparuk River Unit on the North Slope.
A person who may be harmed if the requested order is issued may file a written protest prior to
4:00 p.m. July 6, 1995, with the Alaska Oil and Gas Conservation Commission, 3001 Porcupine
Drive, Anchorage, Alaska 99501, and request a hearing on the matter. If the protest is timely
filed and raises a substantial and material issue crucial to the Commission's determination, a
hearing on the matter'will be held at the above address at 9:00 a.m. on July20 1995, in
conformance with 20 AAC 25.540. If a hearing is to be held, interested parties may confirm this
by calling the Commission's office, 907-279-1433 after July 6, 1995. 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 279-1433 no later than July 17, 1995.
Commissioner
Published June 17, 1995