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Alaska Oil and Gas Conservation Commission
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HomeMy WebLinkAboutAIO 021INDEX AREA INJECTION ORDER NO.21
Meltwater Oil Pool
Kuparuk River Field
1. March 12, 2001 Phillips Alaska, Inc.'s Meltwater Area Injection Order
Application
2.
April 5, 2001
Notice of Public Hearing; Affidavit of Publication and Bulk
Mailing
3.
March 22, 2001
Lease Information (fax)
4.
May 7, 2001
Confidential portion Meltwater Area Injection Order
5.
May 7, 2001
Meltwater Area Injection Order Application
6.
May 7, 2001
Sign -in Sheet for Meltwater Hearing
7.
May 7, 2001
Public Hearing Transcript (Confidential portion in
Confidential room under Meltwater CO 456 and AIO 21)
8.
May 23, 2001
Letter from AOGCC to Phillips re: questions
9.
June 6, 2001
Phillips' request for Aquifer Exemption
10.
July 18, 2001
Letter from Phillips informing AOGCC that they are not
seeking an Aquifer Exemption
11.
September 27, 2004
Public Notice to amend underground injection orders to
incorporate consistent language addressing the mechanical
integrity of wells
12.
December 21, 2009
Letter from CPAI to AOGCC re: Cessation of Water
Injection at Meltwater
13.
October 7, 2011
Interim Update: Meltwater Oil Pool Wells with Elevated
Outer Annuli Surface Pressure
14.
September 25, 2012
Administrative Approval to amend Rule 2 (AIO 21.001)
}
STATE OF ALASKA
ALASKA OIL AND GAS CONSERVATION COMMISSION
333 West ih Avenue, Suite 100
Anchorage Alaska 99501
Re: THE APPLICATION OF )
PHILLIPS ALASKA, INC. for an )
order allowing underground injection )
of fluids for enhanced oil recovery in )
the Meltwater Oil Pool, in the )
Meltwater Participating Area, )
Kuparuk River Field, North Slope, )
Alaska
Area Inj ection Order No. 21
Kuparuk River Field
Meltwater Oil Pool
August 1, 2001
IT APPEARING THAT:
1. By letter and application dated March 12, 2001, Phillips Alaska, Inc. ("PHILLIPS")
requested an order authorizing the injection of fluids for enhanced oil recovery in the
Meltwater Oil Pool ("MOP"). PHILLIPS provided draft written testimony for
Meltwater Pool rules to the Commission on February 14 and March 12, 2001 and
supplemental information on March 22, June 6, June 19, and July 18, 2001.
2. Notice of opportunity for public hearing was published in the Anchorage Daily
News on March 23, 2001. A second public hearing notice changing the date of
public hearing was published in the Anchorage Daily News on April 5, 2001
3. The Commission did not receive a protest.
4. A hearing concerning PHILLIPS request was convened in conformance with 20
AAC 25.540 at the Commission's offices, 333 W. ih Avenue, suite 100, Anchorage,
Alaska 99501 on May 7, 2001. Concurrently, the Commission heard testimony to
define the MOP and establish rules for its development.
FINDINGS:
1. Commission regulation 20 AAC 25.460 provides authority to issue an order
governing underground injection of fluids on an area basis for all wells within the
san1e field, facility site, reservoir, project, or similar area.
2. The proposed MOP is located in the western portion of Township 8 North and Range
7 East, Umiat Meridian, on Alaska State Leases ADL-373111, ADL-373112, ADL-
389058 and ADL-389059. The MOP is located within and adjacent to the current
boundaries of the Kuparuk River Unit ("KRU"), North Slope, Alaska.
)
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l
Area Injection Order No 21
August 1, 2001
Page 2
3. PHILLIPS is the operator of the MOP. PHILLIPS, BP Exploration (Alaska) Inc.,
Unocal Corporation, ExxonMobil Corporation, and Chevron U.S.A. Inc are working
interest owners. The State of Alaska is the surface owner.
4. PHILLIPS has applied to the Alaska Department of Natural Resources to expand the
existing Kuparuk River Unit to encompass the southern half of the proposed MOP
and approve a Meltwater Participating Area ("MP A").
5. PHILLIPS drilled three exploratory wells, Meltwater North 1, 2 and 2A, into the
proposed MOP. Well and 3-D seismic data have been used to characterize the
hydrocarbon accumulation within the proposed MOP.
6. The proposed MOP is defined as an accumulation of hydrocarbons that is common
to, and correlates with, the interval between 6411' and 6974' measured depth
("MD") in the Meltwater North #2A well.
7. The proposed MOP is a sequence of very fine to fine-grained sandstones and
associated mudstones that are late Cretaceous-aged (Cenomanian-Turonian) and lie
within the Seabee Formation. The MOP proposed by PHILIPS is informally divided
into two stratigraphic units that are named, in ascending order, the Bermuda Interval
and the Cairn Interval.
8. The Bermuda Interval is interpreted as a channel fill and lobate sandstone turbidite
fan accumulation, deposited in a slope-apron environment below an incised
Cenomanian-age shelf. This interval lies between 6785' and 6974' MD in the
Meltwater North #2A well, and is the only demonstrated productive interval within
the proposed MOP.
9. The top of the Bermuda Interval dips approximately 2 to 3 degrees to the east-
southeast. Complex faulting occurs along the western (updip) margin of the MOP.
Shale filled channel complexes and stratigraphic pinch-outs act as lateral boundaries
for the MOP.
10. Hydrocarbons are stratigraphically trapped in the Bermuda Interval, and their
distribution is controlled by the distribution of sand. No gas cap or water has been
encountered in Bermuda Interval within the MOP.
11. The MOP Bermuda interval is the stratigraphic equivalent and has similar lithology
to the Tam accumulation to the north. Drilling at Tam has shown these deposits to
be compartmentalized, primarily due to discontinuous sandstone distribution.
12. Petrophysical log, conventional core, sidewall core and cased-hole test data have
been used to determine Bermuda Interval reservoir properties.
13. The Bermuda Interval sands are fine to very fine-grained, lithic-rich, and have
common mudstone laminations and interbeds. X-ray diffraction analyses indicate
clay content ranges from 15 to 25%, but the clay minerals occur dominantly as
framework grains rather than as matrix.
14. Sandstone cores from the Bermuda Interval average 200/0 porosity and 12
millidarcies air permeability. Facies dependent water saturation values calculated
from well logs range from 32% to 450/0.
Area Injection Order No 21
August 1, 2001
Page 3
15. Initial reservoir pressure is approximately 2,400 pounds per square inch ("psi") and
reservoir temperature is 135° F at datum level 5400 feet TVDss.
16. Bermuda Interval crude oil gravity is 37° API, formation volume factor at reservoir
pressure is about 1.33 reservoir barrels per stock tank barrel, solution gas-oil ratio is
about 620 SCF/B, and the viscosity of the oil is 0.76 cps.
17. The Bermuda Interval original oil in place ("OOIP") is estimated to be 125 million
stock tank barrels of oil ("MMSTB"), with an additional possible 7 MMSTB OOIP
within the Cairn Interval (see Cairn Interval description below)
18. Approximately 3,000 feet of impermeable shale separate the top of the Cairn Interval
from the Tabasco Sandstone equivalent, the first overlying potential reservoir zone.
About 500 feet of shale separate the base of the MOP from the underlying I(uparuk
Formation.
19. Recovery estimates range from 18% of OOIP by primary depletion to 29% with a
waterflood (11 % incremental recovery).
20. Model studies of alternating cycles of water and miscible gas injection (MW AG) are
estimated to increase recovery 20 % over primary depletion and 9% over waterflood.
These model studies assumed a 20% hydrocarbon pore volume slug, which is
approximately 46 BCF. Total recovery with an MW AG process is estimated to be
38% OOIP.
21. The MW AG project is scheduled to commence within six months of production
start-up. Existing Kuparuk River Field facilities will be used to supply Miscible
Injectant (MI). An 8-inch MI injection line will be constructed from Imu Drill Site
2N to the Meltwater Drill Site 2P.
22. MI and water will be injected to provide reservoir pressure support and to maximize
recovery. As development matures, lean gas will be injected to maximize recovery
of light hydrocarbon liquids injected as part of the MI stream. Produced water from
the KRU and Meltwater will be the source of injection water. Imu facilities will be
the major source of produced water, MI and lean gas. Produced water from
Meltwater may provide an additional source of injection water.
23. MI and water well head injection pressures are expected to range from 2,600 to
3,600 psi and 1,600 to 2,600 psi, respectively.
24. PHILLIPS' modeling indicates that the maximum injection pressure is not likely to
initiate or propagate fractures through the confining strata.
25. The chloride content in water derived from Meltwater cores is estimated to be
35,000 to 45,000 parts per million ("ppm") NaCI. Average salinity estimates from
core plugs obtained in the Bermuda Interval within the Tam Oil Pool, located 8
miles to the north, is 30,000 ppm NaCl.
26. Wireline log analytical techniques, which comply with EP A recommended methods
as described in "Survey of Methods to Determine Total Dissolved Solids
Concentrations", (KEDA Project No. 30-956), were used to characterize formation
water total dissolved solids content in the Meltwater Oil Pool vicinity.
)
)
Area Injection Order No 21
August 1, 2001
Page 4
27. Analysis of potential underground sources of drinking water also included dipole
sonic and mud log data. These data demonstrate that apparent aquifers in the
Meltwater pool area contain significant hydrocarbon saturations related to either
hydrates or free gas.
28. PHILLIPS interprets the Cairn Interval within the proposed MOP as a marine,
contourite-like, channel fill sand deposit that formed in a base of slope setting. This
interval lies between 6411' and 6785' MD in the Meltwater North #2A well, and is a
potential source of hydrocarbons.
29. Exploration targets within the Cairn Interval are offset along the eastern margin of
the Bermuda hydrocarbon accumulation and are down dip from the western portion
of the field.
30. Reservoir quality sandstones have not been encountered within Cairn Interval, but
may be present near the center of the proposed MOP area. This interval is expected
to be a stratigraphic trap.
31. Phillips will attempt to evaluate the productivity of the Cairn interval early in the
development of the Bermuda interval.
32. Communication between the Bermuda and Cairn Intervals is uncertain at present. It
is uncertain if underground injection of fluids into the Bermuda reservoir will have
any effect on potential Cairn reservoirs.
CONCLUSIONS:
1. The application requirements of20 AAC 25.402 have been met.
2. An Area Injection Order is appropriate for the project area in accordance with 20
AAC 25.460
3. The U.S. Environmental Protection Agency has exempted all aquifers in the existing
KRU (40 CFR Subpart C 147.102).
4. There are no potential underground sources of drinking water in the Meltwater pool
area.
5. The proposed injection operations will be conducted in permeable strata, which can
reasonably be expected to accept injected fluids at pressures less than the fracture
pressure of the confining strata.
6. Injected fluids will be confined within the appropriate receiving intervals by
impermeable lithology, cement isolation of the wellbore and appropriate operating
conditions.
7. Implementation of an enhanced recovery operation involving injection of alternating
cycles of water and miscible gas, MW AG, will preserve reservoir pressure/energy
and enhance ultimate recovery.
8. The proposed MOP water injection project will result in 20 percent (about 25 million
barrels) increased recovery over primary production alone.
)
)
Area Injection Order No 21
August 1, 2001
Page 5
9. Reservoir surveillance, operating parameter surveillance and mechanical integrity
tests will demonstrate appropriate performance of the enhanced oil recovery project
or disclose possible abnormalities.
10. An Area Injection Order enabling enhanced oil recovery activity will not cause
waste nor jeopardize correlative rights.
NOW, THEREFORE, IT IS ORDERED THAT the following rules, in addition to
statewide requirements under 20 AAC 25 (to the extent not superseded by these rules),
govern Class II enhanced oil recovery injection operations in the affected area described
below:
Umiat Meridian
Township
T8N
Range Section
R7E
Sections 1 through 36: All State Lands
Rule 1 Authorized In.iection Strata for Enhanced Recovery
Within the affected area, fluids appropriate for enhanced recovery may be injected for
purposes of pressure maintenance and enhanced recovery into strata that are common to,
and correlate with, the interval between 6,785' and 6,974' MD in the Meltwater North
#2A well.
Rule 2 Fluid In.i ection Wells
The underground injection of fluids must be through a well permitted for drilling as a
service well for injection in conformance with 20 AAC 25.005, or through a well
approved for conversion to a service well for injection in conformance with 20 AAC
25.280.
Rule 3 Monitoring the Tubing-Casing Annulus Pressure Variations
The tubing-casing annulus pressure and injection rate of each injection well must be
checked at least weekly to confirm continued mechanical integrity.
Rule 4
Demonstration of Tubing-Casing Annulus Mechanical Integrity
A schedule must be developed and coordinated with the Commission that ensures that the
tubing-casing annulus for each injection well is pressure tested prior to initiating
injection, following well workovers affecting mechanical integrity, and at least once
every four years thereafter.
Rule 5 Notification of Improper Class II In.iection
The operator must notify the Commission if it leams of any improper Class II injection.
Additionally, notification requirements of any other State or Federal agency remain the
operators' responsibility.
)
Area Injection Order No 21
August 1, 2001
Rule 6
Administrative Action
Page 6
Upon proper application, the Commission may administratively waive the requirements
of any rule stated above or administratively amend any rule as long as the change does
not promote waste or jeopardize correlative rights, is based on sound engineering and
geoscience principles and will not result in an increased risk of fluid movement into a
USDW.
DONE at Anchorage, Alaska and dated August 1, 2001.
Cæ~/lLlU~
Cammy OeWsli Taylor, -C~r
Alaska Oil and Gas Cons rvation Commission
?1¡¡¿!::mmiSSioner
Alaska Oil al1d Gas Conservation Commission
."
Ju.f~~; M ' *L1.~r
Julie M. Heusser, Commissionner
Alaska Oil and Gas Conservation Commission
AS 31.05.080 provides that within 20 days after receipt of written notice of the entry of an order, a person affected by it
may tìle with the Commission an application for rehearing. A request for rehearing must be received by 4:30 PM on
the 23rd day following the date of the order, or next working day if a holiday or weekend, to be timely filed. The
Commission shall grant or refuse the application in whole or in part within 10 days. The Commission can refuse an
application by not acting on it within the 10-day period. An affected person has 30 days from the date the Commission
refuses the application or mails (or otherwise distributes) an order upon rehearing, both being the final order of the
Commission, to appeal the decision to Superior Court. Where a request for rehearing is denied by nonaction of the
Commission, the 30 day period for appeal to Superior Court runs from the date on which the request is deemed denied
(i.e., lOth day after the application for rehearing was filed).
OFFICE OF THE GOVERNOR,
JOHN KATZ STE 518
444 N CAPITOL NW
WASHINGTON, DC 20001
LIBRARY OF CONGRESS, STATE
DOCUMENT SECTION
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NATIONAL CTR MS 950
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AMOCO CORP 2002A, LIBRARY/INFO
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ALFRED JAMES III
107 N MARKET STE 1000
WICHITA, KS 67202-1811
XTO ENERGY,
SUSAN LILLY
210 PARK AVE STE 2350
OKLAHOMA CITY, OK 73102-5605
OIL & GAS JOURNAL,
LAURA BELL
POBOX 1260
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INFORMATION ADMINISTRATION
MIR YOUSUFUDDIN
1999 BRYAN STREET STE 1110
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XTO ENERGY,
MARY JONES
810 HOUSTON ST STE 2000
FORT WORTH, TX 76102-6298
')
PIRA ENERGY GROUP, LIBRARY
3 PARK AVENUE (34th & PARK)
NEW YORK, NY 10016
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PHYLLIS MARTIN MS EI823
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POBOX 61780
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IOGCC,
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GAFFNEY, CLINE & ASSOC., INC.,
LIBRARY
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DEGOL YER & MACNAUGHTON,
MIDCONTINENT DIVISION
ONE ENERGY SQ, STE 400
4925 GREENVILLE AVE
DALLAS, TX 75206-4083
SHELL WESTERN E&P INC,
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HOUSTON, TX 77001-0574
)
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381 ELDEN ST MS 4022
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TECHSYS CORP,
BRANDY KERNS
PO BOX 8485
GATHERSBURG, MD 20898
SD DEPT OF ENV &. NA TRL
RESOURCES, OIL & GAS PROGRAM
2050 W MAIN STE #1
RAPID CITY, SD 57702
LINDA HALL LIBRARY, SERIALS DEPT
5109 CHERRY ST
KANSAS CITY, MO 64110-2498
UNIV OF ARKANSAS, SERIALS DEPT
UNIV LIBRARIES
FAYETTEVILLE, AR 72701
R E MCMILLEN CONSULT GEOL
202 E 16TH ST
OWASSO, OK 74055-4905
BAPIRAJU
335 PINYON LN
COPPELL, TX 75019
STANDARD AMERICAN OIL CO,
AL GRIFFITH
POBOX 370
GRANBURY, TX 76048
H J GRUY,
A TIN: ROBERT RASOR
1200 SMITH STREET STE 3040
HOUSTON, TX 77002
PURVIN& GERTZ INC, LIBRARY
l 2150 TEXAS COMMERCE TWR
600 TRAVIS ST
HOUSTON, TX 77002-2979
OIL & GAS JOURNAL,
BOB WI LLlAMS
1700 W LOOP SOUTH STE 1000
HOUSTON, TX 77027
MARATHON Oil CO,
GEORGE ROTHSCHILD JR RM 2537
POBOX 4813
HOUSTON, TX 77210
EXXON EXPLORATION CO.,
T E ALFORD
POBOX 4778
HOUSTON, TX 77210-4778
PHILLIPS PETROLEUM COMPANY,
W ALLEN HUCKABAY
PO BOX 1967
HOUSTON, TX 77251-1967
EXXONMOBIL PRODUCTION
COMPANY,
J W KIKER ROOM 2086
POBOX 2180
HOUSTON, TX 77252-2180
MARATHON,
Ms. Norma L. Calvert
POBOX 3128, Ste 3915
HOUSTON, TX 77253-3128
TEXACO INC,
R Ewing Clemons
PO BOX 430
BELLAIRE, TX 77402-0430
INTL OIL SCOUTS,
MASON MAP SERV INC
POBOX 338
AUSTIN, TX 78767
DIANE SUCHOMEL
10507D W MAPLEWOOD DR
LITTLETON, CO 80127
)
RAY TYSON
2016 MAIN #1415
HOUSTON, TX 77002-8844
PETRAL CONSULTING CO,
DANIEL L LIPPE
9800 RICHMOND STE 505
HOUSTON, TX 77042
UNOCAL, REVENUE ACCOUNTING
POBOX 4531
HOUSTON, TX 77210-4531
CHEVRON USA INC., ALASKA DIVISION
ATTN: CORRY WOOLlNGTON
POBOX 1635
HOUSTON, TX 77251
WORLD OIL,
DONNA WILLIAMS
POBOX 2608
HOUSTON, TX 77252
PENNZOIL E&P,
WILL D MCCROCKLIN
POBOX 2967
HOUSTON, TX 77252-2967
ACE PETROLEUM COMPANY,
ANDREW C CLIFFORD
PO BOX 79593
HOUSTON, TX 77279-9593
WATTY STRICKLAND
2803 SANCTUARY CV
KATY, TX 77450-8510
BABCOCK & BROWN ENERGY, INC.,
350 INTERLOCKEN BLVD STE 290
BROOMFIELD, CO 80021
GEORGE G VAUGHT JR
POBOX 13557
DENVER, CO 80201
)
CHEVRON,
PAUL WALKER
1301 MCKINNEY RM 1750
HOUSTON, TX 77010
MARK ALEXANDER
7502 ALCOMIT A
HOUSTON, TX 77083
EXXON EXPLOR CO,
LAND/REGULATORY AFFAIRS RM 301
POBOX 4778
HOUSTON, TX 77210-4778
PETR INFO,
DAVID PHILLIPS
POBOX 1702
HOUSTON, IX 77251-1702
EXXONMOBIL PRODUCTION
COMPANY,
GARY M ROBERTS RM 3039
POBOX 2180
HOUSTON, TX 77252-2180
CHEVRON CHEM CO,LlBRARY & INFO
CTR
POBOX 2100
HOUSTON, TX 77252-9987
PHILLIPS PETR CO, PARTNERSHIP
OPRNS
JIM JOHNSON
6330 W LOOP S RM 1132
BELLAIRE, TX 77401
TESORO PETR CORP,
LOIS DOWNS
300 CONCORD PLAZA DRIVE
SAN ANTONIO, TX 78216-6999
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BOX 25046 MS 914
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C & R INDUSTRIES, INC."
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RUBICON PETROLEUM, llC,
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SIX PINE ROAD
COLORADO SPRINGS, CO 80906
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POBOX 8279 VIKING STN
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TEXACO INC, Portfolio T earn Manager
R W Hill
POBOX 5197x
Bakersfield, CA 93388
H l WANGENHEIM
5430 SAWMILL RD SP 11
PARADISE, CA 95969-5969
MARPLES BUSINESS NEWSLETTER,
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117 W MERCER ST STE 200
SEATTLE, WA 98119-3960
GUESS & RUDD,
GEORGE l YLE
510 l ST, STE 700
ANCHORAGE, AK 99501
TRUSTEES FOR ALASKA,
1026 W. 4th Ave, Ste 201
ANCHORAGE, AK 99501
FOREST Oil,
JIM ARLINGTON
310 K STREET STE 700
ANCHORAGE, AK 99501
)
JERRY HODGDEN GEOl
408 18TH ST
GOLDEN, CO 80401
JOHN A lEVORSEN
200 N 3RD ST #1202
BOISE, ID 83702
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lOS ANGELES, CA 90045-0738
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POBOX 94625
PASADENA, CA 91109
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345 MIDDlEFIElD RD MS 999
MENLO PARK, CA 94025
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SAM VAN VACTOR
POBOX 683
PORTLAND, OR 97207
DEPT OF REVENUE, Oil & GAS AUDIT
DENISE HAWES
550 W 7TH A V STE 570
ANCHORAGE, AK 99501
STATE PIPELINE OFFICE, LIBRARY
KATE MUNSON
411 W 4TH AVE, STE 2
ANCHORAGE, AK 99501
DEPT OF ENVIRON CONSERVATION,
DIV OF AIR & WATER QUALITY
TOM CHAPPLE
555 CORDOVA STREET
ANCHORAGE, AK 99501
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ANCHORAGE, AK 99501
)
NRG ASSOC,
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POBOX 1655
COLORADO SPRINGS, CO 80901-
1655
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630 W 5TH ST
lOS ANGELES, CA 90071
ORO NEGRO, INC.,
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NORTHRIDGE, CA 91324-2410
SHIELDS LIBRARY, GOVT DOCS DEPT
UNIV OF CALIF
DAVIS, CA 95616
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THOR CUTLER OW-137
1200 SIXTH AVE
SEATTlE,WA 98101
FAIRWEATHER E&P SERV INC,
JESSE MOHRBACHER
7151ST #4
ANCHORAGE, AK 99501
DEPT OF ENVIRON CONSERVATION,
DIV OF ENVIRONMENTAL HEALTH
JANICE ADAIR
555 CORDOVA STREET
ANCHORAGE, AK 99501
DUSTY RHODES
229 WHITNEY RD
ANCHORAGE, AK 99501
DEPT OF REVENUE,
CHUCK lOGSTON
550 W 7TH AVE, SUITE 500
ANCHORAGE, AK 99501
DEPT OF REVENUE,
BEVERLY MARQUART
550 W 7TH A V STE 570
ANCHORAGE, AK 99501
ALASKA DEPT OF lAW,
ROBERT E MINTZ ASST A TTY GEN
1031 W 4TH AV STE 200
ANCHORAGE, AK 99501-1994
DEPT OF REVENUE, Oil & GAS AUDIT
FRANK PARR
550 W 7TH AVE STE 570
ANCHORAGE, AK 99501-3540
DEPT OF NATURAL RESOURCES, DIV
OF Oil & GAS
JULIE HOULE
550 W 7TH AVE, SUITE 800
ANCHORAGE, AK 99501-3560
AK JOURNAL OF COMMERCE, Oil &
INDUSTRY NEWS
ROSE RAGSDALE
4220 B Street Ste #210
ANCHORAGE, AK 99501-3560
HDR ALASKA INC,
MARK DALTON
2525 C ST STE 305
ANCHORAGE, AK 99503
BAKER Oil TOOLS, ALASKA AREA
MGR
4710 BUS PK BLVD STE 36
ANCHORAGE, AK 99503
FINK ENVIRONMENTAL CONSULTING,
INC.,
THOMAS FINK, PHD
6359 COLGATE DR.
ANCHORAGE, AK 99504-3305
US BUREAU OF LAND MNGMNT,
ANCHORAGE DIST OFC
DICK FOLAND
6881 ABBOTT lOOP RD
ANCHORAGE, AK 99507
US BlM AK DIST OFC, RESOURCE
EV Al GRP
ART BONET
6881 ABBOTT lOOP RD
ANCHORAGE, AK 99507-2899
)
YUKON PACIFIC CORP,
JOHN HORN VICE CHM
1049 W 5TH AV
ANCHORAGE, AK 99501-1930
GAFO,GREENPEACE
PAMELA MillER
125 CHRISTENSEN DR. #2
ANCHORAGE, AK 99501-2101
DEPT OF NATURAL RESOURCES, DIV
OF Oil & GAS
BRUCE WEBB
550 W 7TH AVE, SUITE 800
ANCHORAGE, AK 99501-3560
DNR, DIV OF Oil & GAS
JAMES B HAYNES NATURAL RESRCE
MGR
550 W 7TH AVE, SUITE 800
ANCHORAGE, AK 99501-3560
DEPT OF NATURAL RESOURCES, DIV
OF OIL & GAS
JIM STOUFFER
550W 7TH AVE, SUITE 800
ANCHORAGE, AK 99501-3560
ANADARKO,
MARK HANLEY
3201 C STREET STE 603
ANCHORAGE, AK 99503
ALASKA OIL & GAS ASSOC,
JUDY BRADY
121 W FIREWEED IN STE 207
ANCHORAGE, AK 99503-2035
ARLEN EHM GEOL CONSl TNT
2420 FOXHAll DR
ANCHORAGE, AK 99504-3342
US BUREAU OF LAND MNGMNT,
ANCHORAGE DIST OFC
PETER J DITTON
6881 ABBOTT lOOP ROAD
ANCHORAGE, AK 99507
UOA/ ANCHORAGE, INST OF SOCIAL
& ECON RESEARCH
TERESA HULL
3211 PROVIDENCE DR
ANCHORAGE, AK 99508
)
PRESTON GATES ELLIS LlP, LIBRARY
420 l ST STE 400
ANCHORAGE, AK 99501-1937
DEPT OF NATURAL RESOURCES,·DIV
OF Oil & GAS
TIM RYHERD
550 W 7th AVE STE 800
ANCHORAGE, AK 99501-3510
DEPT OF NATURAL RESOURCES, DIV
OIL & GAS
WilLIAM VAN DYKE
550 W 7TH AVE, SUITE 800
ANCHORAGE, AK 99501-3560
DEPT OF NATURAL RESOURCES,
PUBLIC INFORMATION CTR
550 W 7TH AVE, SUITE 800
ANCHORAGE, AK 99501-3560
BRISTOL ENVIR SERVICES,
JIM MUNTER
2000 W. INT'L AIRPORT RD #C-1
ANCHORAGE, AK 99502-1116
N-I TUBULARS INC,
3301 C Street Ste 209
ANCHORAGE, AK 99503
ANADRILl-SCHLUMBERGER,
3940 ARCTIC BLVD #300
ANCHORAGE, AK 99503-5711
JAMES E EASON
8611 lEEPER CIRCLE
ANCHORAGE, AK 99504-4209
AMERICA/CANADIAN STRATIGRPH CO,
RON BROCKWAY
4800 KUPREANOF
ANCHORAGE, AK 99507
THOMAS R MARSHALL JR
1569 BIRCHWOOD ST
ANCHORAGE, AK 99508
VECO ALASKA INC.,
f CHUCK O'DONNELL
949 EAST 36TH AVENUE
ANCHORAGE, AK 99508
US MIN MGMT SERV, RESOURCE
STUDIES AK OCS REGN
KIRK W SHERWOOD
949 E 36TH A V RM 603
ANCHORAGE, AK 99508-4302
US MIN MGMT SERV,
FRANK MILLER
949 E 36TH A V STE 603
ANCHORAGE, AK 99508-4363
US MIN MGMT SERV, RESOURCE
EVAL
JIM SCHERR
949 E 36TH A V RM 603
ANCHORAGE, AK 99508-4363
CIRI, LAND DEPT
POBOX 93330
ANCHORAGE, AK 99509-3330
PHILLIPS ALASKA, LEGAL DEPT
MARK P WORCESTER
POBOX 100360
ANCHORAGE, AK 99510-0360
PHILLIPS ALASKA,
JOANN GRUBER ATO 712
POBOX 100360
ANCHORAGE, AK 99510-0360
PHILLIPS ALASKA. KUP CENTRAL
WELLS ST TSTNG
WELL ENG TECH NSK 69
POBOX 196105
ANCHORAGE, AK 99510-6105
US BUREAU OF LAND MGMT, OIL &
GAS OPRNS (984)
J A DYGAS
222 W 7TH AV #13
ANCHORAGE, AK 99513-7599
JODY COLOMBIE
6811 ROUND TREE DRIVE
ANCHORAGE, AK 99516
)
TRADING BAY ENERGY CORP,
PAUL CRAIG
5432 NORTHERN LIGHTS BLVD
ANCHORAGE, AK 99508
US MIN MGMT SERV,
RICHARD PRENTKI
949 E 36TH AV
ANCHORAGE, AK 99508-4302
REGIONAL SUPRVISOR, FIELD
OPERATNS, MMS
ALASKA OCS REGION
949 E 36TH A V STE 308
ANCHORAGE, AK 99508-4363
JOHN MILLER
3445 FORDHAM DR
ANCHORAGE, AK 99508-4555
PHILLIPS ALASKA, LAND MANAGER
JIM RUUD
P.O. BOX 100360
ANCHORAGE, AK 99510
PHILLIPS ALASKA, LAND DEPT
JAMES WINEGARNER
POBOX 10036
ANCHORAGE, AK 99510-0360
PHILLIPS ALASKA,
MARK MAJOR ATO 1968
POBOX 100360
ANCHORAGE, AK 99510-0360
AL YESKA PIPELINE SERV CO,
PERRY A MARKLEY
1835 S BRAGAW - MS 575
ANCHORAGE, AK 99512
ANCHORAGE DAILY NEWS,
EDITORIAL PG EDTR
MICHAEL CAREY
POBOX 149001
ANCHORAGE, AK 99514
JWL ENGINEERING,
JEFF LIPSCOMB
9921 MAIN TREE DR.
ANCHORAGE, AK 99516-6510
)
US MIN MGMT SERV, AK OCS
REGIONAL DIR
949 E 36TH AV RM 110
ANCHORAGE, AK 99508-4302
GORDONJ.SEVERSON
3201 WESTMAR CIR
ANCHORAGE, AK 99508-4336
US MIN MGMT SERV, LIBRARY
949 E 36TH A V RM 603
ANCHORAGE, AK 99508-4363
USGS - ALASKA SECTION. LIBRARY
4200 UNIVERSITY DR
ANCHORAGE, AK 99508-4667
ANCHORAGE TIMES,
BERT TARRANT
POBOX 100040
ANCHORAGE, AK 99510-0040
PHILLIPS ALASKA,
STEVE BENZLER ATO 1404
POBOX 100360
ANCHORAGE, AK 99510-0360
PETROLEUM INFO CORP,
KRISTEN NELSON
POBOX 102278
ANCHORAGE, AK 99510-2278
AL YESKA PIPELINE SERV CO, LEGAL
DEPT '
1835 S BRAGAW
ANCHORAGE, AK 99512-0099
DAVID W. JOHNSTON
320 MARINER DR.
ANCHORAGE, AK 99515
NORTHERN CONSULTING GROUP,
ROBERT BRITCH, P.E.
2454 TELEQUANA DR.
ANCHORAGE. AK 99517
, '
GERALD GANOPOLE CONSULT GEOL
2536 ARLINGTON
ANCHORAGE, AK 99517-1303
DAVID CUSATO
600 W 76TH A V #508
ANCHORAGE, AK 99518
ARMAND SPIELMAN
651 HILANDER CIRCLE
ANCHORAGE, AK 99518
HALLIBURTON ENERGY SERV,
MARK WEDMAN
6900 ARCTIC BLVD
ANCHORAGE, AK 99518-2146
JACK 0 HAKKILA
POBOX 190083
ANCHORAGE, AK 99519-0083
ENSTAR NATURAL GAS CO,
BARRETT HATCHES
POBOX 190288
ANCHORAGE, AK 99519-0288
MARATHON OIL CO, LAND
BROCK RIDDLE
POBOX 196168
ANCHORAGE, AK 99519-6168
UNOCAL,
POBOX 196247
ANCHORAGE, AK 99519-6247
EXXON MOBIL PRODUCTION
COMPANY,
MARK P EVANS
PO BOX 196601
ANCHORAGE, AK 99519-6601
BP EXPLORATION (ALASKA), INC.,
MARK BERLINGER MB 8-1
PO BOX 196612
ANCHORAGE, AK 99519-6612
BP EXPLORATION (ALASKA) INC,
PETE ZSELECZKY LAND MGR
POBOX 196612
ANCHORAGE, AK 99519-6612
BP EXPLORATION (ALASKA) INC, INFO
RESOURCE CTR MB 3-2
POBOX 196612
ANCHORAGE, AK 99519-6612
AMSINALLEE CO INC,
WILLIAM 0 VALLEE PRES
PO BOX 243086
ANCHORAGE, AK 99524-3086
L G POST O&G LAND MGMT CONSULT
10510 Constitution Circle
EAGLE RIVER, AK 99577
D A PLATT & ASSOC,
9852 LITTLE DIOMEDE CIR
EAGLE RIVER, AK 99577
JAMES RODERICK
PO BOX 770471
EAGLE RIVER, AK 99577-0471
COOK INLET KEEPER,
BOB SHA VELSON
PO BOX 3269
HOMER, AK 99603
RON DOLCHOK
POBOX 83
KENAI, AK 99611
DOCUMENT SERVICE CO,
JOHN PARKER
POBOX 1468
KENAI, AK 99611-1468
KENAI PENINSULA BOROUGH,
ECONOMIC DEVEL DISTR
STAN STEADMAN
POBOX 3029
KENAI, AK 99611-3029
)
ASRC,
CONRAD BAGNE
301 ARCTIC SLOPE A V STE 300
ANCHORAGE, AK 99518
OPST AD & ASSOC,
ERIK A OPSTAD PROF GEOL
POBOX 190754
ANCHORAGE, AK 99519
MARATHON OIL CO, OPERATIONS
SUPT
W.C. BARRON
POBOX 196168
ANCHORAGE, AK 99519-6168
UNOCAL,
KEVIN TABLER
POBOX 196247
ANCHORAGE, AK 99519-6247
BP EXPLORATION (ALASKA) INC,
SUE MILLER
POBOX 196612 MIS LR2-3
ANCHORAGE, AK99519-6612
BP EXPLORATION (ALASKA) INC,
MR. DAVIS, ESQ
POBOX 196612 MB 13-5
ANCHORAGE, AK 99519-6612
PINNACLE,
STEVE TYLER
20231 REVERE CIRCLE
EAGLE RIVER, AK 99577
DEPT OF NATURAL RESOURCES,
DGGS '
JOHN REEDER
POBOX 772805
EAGLE RIVER, AK 99577-2805
PHILLIPS PETROLEUM CO, ALASKA
OPERATIONS MANAGER
J W KONST
P 0 DRAWER 66
KENAI, AK 99611
NANCY LORD
PO BOX 558
HOMER, AK 99623
f '
PENNY VADLA
POBOX 467
NINILCHIK, AK 99639
PACE,
SHEILA DICKSON
POBOX 2018
SOLDOTNA, AK 99669
AL YESKA PIPELINE SERVICE CO,
VALDEZ CORP AFFAIRS
SANDY MCCLINTOCK
POBOX 300 MS/701
VALDEZ, AK 99686
UNIV OF ALASKA FAIRBANKS, PETR
DEVEL LAB
DR V A KAMATH
427 DUCKERING
FAIRBANKS, AK 99701
C BURGLlN
POBOX 131
FAIRBANKS, AK 99707
K&K RECYCL INC,
POBOX 58055
FAIRBANKS, AK 99711
UNIV OF ALASKA FBX, PETR DEVEL
LAB
SHIRISH PATIL
437 DICKERING
FAIRBANKS, AK 99775
DEPT OF ENVIRON CONSERV SPAR,
CHRIS PACE
410 WILLOUGHBY AV STE 105
JUNEAU, AK 99801-1795
)
BELOWICH,
MICHAEL A BELOWICH
1125 SNOW HILL AVE
WASILLA, AK 99654-5751
KENAI NATL WILDLIFE REFUGE,
REFUGE MGR
POBOX 2139
SOLDOTNA, AK 99669-2139
VALDEZ VANGUARD, EDITOR
POBOX 98
VALDEZ, AK 99686-0098
RICK WAGNER
POBOX 60868
FAIRBANKS, AK 99706
FRED PRATT
POBOX 72981
FAIRBANKS, AK 99707-2981
ASRC,
BILL THOMAS
POBOX 129
BARROW, AK 99723
UNIVERSITY OF ALASKA FBKS, PETR
DEVEL LAB
DR AKANNI LAWAL
POBOX 755880
FAIRBANKS, AK 99775-5880
/. /i
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JAMES GIBBS
POBOX 1597
SOLDOTNA, AK 99669
VALDEZ PIONEER,
POBOX 367
VALDEZ,AK 99686
NICK STEPOVICH
543 2ND AVE
FAIRBANKS, AK 99701
FAIRBANKS DAILY NEWS-MINER,
KATE RIPLEY
POBOX 70710
FAIRBANKS, AK 99707
DEPT OF NATURAL RESOURCES, DIV
OF LAND
REG MGR NORTHERN REGION
3700 AIRPORT WAY
FAIRBANKS, AK 99709-4699
RICHARD FINEBERG
PO BOX 416
ESTER, AK 99725
SENATOR LOREN LEMAN
STATE CAPITOL RM 113
JUNEAU, AK 99801-1182
STATE OF ALASKA
ALASKA OIL AND GAS CONSERVATION COMMISSION
333 West 7th Avenue, Suite 100
Anchorage Alaska 99501
Re: THE APPLICATION OF )
Area Injection Order No. 21.001
CONOCO PHILLIPS ALASKA, )
INC. for an order allowing )
Kuparuk River Field
underground injection of fluids for )
Meltwater Oil Pool
enhanced oil recovery in the )
Meltwater Oil Pool, in the Meltwater )
October 4, 2012
Participating Area, Kuparuk River )
Field, North Slope, Alaska
By letters dated September 25, 2012, ConocoPhillips Alaska Inc. (CPAI) requests administrative
approval for two injection wells in the Kuparuk River Unit (KRU) Meltwater Oil Pool to allow
the continued injection of miscible injectant (MI) with the outer casing annulus indicating re -
pressurization after pressure bleeds. The Alaska Oil and Gas Conservation Commission
(AOGCC) is returning CPAI's administrative approval requests without action, and on its own
motion is hereby administratively amending Area Injection Order (AIO) 021.000, Rule 2 to
include an injection pressure limit. This approval authorizes the continued injection of MI into
the Meltwater Oil Pool for enhanced oil recovery purposes until such time as additional AIO
21.000 amendments have been considered by the AOGCC.
Rule 2 ("Fluid Injection Wells") is hereby amended to read as follows:
The underground injection of fluids must be through a well permitted for drilling as a
service well for injection in conformance with 20 AAC 25.005, or through a well
approved for conversion to a service well for injection in conformance with 20 AAC
25.280. Surface injection pressure shall be limited to 2600 psi.
Motivating this amendment and efforts further to revise AIO 21.000 are two issues: indications
of MI migrating out of the authorized injection zone as defined and described in the AIO, and
elevated outer annulus pressures in Meltwater Oil Pool injection and producing wells.
MI Migration out of the Injection Zone. Interpreted seismic data provided by CPAI shows the
existence of vertical fractures that are consistent with the bottomhole location of Meltwater Oil
Pool injection wells. Based on the results and interpretation of the seismic, vertical fractures
appear to have allowed MI to migrate above the injection zone. In response, CPAI has imposed
a wellhead injection pressure limit on Meltwater Oil Pool injection wells to ensure the injection
pressure at the sand face is less than 3400 psi, which corresponds to a pressure less than the leak -
off test data gathered after drilling out of the production casing (top -sets the injection
zone/producing horizon). As noted in AIO 21.000, there are no potential underground sources of
drinking water in the Meltwater Oil Pool area.
Elevated Outer Annulus Pressures. With the restricted injection pressure, data provided by CPAI
indicates that the outer annulus pressure in wells has declined. Where pressures remain, the rate
of pressure build-up in the outer annulus is manageable with periodic pressure bleeds.
AIO 21.001
October 4, 2012
Page 2 of 2
Effective immediately the following additional conditions are imposed:
1. CPAI shall record wellhead pressures and injection rates daily;
2. CPAI shall submit to the AOGCC a monthly report detailing the daily monitoring of
all Meltwater Oil Pool wells. Included in the monthly report CPAI shall submit OA
fluid levels, well pressures, injection and/or production rates, and pressure bleeds for
all annuli. Trends shall be evaluated and detailed;
3. CPAI shall limit the outer annulus pressure to 1000 psi;
4. CPAI shall immediately shut in any well indicating a change in its mechanical
condition;
5. CPAI shall immediately notify AOGCC when a well is shut in for mechanical
integrity reasons; and
6. After well shut in due to a change in the well's mechanical condition, AOGCC
approval shall be required to restart injection.
The AOGCC has scheduled a hearing on November 8, 2012 at 9:00am to consider the need for
additional amendments to AIO 21.000.
This Administrative Amendment will not promote waste or jeopardize correlative rights, is based
on sound engineering and geoscience principles and will not result in an increased risk of fluid
movement into a USDW.
DONE at Anchorage, Alaska and dated October 4,
Cathy . Foerster Daniel T. Seamount,
Chair, Commissioner Commissioner
As provided in AS 31.05.080(a), within 20 days after written notice of the entry of this order or decision, or such further ti as \,
AOGCC grants for good cause shown, a person affected by it may file with the AOGCC an application for reconsiderati o
maner determined by it. If the notice was mailed, then the period of time shall be 23 days. An application for reconsiderat n
set out the respect in which the order or decision is believed to be erroneous.
The AOGCC shall grant or refuse the application for recomidermion in whole or in part within 10 days after it is filed. Failure
on it within 10 -days is a denial of reconsideration. If the AOGCC denies reconsideration, upon denial, this order or decision sn
TION a
denial of reconsideration are FINAL and may be appealed to superior court. The appeal MUST be filed within 33 days after the dot
on which the AOGCC mails, OR 30 days if the AOGCC otherwise distributes, the order or decision denying reconsideration,
UNLESS the denial is by inaction, in which ease the appeal MUST be filed within 40 days after the date on which the application for
reconsideration was filed.
If the AOGCC grants an application for reconsideration, this order or decision does not become final. Rather, the order or decision on
reconsideration will be the FINAL order or decision of the AOGCC, and it may be appealed to superior court. That appeal MUST be
filed within 33 days after the date on which the AOGCC mails, OR 30 days if the AOGCC otherwise distributes, the order or decision
on reconsideration. As provided in AS 31.05.080(6), "[tlhe questions reviewed on appeal are limited to the questions presented to the
AOGCC by the application for reconsideration."
In computing a period of time above, the date of the event or default after which the designated period begins to ran is not included in
the period; the last day of the period is included, unless it falls on a weekend or state holiday, in which event the period runs until 5:00
Wallace, Chris D (CED)
From: Rodgers, James T <James.T.Rodgers@conocophiIli ps.com>
Sent: Friday, September 21, 2012 10:09 AM
To: Wallace, Chris D (DOA)
Subject: RE: Meltwater Update
Chris, in response to your second paragraph, I assume being prompted by the question in our 9/18 meeting from Jim
Regg asking why we currently had no Administrative Approvals (AA) for existing Meltwater injectors, following is our
response.
Meltwater's Area Injection Order (AIO) 21 is different from all our other Operated Asset's AIOs. It does not require or
imply that CPAI needs Administrative Approval (AA) to operate the two injection wells that have outer annulus pressure
(let alone all five Meltwater injection wells). I understand that Tom Maunder discussed this with the Well Integrity Team in
the early days; however, they have found no written documentation of those conversations. Consequently, in answer to
Mr. Regg's question, in the AIO's current state, no AA's should be required for Meltwater injection wells with pressure on
the casing by casing annulus; therefore, CPAI has been operating these injection wells in compliance with that aspect of
the AIO.
Please let me know if you have any other questions.
James Rodgers
From: Wallace, Chris D (DOA) [mailto:chris.wallace@alaska.gov]
Sent: Wednesday, September 19, 2012 8:47 AM
To: Rodgers, James T
Subject: (EXTERNAL]RE: Meltwater Update
James,
Thanks to you and your team. I appreciated the open candid discussion and sharing of information, and was
pleased that you were able to address our concerns/topics. 1 feel we have re-established a foundation of
understanding and look forward to getting the orders in line to reflect our latest thinking and path forward.
You mentioned that there has been some correspondence relating to Administrative
Approvals/waivers/agreements for the operation and monitoring of the wells in the recent past. If you have that
please send as it is unfortunately not captured in our files.
Thanks and Regards,
Chris Wallace
Sr. Petroleum Engineer
Alaska Oil and Gas Conservation Commission
333 West Th Avenue
Anchorage, AK 99501
(907) 793-1250 (phone)
(907) 276-7542 (fax)
chris.wallaceR alaska.gov
From: Rodgers, James T [mailto:James.T.Rodgers@conocophillips.com]
Sent: Wednesday, September 19, 2012 8:30 AM
To: Wallace, Chris D (DOA)
Subject: RE: Meltwater Update
Chris, l wanted to thank you and your Team for our meeting yesterday afternoon. 1 am very happy that it turned into more of a
working meeting with a sharing of ideas. It was a huge help to us to better understand all the different perspectives regarding
our plans going forward. The Meltwater Team will work diligently to amend the AIO. Appreciate it
James Rodgers
ConocoPhillips
Alaska
P.O. BOX 100360
ANCHORAGE, ALASKA 99510-0360
September 25, 2012
Commissioner Dan Seamount
Alaska Oil and Gas Conservation Commission
333 West 7°1 Avenue, Suite 100
Anchorage, AK 99501
Dear Commissioner Seamount:
Enclosed please find the request for Administrative Action per Rule 6 in Area Injection
Order 21 on Meltwater injection well 2P-434 (PTD 203-153).
Please call Martin Walters or me at 659-7043 if you have any questions.
Sincerely,
lei
MJ Lo4and
ConocoPhillips
Well Integrity Projects Supervisor
Enclosures
ConocoPhillips Alaska, Inc.
Kuparuk River Field, Meltwater Oil Pool
2P-434 (PTD# 203-153)
Technical Justification for Administrative Action Request
Purpose
ConocoPhillips Alaska, Inc. proposes that the Alaska Oil and Gas Conservation Commission
(AOGCC) approve this Administrative Action (AA) request as per Area Injection Order (AIO)
21, Rule 6. Meltwater injection well 2P-434 (PTD# 203-153) is currently operating in
compliance with AIO 21; however the AA per Rule 6, will allow additional monitoring by the
AOGCC for historic elevated outer annulus (OA) pressure on this well.
Well History and Status
Meltwater injection well 2P-434 (PTD# 203-153 was drilled and completed on Jan 1, 2004 as a
water alternating gas (WAG) enhanced oil recovery (EOR) service well. It was placed on
produced water injection in February 2004 and passed a subsequent state witness mechanical
integrity test (MIT). The well was operated with WAG cycles until August 2007 when it was
shut in.
Elevated OA pressure above 1000 psi from the open OA shoe was reported to the AOGCC on
April 12, 2004. Due to the language currently written in AIO 21 Administrative Action is not
implied or required. In the time since the well has been shut in the OA pressure has dropped
below 100 psi (see attached).
The well has maintained tubing, packer, and production casing integrity as shown by the passing
4 year MIT's and pressure trend plots.
Barrier and Hazard Evaluation
Tubing. The 3-1/2", 9.3#, L-80 tubing has integrity to Baker Seal assembly @ 5538' MD (5141'
TVD), based on the passing MITIA completed on 08/08/10 and historic pressure trends.
Production: casing. The 7", 26#, L-80 production casing has an internal yield pressure rating of
7240 psi has integrity to the packer @ 5538' MD (5141' TVD) based upon historic pressure
trends and MITIA's.
Surface casing: The 9-5/8", 40#, L-80 surface casing with an internal yield pressure rating of
5750 psi set at 2421' MD (2356' TVD) has an open OA shoe, however has historically held
elevated pressure showing casing integrity at that time.
Primary barrier: The primary barrier to prevent a release from the hydrocarbon producing
formation in this well is the production tubing.
Second barrier: The secondary barrier to prevent a release from the hydrocarbon producing
formation in this well is the production casing envelope should the production tubing fail.
Well Integrity Project Supervisor 9/24/2012
Monitoring
Each well is monitored daily for wellhead pressure changes. Should leaks develop in the tubing
or surface casing above the conductor shoe it will be noted during the daily monitoring process.
Any deviations from approved allowable operating annular and or injection pressures require
investigation and corrective action, up to and including a shut-in of the well. T/I/O plots are
compiled, reviewed, and submitted to the AOGCC for review on a monthly basis.
Proposed Operating and Monitoring Plan
1. Well will be used for MI or wag (if water becomes available) injection;
2. OA will be monitored daily and recorded for trending,
3. Monthly OA fluid levels
4. Perform an MITIA every four years;
5. Submit monthly reports of daily tubing, IA, OA pressures, injection volumes, and any OA
bleeds;
6. Notify AOGCC and take appropriate action should the MIT, injection rates, or pressures
indicate well integrity issues.
Well Integrity Project Supervisor 9/24/2012
OHUKt VIF
FTT IAP
-- - OAP
TWO Plot - 2P-434
200
3000 .... ... ............ .................................................. ........ 150
2000 100
E
a
JJIIJJII'' m
Fn' .... ... .. .. .. ......... .IY �illhl ..... .................
1000 t !
9
01 -Jan -05 01 -Jan -07 01 -Jan -09 01 -Jan -11
Date
50
STATE OF ALASKA
ALASKA OIL AND GAS CONSERVATION COMMISSION
Mechanical Integrity Test
Email to:(im.regg@alaska.gov; phcebe.brooks@alaska.gov; tron.maunder@alaska.gov; doa.aogcc.prudhoe.bay@alaska.gov
OPERATOR:
ConocoPhillips Alaska Inc.
FIELD / UNIT / PAD:
Kuparuk / KRU / 2P
DATE:
08/08/10
OPERATOR REP:
Colee / Coleman - AES
AOGCC REP:
Robert Noble
TYPE INJ Codes
TYPE TEST Codes
D = Drilling Waste
Packer Depth
G = Gas
Pretest
Initial
15 Min.
30 Min.
A= Temperature Anomaly Survey
W = Water
Well
2P-419
Type In'.
G
TVD
5,202'
Tubin
3,700
3,700
3,700
3,700
Interval
4
P.T.D.
2040170
Type test
P
Test si
1500
Casin
2,716
3,300
3,260
3,260
PIF
P
Notes:
I
OAJ
291 1
335 1
338 1
336
Weil
2P-420
1 Type In'.
I G
I TVD
1 5,428' 1
Tubing!
3,0501
1
3.0501
Interval
4
P.T.D.
2011820
I Typetest
I P
I Test pall
1600 1
Casingi
1,8501
1
1
1,7691
PIF
I F
Notes: Pumped 13bbls. With no pressure increase.
I
OAl
2911
1
1
275
Wel12P-427
Type ln'.
G
TVD
5,455'
Tubin
3,100
3,100
3,100
3,100
Inlerval
4
P.T.D.
2020180
Type lest
P
Test pail1500
Casin
1,925
2,600
2,520
2,520
P/F
P
Notes:
I
OAJ
6751
6761
676[_676
Well
2P-429
I Type In'.
N
1 TVD
1 5,218' 1
Tubingl
910
910 1
910 1
910 1
Interval
4
P.T.D.
2011020
I Type test
P
I Test psil
1500 1
Casingi
435
1,820 1
1,770 1
1,760 1
P/Fl
P
Notes:
I
OAJ
10 1
442 1
349 1
339
We112P-434
T eln.
N
TVD
5129'
Tubin
1,625
1,625
1,625
1,625
Interval
4
P. T.D.
2031530
Type test
P
Test pail1500
Casin
5
2,390
2,290
2280
PIF
P
Notes:
I
OAI
1001
1011
1011
101
WeII2P-447
Type Ini.
G
TVD
1 5,226'1
Tubingi
3.5001
3,5001
3,5001
3.5001
Interval
4
P.T.D.2031540
Type test
P
I Test pail
1500
Casingi
2401
1,8401
1.8101
1,810
P/FI
P
Notes:
I
OAI
11751
11761
11951
1201
Well
T e In'.
TVD
Tubin
Interval
P.T.D.
Type test
Test psil
I
Casingi
I
I
IP!F
Notes:
I
OA
Well
T e In'.
1 TVD
I I
TubingI
I
Interval
P.T.D.
T atest
Test pail
I
Casingi
I
PIF
Notes:
I
OA
TYPE INJ Codes
TYPE TEST Codes
D = Drilling Waste
M = Annulus Monitoring
G = Gas
P = Standard Pressure Test
I = Industrial Wastewater
R = Internal Radioactive Tracer Survey
N = No! Injecting
A= Temperature Anomaly Survey
W = Water
D = Differential Temperature Test
MIT Report Form
BFL 11/27/07 MIT KRU 2P Pad 08-08-10.zls
INTERVAL Codes
I = Initial Test
4 = Four Year Cycle
V = Required by Variance
T = Test during Workover
O = Other (describe in notes)
KUP 2P-434
ConocoPhillips Well Attributes TMe%r,AnLfOgIB8,MD TD
\I w.naonsenuwi e.m x.m. vi.0 sum. m. ^�ORB� Ptl Bim'XNB�
Itflfl,
SSt5d Ot5�
14 BOYJ
ConocoPhillips
Alaska
P.O. BOX 100360
ANCHORAGE, ALASKA 99510-0360
September 25, 2012
Commissioner Dan Seamount
Alaska Oil and Gas Conservation Commission
333 West 7°i Avenue, Suite 100
Anchorage, AK 99501
Dear Commissioner Seamount:
Enclosed please find the request for Administrative Action per Rule 6 in Area Injection
Order 21 on Meltwater injection well 2P-447 (PTD 203-154).
Please call Martin Walters or me at 659 7043 if you have any questions.
Sincerely,
,- 4,��r��G_,�
MJ Loveland
ConocoPhillips
Well Integrity Projects Supervisor
Enclosures
ConocoPhillips Alaska, Inc.
Kuparuk River Field, Meltwater Oil Pool
2P-447 (PTD# 203-154)
Technical Justification for Administrative Action Request
Purpose
ConocoPhillips Alaska, Inc. proposes that the Alaska Oil and Gas Conservation Commission
(AOGCC) approve this Administrative Action (AA) request as per Area Injection Order (AIO)
21, Rule 6. Meltwater injection well 2P-447 (PTD# 203-154) is currently operating in
compliance with AIO 21; however the AA per Rule 6, will allow additional monitoring by the
AOGCC for historic elevated outer annulus (OA) pressure on this well.
Well History and Status
Meltwater injection well 2P-447 (PTD# 203-154) was drilled and completed on February 6, 2004
as a water alternating gas (WAG) enhanced oil recovery (EOR) service well. This well has had
cement pumped down the OA by the drilling rig to improve the cement bond on the production
casing. Subsequently the OA can no longer be pumped into however the shoe still leaks. The
well was placed on produced water injection in February 2004 and passed a subsequent state
witness mechanical integrity test (MIT). The well was operated with WAG cycles until June
2010 at which time gas became the only fluid available for injection. Currently 2P-447 is shut
in for reservoir management, however may be returned to service in the future.
Elevated OA pressure above 1000 psi from the leaking OA shoe was reported to the AOGCC on
March 30, 2004. Due to the language currently written in AIO 21, Administrative Action is not
implied or required.
Recently the Meltwater injection/withdrawal operating principles were changed to a lower
injection pressure and a lower injection/withdrawal ratio (I/W). Since that change the OA
pressure has dropped below 500 psi.
The well has maintained tubing, packer, and production casing integrity as shown by the passing
4 year MIT's and pressure trend plots (see attached).
Barrier and Hazard Evaluation
Tubing. The 3-1/2", 9.3#, L-80 tubing has integrity to Baker Seal assembly @ 7429' MD (5232'
TVD), based on the passing MITIA completed on 08/08/10 and historic pressure trends.
Production casing. The 7", 26#, L-80 production casing has an internal yield pressure rating of
7240 psi has integrity to the packer @ 7429' MD (5305' TVD) based upon historic pressure
trends and MITIA's.
Surface casing: The 9-5/8", 40#, L-80 surface casing with an internal yield pressure rating of
5750 psi set at 2705' MD (2318' TVD) has a leaking OA shoe, however has historically held
elevated pressure showing casing integrity.
Primary barrier: The primary barrier to prevent a release from the hydrocarbon producing
formation in this well is the production tubing.
Second barrier: The secondary barrier to prevent a release from the hydrocarbon producing
formation in this well is the production casing envelope should the production tubing fail.
Well Integrity Project Supervisor 9/24/2012
Monitoring
Each well is monitored daily for wellhead pressure changes. Should leaks develop in the tubing
or surface casing above the conductor shoe it will be noted during the daily monitoring process.
Any deviations from approved allowable operating annular and or injection pressures require
investigation and corrective action, up to and including a shut-in of the well. T/I/O plots are
compiled, reviewed, and submitted to the AOGCC for review on a monthly basis.
Proposed Operating and Monitoring Plan
1. Well will be used for MI or wag (if water becomes available) injection;
2. OA will be monitored daily and recorded for trending,
3. Monthly OA fluid levels
4. Perform an MITIA every four years;
5. Submit monthly reports of daily tubing, IA, OA pressures, injection volumes, and any OA
bleeds;
6. Notify AOGCC and take appropriate action should the MIT, injection rates, or pressures
indicate well integrity issues.
Well Integrity Project Supervisor 9/24/2012
- CHOKE FTP
— — FTT IAP TWO Plot - 2P-447
OAP 200
3000 p ................... 1a. ,:: I;. _.............................,. _ ... _..
2500.............................................................................. ......
150
2000 .. .............................................. ......................... ...... a
E
m
an 100
1500 ........w.......... ..... r
' U
1000 ........... ........ ,r.` ................
500...................................................I..........' .............. ... I...�:
0 T i i t m 4 1 a 1 I ' 0
01 -Oct -11 01 -Dec -11 01 -Feb -12 01 -Apr -12 01 -Jun -12 01 -Aug -12
Date
CHOKE - - FTP
FTT IAP
-- OAP
3500 ...........................
TWO Plot - 2P-447
�I ............................
...
200
3000 ....................
.� .
150
2500 { .. .....
...... .
2000
.. ..
1 .
...
t
M
100
�.
1500
.
...
u
1000 ....
I I
i
.... ..
.. ......
50
i
500
y. .
.. .. .,..
0
0
01-Jan-05
01-Jan-07 01-Jan-09
01-Jan-11
Date
STATE OF ALASKA
ALASKA OIL AND GAS CONSERVATION COMMISSION
Mechanical Integrity Test
Email lo:jim.regg@alaska.gov; phoebe.brooks@alaska.gov; tom.maunder@alaska.gov; doa.aogcc.prudhoe.bay@alaska.gov
OPERATOR:
ConocoPhillips Alaska Inc.
FIELD I UNIT I PAD:
Kuparuk / KRU / 2P
DATE:
08/08/10
OPERATOR REP:
Colee / Coleman - AES
AOGCC REP:
Robert Noble
TYPE INJ Codes
TYPE TEST Codes
0 = Drilling Waste
Packer Depth
G = Gas
Prates(
Initial
15 Min.
30 Min.
A= Temperature Anomaly Survey
W = Water
Well 2P-419
Type In'.
G
TVD
5,2024"1Tubin
3,700
3,700
3,700
3,700
Interval
4
P.T.D. 2040170
Type tesl
P
Test pail1500
Casin
2,718
3,300
3,260
3,260
PIF
P
Notes:
I
OAI
291 1
335 1
338 1
336
Well
2P-420
I Type In'.
I G
I TVD
1 5,428' 1
Tubingl
3.0501
Interval
4
P.T.D.
2011820
I Type test
I P
I Test pail
1500 1
Casingi1,850
1,769
PIF
F
Notes: Pumped 13bbis. With no pressure increase.
I
OAJ
2911
275
Well 2P-427
Type In'.
G
TVD
5,455'
Tubin
3,100
3,100
3,100
3,100
Interval
4
P.T.D. 2020180
Type test
P
I Test psil
1500
Casin
1,925
2,600
2,520
2,520
PIF
P
Notes:
I
OAJ
6751
6761
6761
676
Well
2P-429
1 Type In'.
1 N
TVD
1 5,218' 1
Tubing[
910 1
910
910 1
910
1 Interval
4
P.T.D.2011020
I Type test
P
Test pail
1500 1
Casingi435
1,820
1,770
1,760
PIF
P
Notes:
I
OAI
310 1
442
349 1
339
Well
2P-434
T e In'.
N
TVD
5,129'
Tubin
1,625
1,625
1,625
1,625
Interval
4
P.T.D.
2031530
Type tesf
P
Test si
1500
Casin
5
2,390
2,290
2,280
PIF
P
Notes:
I
OAI
1001
loll
loll
101
WeII2P-447
1T eln'.
G
TVD1
5.226'1
Tubingj
3.5001
3,500
3,500
3,500
Interval
4
P.T.D.
2031540
I Typetest
P
Test pail
15001
Casingi
240
1.840
1,810
1,810
PIF
P
Notes:
I
QAJ
11751
11761
11951
1201
Well
Type ln.
TVD
Tubing!Interval
P.T.D.
Type testj
I Test psi
I
Casin
PIF
Notes:
I
GA
Weill
I TyeeIn'.
TVD
I I
Tubingj
Interval
P.T.D.
T etest
Testpsi[
Casing[
P/F
Notes
I
OA
TYPE INJ Codes
TYPE TEST Codes
0 = Drilling Waste
M = Annulus Monitoring
G = Gas
P = Standard Pressure Test
I = Industrial Wastewater
R = Internal Radioactive Tracer Survey
N = Not Injecting
A= Temperature Anomaly Survey
W = Water
D = Differential Temperature Test
MIT Report Form
BFL 11/27/07 MIT KRU 2P Pad 08-08-10.xis
INTERVAL Codes
I = Initial Test
4 = Four Year Cycle
V = Required by Variance
T = Test during Workover
O = Other (describe in notes)
ConoctiPhillips
AL,r,,, In
IngR
I r ema�_
less S
KUP
2P-447
Wetl Attributes Max An le & MD TO
4Ye11bare APINV/1 Fleltl Wme
501032046800 "'M'ATER
VJeII Slalua Inel14'1 MD 18 IS Act BIm Ifln.)
INJ 59.82 ],682.99 8,0150
crimmem X]s 1pPml pee Ars. bn
SSSV: NIPPLE Lasl WO:
fns inn. Keunt, I Rly S. ....le
2798 1nN2004
Mnm.nen pepin InKe) ane pne ---------L..t
List1 :SW ],6]1.0 l=009 Rev Reason:REMSECSGID
nme._ Ena Dae
nnan 8152012
Casin Strin a
Caeme N...lpnen string 9...
CONDUCTOR 16
suing -
15062
Toploxal s.1 Dept 11- set D.0 1-. 9trluewl..' Dine... stanSTap Na
30.0 108.0 IWO 62.50 H40 VIEWED
Caang Deaeapllon Suing O...
SURFACE 958
String III
8.835
TopinKBl SnOvish 1.,. Sa DePtn(Np1- slruggs.. Shing- Suns Trip TMa
28.1 2,705.6 2,318.0 40.00 L -W BTC
Canns De¢apllan suing O..,
INTERMEDIATE 7
liul,g...
6.2]6
T,MBI Set DMIRR Sel DrPihRMR- SRw,W.... .M1in,... Suing Trip TNa
25.2 7,562.0 5,305.9 am LEO BTC -W
Caslne IN -upon sung O...
LINER 312
sing ID._
2.992
Top lnKBl Set Depinll-Set DMbRW))- Sus'sa... Slang... Suing Tap Tura
],4155 8,010.0 5,546.3 9.30 L-60 SIM
Line, Details
Tep Nplu
ITVDI Tori nom!...
Top (1DtB IRKS) li Ium Dndlpbn Crimsem IDhn)
7,415.5 5,2262 5540 PACKER ZKP HR LINER TOP ISOLATION PACKER YJRIE BACK 4.73
9,434.4 6.23561 55]ONIPPLE RS PACKOFF SEAL NIPPLE 4.250
],43].2 5,23].3 55]6 HANGER BAKER FLEXLOCK LINER HANGER 5.000
), 4 S 5,242.8 55.99 SBE BAKER 8040
]465.7 b,25Lllj CROSSOVER BUSHING 3000
Tobin SVin a
TUElne baotlptim set DeNM1 n... set Depinlrvp)... going Wb.. 9ul-1 SDMa Trip TMa
"14-1SUNg10... TI -3N
13"14-112
TUBING 4 ill 3.958 23.0 ],468.0 5,251.0 12.1 LEO IBT-M
Com letion Details
Trip(9epm
JDD) Tripmn xriml...
To nne nt I') lam osecn non comment I011nl
23.0 23.0 -840 HANGER --- -- 4.500
5027 502.5 4.98 NIPPLE CAMCO NO GO'OB' NIPPLE a875
],365.] 5,197.0 M.27 SLEEVE BAKER CMU SLIDING SLEEVE ud3SIT OBPROFILE 3.9-15
-aa7-W
7.3824 5807.0 51.65 MPPLE CAMCO'DE' NIPPLE 11:3.]5- N0 G0PR0FILE
7.428.1 5.2!1.9 5555 LOCATOR G -U LOCATOR 3.010
7,429.3 5232.6 55.50EALASSV BAKER8040 SEAL w1112 MInESHOE 3.98" x 3.W TWO
Perforations & Slots
sm
TppnW) elm RVDI D.n.
Tri Me atm nxa Inxe) InKe) Zone Daro tem.. T cammeM
7,600 ],640 5,3254 5,315.)T -32P -M) ai(NW 6.0 APERF 2.0 "SD PJ Cmgs. SO Me Ines.
)100 7,]80 5,3]5.] 5419.OT-3, W447 2n1 601PERF 2.SHSDPJr;MiSw0egpnlue
),) 7, 5,4]9.0 5429.9 T-3, 2P-041 25(Xxl1 1 6,01IPERF 2.9'H30 PJ Chrys,Wdeg phase
Notes: General & Safety
ane Deu AnRW
VEREDOA: PSURE CHARGING FROM R RESERVOIR
6N42W1 NOTE: WARES
1252W8 Imul E: VIEW SCHEMATIC sh"ISSie SUtemllic9.0
Mandrel Details
Sm To RKI
Top Depth
Irvol
pIKB)
Tep
mel
I')
M.Me
Mritlel
op
Pnl
9ury
vnn
Type
c.mn
TYp.
von
eIn
(I -I
rao aun
IWURun
Dae
Cam...
1 ],316.2
5,1889
5403.
CAMCO
KB 62
1
Gas LIB
pM V
BK
0=
80
12)
X12
,~ R~~~~
Q ~ 1, A~ ~~ l %; I.
{asks Oil ~ G«~ ~~r~~: ~~rrrlrrlissl~~
ConocoPhillips
David Jamieson ~r9f,l~`s`~~~
Supervisor, GKA Reservoir Planning
Greater Kuparuk Area
ConocoPhillips Alaska Inc.
ATO-1320
PO Box 100360
Anchorage AK 99510-0360
Phone: (907) 263-4027
Fax: (907) 265-6133
December 21, 2009
Dan Seamont, Commissioner
Alaska Oil and Gas Conservation Commission
333 West 7'" Ave. Suite #100
Anchorage, Alaska 99501-3539
RE: Cessation of Water Injection at Meltwater
Dear Mr. Seamont,
This letter is to inform the Alaska Oil and Gas Conservation Commission that water injection ceased
in the Meltwater Field on October 15, 2009. On this date, the water injection pipeline to the
Meltwater field was declared unsuitable for continued operation due to internal corrosion. Miscible
gas injection continues to maintain a voidage balance with production in the field.
As of October 15, 2009, approximately 37 BSCF of miscible gas had been injected in the Meltwater
Field compared with the target volume in Area Injection Order No. 21 of 46 BSCF. This represents
a pore volume slug of 17% of the 132 MMBO of initial oil in place, compared with the target slug size
of 20% as stated in Area Injection Order No. 21.
At this time, there are no near-term plans to restore water injection service to Meltwater.
ConocoPhillips does not anticipate any recovery impacts as little or no reservoir pressure support
has been observed to date from water injection, however some response to gas injection has been
observed. Studies are ongoing to determine the future development options for the highly
compartmentalized Meltwater field in light of the recent de-rated water injection pipeline.
ConocoPhillips expects to complete these studies by Q3 2010 and will update the AOGCC in 04
2010.
If you have any questions concerning this, please contact Adam Lewis at 265-6362 or Michael Braun
at 263-4185.
Sincerely,
~--
Davi amieson
Supervisor, GKA Reservoir Planning
Greater Kuparuk Area
cc: Mr. Warwick King, CPAI
Mr. James Rodgers, CPAI
Mr. Darron Jackson, CPAI
Mr. Paul Wharton, CPAI
Mr. Don Dunham, BPXA
Mr. Glenn Fredrick, Chevron
Mr. Dale Pittman, ExxonMobil
#11
17
FRANK H. MURKOWSK/, GOVERNOR
Li
KA OIL AND GAS
333 W. 7TM AVENUE, SUITE 100
CONSERVATION COMMISSION
ANCHORAGE, ALASKA 99501-3539
PHONE (907) 279-1433
FAX (907) 276-7542
September 27, 2004
Proposals to Amend Underground Injection Orders to Incorporate
Consistent Language Addressing the Mechanical Integrity of Wells
The Alaska Oil and Gas Conservation Commission ("Commission"), on its own motion,
proposes to amend the rules addressing mechanical integrity of wells in all existing area injection
orders, storage injection orders, enhanced recovery injection orders, and disposal injection
orders. There are numerous different versions of wording used for each of the rules that create
confusion and inconsistent implementation of well integrity requirements for injection wells
when pressure communication or leakage is indicated. In several injection orders, there are no
rules addressing requirements for notification and well disposition when a well integrity failure
is identified. Wording used for the administrative approval rule in injection orders is similarly
inconsistent.
The Commission proposes these three rules as replacements in all injection orders:
Demonstration of Mechanical Integrity
The mechanical integrity of an injection well must be demonstrated before injection
begins, at least once every four years thereafter (except at least once every two years in
the case of a slurry injection well), and before returning a well to service following a
workover affecting mechanical integrity. Unless an alternate means is approved by the
Commission, mechanical integrity must be demonstrated by a tubing/casing annulus
pressure test using a surface pressure of 1500 psi or 0.25 psi/ft multiplied by the vertical
depth of the packer, whichever is greater, that shows stabilizing pressure and does not
change more than 10 percent during a 30 minute period. The Commission must be
notified at least 24 hours in advance to enable a representative to witness mechanical
integrity tests.
Well Integrity Failure and Confinement
Whenever any pressure communication, leakage or lack of injection zone isolation is
indicated by injection rate, operating pressure observation, test, survey, log, or other
evidence, the operator shall immediately notify the Commission and submit a plan of
corrective action on a Form 10-403 for Commission approval. The operator shall
immediately shut in the well if continued operation would be unsafe or would threaten
contamination of freshwater, or if so directed by the Commission. A monthly report of
daily tubing and casing annuli pressures and injection rates must be provided to the
Commission for all injection wells indicating well integrity failure or lack of injection
zone isolation.
Administrative Actions
Unless notice and public hearing is otherwise required, the Commission may
administratively waive or amend any rule stated above as long as the change does not
promote waste or jeopardize correlative rights, is based on sound engineering and
geoscience principles, and will not result in fluid movement outside of the authorized
injection zone.
The following table identifies the specific rules affected by the rewrite.
Injection Order
"Demonstration 0 f
Mechanical
Integrity"
Affected Rules
"Well Integrity
Failure and
Confinement"
"Administrative
Action"
Area Injection Orders
AIO 1 - Duck Island Unit
AIO 2B - Kuparuk River
Unit; Kuparuk River,
Tabasco, Ugnu, West Sak
Fields
AIO 3 - Prudhoe Bay Unit;
Western Operating Area
AIO 4C - Prudhoe Bay Unit;
Eastern Operating Area
AIO 5 - Trading Bay Unit;
McArthur River Field
AIO 6 - Granite Point Field;
Northern Portion
AIO 7 - Middle Ground
Shoal; Northern Portion
AIO 8 - Middle Ground
Shoal; Southern Portion
AIO 9 - Middle Ground
Shoal; Central Portion
AIO lOB - Milne Point Unit;
Schrader Bluff, Sag River,
Kuparuk River Pools
AIO 11 - Granite Point
Field; Southern Portion
AIO 12 - Trading Bay Field;
Southern Portion
AIO 13A - Swanson River
Unit
AIO 14A - Prudhoe Bay
Unit; Niakuk Oil Pool
AIO 15 - West McArthur
6
7
9
6
7
9
6 7 9
6 7 9
6 6 9
6 7 9
6 7 9
6 7 9
6 7 9
4 5 8
5 6 8
5 6 8
6 7 9
4 5 8
5 6 9
)
,
Affected Rules
"Demonstration of "Well Integrity "Administrati ve
Injection Order Mechanical Failure and Action"
Integrity" Confinement"
River Unit
AIO 16 - Kuparuk River 6 7 10
Unit; Tarn Oil Pool 6 8
AIO 17 - Badami Unit 5
AIO 18A - Colville River 6 7 11
Unit; Alpine Oil Pool
AIO 19 - Duck Island Unit; 5 6 9
Eider Oil Pool
AIO 20 - Prudhoe Bay Unit; 5 6 9
Midnight Sun Oil Pool
AIO 21 - Kuparuk River 4 No rule 6
Unit; Meltwater Oil Pool
AIO 22C - Prudhoe Bay 5 No rule 8
Unit; Aurora Oil Pool 6 9
AIO 23 - N orthstar Unit 5
AIO 24 - Prudhoe Bay Unit; 5 No rule 9
Borealis Oil Pool
AIO 25 - Prudhoe Bay Unit; 6 8 13
Polaris Oil Pool
AIO 26 - Prudhoe Bay Unit; 6 No rule 13
Orion Oil Pool
Disposal Injection Orders
DIO 1 - Kenai Unit; KU No rule No rule No rule
\VD-l
DIO 2 - Kenai Unit; KU 14- No rule No rule No rule
4
DIO 3 - Beluga River Gas No rule No rule No rule
Field; BR WD-l
DIO 4 - Beaver Creek Unit; No rule No rule No rule
BC-2
DIO 5 - Barrow Gas Field; No rule No rule No rule
South Barrow #5
DIO 6 - Lewis River Gas No rule No rule 3
Field; WD-l
DIO 7 - West McArthur 2 3 5
River Unit; WMRU D-I
DIO 8 - Beaver Creek Unit; 2 3 5
BC-3
DIO 9 - Kenai Unit; KU 11- 2 3 4
17
DIO 10 - Granite Point 2 3 5
Field; GP 44-11
Injection Order
"Demonstration of
Mechanical
Integrity"
2
DIO 11 - Kenai Unit; KU
24-7
DIO 12 - Badami Unit; WD-
1, WD-2
DIO 13 - North Trading Bay
Unit; S-4
010 14 - Houston Gas
Field; Well #3
010 15 - North Trading Bay
Unit; S-5
DIO 16 - West McArthur
River Unit; WMRU 4D
DIO 17 - North Cook Inlet
Unit; NCIU A-12
DIO 19 - Granite Point
Field; W. Granite Point State
17587 #3
010 20 - Pioneer Unit; Well
1702-15DA WDW
01021 - Flaxman Island;
Alaska State A - 2
010 22 - Redoubt Unit; RU
D1
010 23 - Ivan River Unit;
IRU 14-31
010 24 - Nicolai Creek
Unit; NCU #5
DIO 25 - Sterling Unit; SU
43-9
010 26 - Kustatan Field;
KFl
Storage Injection Orders
SIO 1 - Prudhoe Bay Unit,
Point Mcintyre Field #6
SIO 2A- Swanson River
Unit; KGSF #1
SIO 3 - Swanson River Unit;
KGSF #2
Enhanced Recovery Inj ection Orders
EIO 1 - Prudhoe Bay Unit;
Prudhoe Bay Field, Schrader
Bluff Formation Well V-105
2
2
2
2
2
2
3
3
3
3
No rule
3
3
No rule
')
L.
2
No rule
Affected Rules
"Well Integrity
Failure and
Confinement"
"Administrati ve
Action"
3
4
3
5
3
6
3
5
3
Rule not numbered
3
5
3
6
4
6
4
6
4
7
No rule
6
No rule
6
Order exp ired
4
7
4
7
No rule No rule
No rule 6
No rule 7
No rule
8
Injection Order
EIO 2 - Redoubt Unit; RU-6
)
"Demonstration of
Mechanical
Integrity"
5
")
Affected Rules
"Well Integrity
Failure and
Confinement"
8
"Administrati ve
Action"
9
I
02-902 (Rev. 3/94)
Publisher/Original Copies: Department Fiscal, Department, Receiving
AO.FRM
STATE OF ALASKA
ADVERTISING
ORDER
SEE BOTT()M f'dRJNVOICE ADDRESS
NOTICE TO PUBLISHER ADVERTISING ORDER NO.
INVOICE MUST BE IN TRIPLICATE SHOWING ADVERTISING ORDER NO., CERTIFIED AO-02514016
AFFIDAVIT OF PUBLICATION (PART 2 OF THIS FORM) WITH ATTACHED COpy OF
ADVERTISEMENT MUST BE SUBMITTED WITH INVOICE
F
AOGCC
333 West th Avenue, Suite 100
Anchorage, AK 99501
907-793-1221
AGENCY CONTACT DA TE OF A.O.
R
o
M
Jody Colombie September 77, 7004
PHONE PCN
(907) 793 -] ??l
DATES ADVERTISEMENT REQIJIRED:
T
o
J oumal of Commerce
301 Arctic Slope Ave #350
Anchorage, AK 99518
October 3, 2004
THE MATERIAL BETWEEN THE DOUBLE LINES MUST BE PRINTED IN ITS
ENTIRETY ON THE DATES SHOWN.
SPECIAL INSTRUCTIONS:
United states of America
AFFIDAVIT OF PUBLICATION
REMINDER
State of
ss
INVOICE MUST BE IN TRIPLICATE AND MUST
REFERENCE THE ADVERTISING ORDER NUMBER.
A CERTIFIED COPY OF THIS AFFIDAVIT OF PUBLICATION
MUST BE SUBMllTED WITH THE INVOICE.
ATTACH PROOF OF PUBLICATION HERE.
division.
Before me, the undersigned, a notary public this day personally appeared
who, being first duly sworn, according to law, says that
he/she is the
of
Published at
in said division
and
state of
and that the advertisement, of which the annexed
is a true copy, was published in said publication on the
day of
2004, and thereafter for _ consecutive days, the last
publication appearing on the _ day of
, 2004, and that
the rate charged thereon is not in excess of the rate charged private
individuals.
Subscribed and sworn to before me
This _ day of
2004,
Notary public for state of
My commission expires
Public Notices
)
)
Subject: Public Notices
From: Jody Colombie <jody _ colombie@admin.state.ak.us>
Date: Wed, 29 Sep 2004 13:01 :04 -0800
To: undisclosed-recipients:;
BeC: Cynthia B Mciver <bren_mciver@~d:rrti~.state.ak.us>, Ang~laWebb .
<angie _ webb@adtnin~s~ate.ak:.us>, Robert EMintz <robert_min.tz@law.state.ak.us>; Christine
Hahsen.<c.hans~n@iogcc.state.ok.us>, Terrie·Hubble <hubble~l.@bp.com>, So~dra Stewman
<StewmaSD@BP.com>, Scott·& Cammy Taylor <staylor@·ahlsk~.Ï1:et>, stailekj
<sianekj@unoca1.co1n>, ecolaw <ecolaw@trustees.org>, roseragsdale ~roseragsda1e@gci.net>, trmjr 1
<trmjr 1 @aol.com>, jbriddle <jbriddle@marathonoiLcom::>, rockhil~. <rockhill@aoga.org>, shaneg
<shaneg@evergreengâs.com>, jdarlington <jdarIington~f(J~estoil~com>, n~1son.
<knelson@petroleumnews.com>, cboddy <cbQd4y@usibelli.com>, . Mark ,D.alton .
<mark.dalton@hdrinc.com>,. Shannon Donnelly <shannon.donneUy@conocophiIlips.coI't1>:. "Mark P.
. . , ,\. f:
Worcester" <mårk.p~worcester@conocophillips.com>, "Jerry C. Dethlefs" ... ... ! .
<jerry.c.dethlefs@conocophillips.com>, Bob <bob@inlet],(eeper.org>, ·wdv <wdv@dnr~statê.ak.us>,
tjr <tjr@dnt~state. ak.us>, bbritch <bbritch@alaska.net>, J.1ljnelson <mjnelson@pu:rvingertz.çom>,
Charles O'Donnell <charl~s.o'donnell@veco.com>, "Randy L. Skillern" <Skíl1eRL@BP.com>,
"Deborah J. Jonestl <JonesD6@BP.com>, "Paul G. Hyatt" <hyattpg@BP.com>, "Steven R. Rossberg"
<RossbeRS@BP.com>" Lois <lois@inletkeeper~org>,Dan Bross <kUacnews@kuac.org>, Gordon
Pospisil<PospisG@BP.com>, "Francis·S. Sormner" <SommerFS@Ì3P~com>, Mikel Schultz
<Mikel.Schultz@BP.com>, "Nick W. Glover" <GlÒverNW@BP.com>,."Dary:1 J.·K1eppin"
<KleppiDE@BP .com>, "Janet D. Platt'~ <PlattJD@BP .com>, "Rosanne M. Jacobsen"
<JacobsRM@BP.com>, ddonkel <ddonkel@cfl.rr.com>, Collins Mount
<collins _ mount@revenue.state.ak.us>, Mckay <:mckay@gci.net>,Barbara F Fullmer
<barbara.f.fullmer@conocophillips.com>, bocastwf <bocastwf@bp.cpm>,. Charles Barker .
<barket@usgs~gov>, doug_schultze <doug_ schultze@xtoeriergy..com>,Hank Alford ..
<hank.alford@exxonm.øbiLcom>, Mark Kovac <yesno l@gci.net>, gspfoff
<gspfoff@aurorapower..com>,Gregg Nady <gregg.nady@shell.com>,Fred Steece
<fted.steece@state.sd.us>, rcrotty <rcrotty@ch2m~com>, jejones <jejones@~tirorilpower.com>, dapa
<dapa@alflska.net>,jroderick <jroderick@gcLnet>, eyancy <ëyancy@seal-tit~.net>, "James M.
Ruud" <James.IÍl.ruud@conocophillips.com>, Brit Lively <map~aska@ak.net>, jab··
<jah@diJ.r.state.ak..us>, Kurt E Olson <kurt_olson@legis.st~te.ak.us>, buønoje <buonoje@bp.com>,
Mark Hanley <mark_hanleY@at1adarko.com>, loren:-Ieman <loren_leman@gov.state.ak.us>, Julie
Houle <julie_houle@dnr.state.ak.us>,. JohnW Katz <jwkatz@sso.org>, SuZanJ Hill
<suzan_ hill@dec.state·.ak..us>, tablerk <tablerk@unocal.com>, Brady <brady@aoga.org>, Brian
Havelock <beh@dnr.state.ak..us>, bpopp <bpopp@borough.kenaLalcus>, JimC~te
<j·imwhite@satx.rr.com>, "John S. Hawórth" <jolm.s.haworth@exxo~obiLcoIi1>, marty
<triâttY@rlô:ñâusmâILcom.>, ghammons <gham~ons@aol.colIl>,. rmclean
<rmc1ean@pobox.alaska.net>, mkm7200 <mkm12~@ao1.coni>,·Brian Gillespie.
<itbmg@uaa.alaska.edu>, David· L Boelens <dboelens@a~orapower.co:in>, T()dd Durkee
<TDuRKEE@KMG.com>, Gary Schultz <gary _schultZ@dnr.~tate.ak.us>, .W~yne.Rancier
<~~~~~~p~'f.ltj..canada.ca>, Bill Miller <Bill_ Miller@xtoalaska.cQm>, ·Br~~Qri Gagnon
<b~~g11Q~~~r~~.lavv~com>, Paul Winslow <pmw4islow@forestoil.coin>, GmT)' Catron
Sc~tB:1~~~t,p.~9~è' Sharmaine Copeland <copelasv@bp.com>, Suzanne Aliexan .
<§~~~~~~Þ~~tR~µ~J!gy .com>, Kristin Difks ·<kristin _ dìrlci@c;Inr.state.åk.Us>,. KayIi~ll Zeman
<rcj~~~åJi@Ìp~~fJlÓ1'loil.com>, John Tower <John.Tower@eía.dóe.gov>, Bill Fowler .
<aill~FoWler@~adàrko.COM> , Vaughn Swartz <vaughn~swartZ@rbccm."Com> ,Scott Cranswick
10f2
9/29/2004 1: 10 PM
Public Notices
<scott.cranswick@mms.gpv>, Brad McKÏIn <rnckimbs@BP.com>
,~~e.~~r·..finc1· t¡h.e....a;t;:t~ch~.dNot ige.ª,ndÀttasl1Inent:fort~~J?!r8go~~ª. aménâineht
\1:ì1ð.~rgrouIIð.inject:::ion orders· and the puhlic Notice HapPyVë1;lley #10.
~C)dy COlombie
..... ""'..."...............'".."""..,,,,,,.......,,..,.',,......,,..,,......
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Me.chaolcalIntegrIty of WeIlsNobce~doc: .... '.' '.' .,.......'.... ............. ...... ... "'b" . ·6'4'. .
! Content-En~()ªing: ··ase
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.IIappyVaUeyl0_HearingNotice.doc, ............. ...< ...... .
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20f2
9/29/2004 1: 10 PM
Public Notice
)
')
Subject: Public Notice
From: Jody Colombie <jody_colombie@admin.state.ak.us>
~~!e:....."Yecl,<2?..~.e~...~.~..~.~.. .1?:~5.:26 -0800
19~::.l~g~!'c&~!~i(å;jp~~~Cºtµ··· .
Please publish the attached Notice on October 3/ 2004.
Thank you.
Jody Colombie
Content-Type: applicationimsword
Mechanical Integrity of Wells Notice.doc: b 64
i Content-Encoding: ase
."........ .. ..",..""..""..,....
Content-Type: applicationimsword
: Ad Order form. doc
Content-Encoding: base64
1 of 1
9/29/2004 1: 10 PM
Citgo Petroleum Corporation
PO Box 3758
Tulsa, OK 74136
Mary Jones
XTO Energy, Inc.
Cartography
810 Houston Street, Ste 2000
Ft. Worth, TX 76102-6298
/'1a¡/¿:d /tJ/¡(t~
David McCaleb
IHS Energy Group
GEPS
5333 Westheimer, Ste 100
Houston, TX 77056
Kelly Valadez
Tesoro Refining and Marketing Co.
Supply & Distribution
300 Concord Plaza Drive
San Antonio, TX 78216
Robert Gravely
7681 South Kit Carson Drive
Littleton, CO 80122
George Vaught. Jr.
PO Box 1 3557
Denver, CO 80201-3557
Jerry Hodgden
Hodgden Oil Company
408 18th Street
Golden, CO 80401-2433
Richard Neahring
NRG Associates
President
PO Box 1655
Colorado Springs, CO 80901
John Levorsen
200 North 3rd Street, #1202
Boise,lD 83702
Kay Munger
Munger Oil Information Service, Inc
PO Box 45738
Los Angeles, CA 90045-0738
Samuel Van Vactor
Economic Insight Inc.
3004 SW First Ave.
Portland, OR 97201
Michael Parks
Marple's Business Newsletter
117 West Mercer St. Ste 200
Seattle, WA 98119-3960
Mark Wedman
Halliburton
6900 Arctic Blvd.
Anchorage, AK 99502
Schlumberger
Drilling and Measurements
2525 Gambell Street #400
Anchorage, AK 99503
David Cusato
200 West 34th PMB 411
Anchorage, AK 99503
Baker Oil Tools
4730 Business Park Blvd., #44
Anchorage, AK 99503
Ciri
Land Department
PO Box 93330
Anchorage, AK 99503
Jill Schneider
US Geological Survey
4200 University Dr.
Anchorage, AK 99508
Gordon Severson
3201 Westmar Cr.
Anchorage, AK 99508-4336
Jack Hakkila
PO Box 190083
Anchorage, AK 99519
Darwin Waldsmith
PO Box 39309
Ninilchick, AK 99639
James Gibbs
PO Box 1597
Soldotna, AK 99669
Kenai National Wildlife Refuge
Refuge Manager
PO Box 2139
Soldotna, AK 99669-2139
Penny Vadla
399 West Riverview Avenue
Soldotna, AK 99669-7714
Richard Wagner
PO Box 60868
Fairbanks, AK 99706
Cliff Burglin
PO Box 70131
Fairbanks, AK 99707
Bernie Karl
K&K Recycling Inc.
PO Box 58055
Fairbanks, AK 99711
Williams Thomas
Arctic Slope Regional Corporation
Land Department
PO Box 129
Barrow, AK 99723
North Slope Borough
PO Box 69
Barrow, AK 99723
(Fwd: Re: Consistent Wording for Injection þrs - Well Integrity...
)
~ubject:. [Fwd: Re:. ·Consistent Wörgiv~f9t ~j~~tio~....Ordêfs ~··.Wêll··lp;~~'~irY{R~vi$eg)]
Ff0In:. John Norman<.i?hn~ nOrman(@a9min~state.ctk.us>
~i~~~~ '. F~~~..?I...,,<?ct.. ?~?1T..~,. :?9:~6.-9~-o? '.........'..... ...,..,.. ....' '.. ..'............ ... ..... .......,..........................
1'~;:<J"()gy J...ÇpIg~þ~~....<fj.ogyi:þ(:)~QD;11Irie@~~i~.:stélt~~a}pµŠ? ..
more
-------- Original Message --------
Subject:Re: Consistent Wording for Injection Orders - Well Integrity (Revised)
Date:Wed, 25 Aug 2004 16:49:40 -0800
From:Rob Mintz <robert 11lintz@law.state.ak.us>
To:jim regg@admin.state.ak.us
CC:dan seamount@admin.state.ak.us, john norman@admin.state.ak.us
Jim, looks good, but I still think maybe it would be good to include the following sentence or something like it in the well
integrity and confinement rule:
"The operator shall shut in the well if so directed by the Commission."
My thinking is that otherwise, an operator might argue that the Commission can only require the well to be shut in by
going through an enforcement action, issuing an order after notice and opportunity for hearing, or meeting the strict
requirements for an emergency order under the regulations. The proposed language makes clear that it is a condition of the
authorization to inject, that the operator must shut in the well if directed by the Commission after a notification of loss of
integrity, etc.
»> James Regg <¡im regg@admin.state.ak.us> 8/25/2004 3: 15:06 PM »>
Rob - Thanks for the review; here's a redraft after considering your comments. I have accepted most of the suggested edits;
also attached is response to questions you pose (responses are embedded in the comments, using brackets [JBR - ...] to set
apart from your questions).
Jim Regg
Rob Mintz wrote:
Jim, I have some questions abQut the draft language, which are shown as comments on the first document attached. Based
on my current guesses about what the answers will be to my questions, I also have some suggested edits, which are shown
as redlines on the second document attached.
»> James Regg <¡im regg@;;admin.state.ak.us> 8/17/20044:33:52 PM »>
Please delete previous version (email sent 8/9/04); I found another inconsistency in the injection orders regarding well
integrity that I have integrated into the proposed fix.
Attached is a proposal for consistent language in our injection orders addressing 3 rules related to well integrity:
- "Demonstration of Tubing/Casing Annulus Mechanical Integrity"
- "Well Integrity Failure"
- "Administrative Actions".
This proposal includes input from all Sr. staff (except Jack). If you agree with the approach, I'll work with Jody to
prepare the public notice.
Main points -
Demonstration of Tubing/Casing Annulus Mechanical Integrity
- standardizes the wording used for mechanical integrity demonstrations, and establishes abililty to grant alternate
methods (e.g., temp survey, logging, pressure monitoring in lieu of pressure testing
1 of 2
10/2/20044:07 PM
[Fwd: Re: Consistent Wording for Injection
~rs - Well Integrity ."
- specific to AIO 2C for Kuparuk, there is wording that is more appropriately included in Well Integrity Failure (i.e., more
frequent MITs when communication demonstrated)
- establishes more frequent MIT schedule for sluny injection wells (every 2 yrs) which is consistent with our current
practice (but not addressed in regulations)
Well Integrity Failure
- retitles to "Well Integrity Failure and Confinement"; inserted language regarding injection zone integrity (see DIO 25
and 26)
- consistent language regardless of type of injection (disposal, EOR, storage);
- eliminates requirement for immediate shut in and secure; allows continued injection until Commission requires shut in if
there is no threat to freshwater;
- eliminates delay in notifying Commission after detect leakage or communication ("i.e., "immediately notify");
- removes language about notifying "other state and federal" agencies;
- requires submittal of corrective action plan via 10-403;
- requires monthly report of daily injection rate and pressures (tubing and all casing annuli); this is a requirement we
currently impose when notified of leak or pressure communication;
- notice and action not restricted to leaks above casing shoe as stated in several OIOs
Administrative Actions
- adopts "Administrative Actions" title (earlier rules used "Administrative Relief');
- consistent language regardless of type of injection (disposal, EOR, storage);
- uses "administratively waive or amend" in lieu oftenns like "revise", "reissue", etc.;
- adds geoscience to "sound engineering principles";
- language is more generic regarding fluid movement out of zone; existing versions mention varying combinations of
protecting "freshwater", "aquifers", "USDWs"; "risk of fluid movement"; "fluid escape from disposal zone"
Jim Regg
JohnK. Norman <John Norman@admin.state.us>
Commissioner
: Alaska Oil & Gas Conservation Commission
20f2
10/2/2004 4:07 PM
(Fwd: Re: Consistent Wording for Injection ~rs - Well Integrity...
)
~tibject: [Fwd: Re:ConsistentW ordingJor Injection Orqen; ~WenIntégrity(ReyiSed)]
F'roItl: John Nonnan <jQhn~norman@admin~state.ak.µ.s>
D.........,.:...,a... :..,t.............e......, : F..': r.:...i, 0.1. .. .0. .. .....c:..'.t..... 2. ,...0........9.".,..4 11 :08: 5 5 -0800
I9£}è>ØY .JCgJºl)]qi,~<jody _ colombie@admin.state.ak.us>
please print all and put in file for me to review just prior to hearing on these amendments. thanx
-------- Original Message --------
Subject:Re: Consistent Wording for Injection Orders - Well Integrity (Revised)
Date:Thu, 19 Aug 2004 15:46:31 -0800
From:Rob Mintz <robert mintz@law.state.ak.us>
To:dan seamount@admin.state.ak.us, Jim re,gg@admin.state.ak.us,
john nOffilan@admin.state.ak.us
Jim, I have some questions about the draft language, which are shown as comments on the first document attached. Based
on my current guesses about what the answers will be to my questions, I also have some suggested edits, which are shown as
red lines on the second document attached.
»> James Regg <jim regg@2admin.state.ak.us> 8/17/20044:33:52 PM »>
Please delete previous version (email sent 8/9/04); I found another inconsistency in the injection orders regarding well
integrity that I have integrated into the proposed fix.
Attached is a proposal for consistent language in our injection orders addressing 3 rules related to well integrity:
- "Demonstration of Tubing/Casing Annulus Mechanical Integrity"
- "Well Integrity Failure"
- "Administrative Actions".
This proposal includes input from all Sf. staff (except Jack). If you agree with the approach, I'll work with Jody to prepare
the public notice.
Main points -
Demonstration of Tubing/Casing Annulus l\'lechanical Integrity
- standardizes the wording used for mechanical integrity demonstrations, and establishes abililty to grant alternate methods
(e.g., temp survey, logging, pressure monitoring in lieu of pressure testing
- specific to AIO 2C for Kuparuk, there is wording that is more appropriately included in Well Integrity Failure (i.e., more
frequent MITs when communication demonstrated)
- establishes more frequent MIT schedule for slurry injection wells (every 2 yrs) which is consistent with our current practice
(but not addressed in regulations)
Well Integrity Failure
- retitles to "Well Integrity Failure and Confinement"; inserted language regarding injection zone integrity (see DIO 25 and
26)
- consistent language regardless of type of injection (disposal, EOR, storage);
- eliminates requirement for immediate shut in and secure; allows continued injection until Commission requires shut in if
there is no threat to freshwater;
- eliminates delay in notifying Commission after detect leakage or communication ("i.e., "immediately notify");
- removes language about notifying "other state and federal" agencies;
- requires submittal of corrective action plan via 10-403;
- requires monthly report of daily injection rate and pressures (tubing and all casing annuli); this is a requirement we
currently impose when notified of leak or pressure communication;
- notice and action not restricted to leaks above casing shoe as stated in several DIOs
Administrative Actions
10f2
10/2/2004 4:07 PM
[Fwd: Re: Consistent Wording for Injection
;rs - Well Integrity ...
- adopts "Administrative Actions" title (earlier rules used "Administrative Relief');
- consistent language regardless of type of injection (disposal, EOR, storage);
- uses "administratively waive or amend" in lieu oftenns like "revise", "reissue", etc.;
- adds geoscience to "sound engineering principles";
- language is more generic regarding fluid movement out of zone; existing versions mention varying combinations of
protecting "freshwater", "aquifers", "USDWs"; "risk of fluid movement"; "fluid escape from disposal zone"
Jim Regg
JohnK. Norman <John Norman@admin.state.us>
Commissioner
¡ Alaska Oil & Gas Conservation Commission
Content-Type: applicationlmsword
Injection Order language - questions.doc
Content-Encoding: base64
Content-Type: applicationlmsword
Injection Orders language edits. doc
Content-Encoding: base64
20f2
10/2/2004 4:07 PM
)
/
)
Standardized Language for Injection Orders
Date: August 17,2004
Author: Jim Regg
Demonstration of Tubing/Casing Annulus Mechanical Integrity
The mechanical integrity of an injection well must be demonstrated before injection begins, after
a workover affecting mechanical integrity, and at least once every 4 years while actively
injecting. For slurry injection wells, the tubing/casing annulus must be tested for mechanical
integrity every 2 years. The MIT surface pressure must be 1500 psi or 0.25 psi/ft multiplied by
the vertical depth, whichever is greater, must show stabilizing pressure and may not change more
than 10% during a 30 minute period. Any alternate means of demonstrating mechanical integrity
must be approved by the Commission. The Commission must be notified at least 24 hours in
advance to enable a representative to witness pressure tests.
Well Integrity Failure and Confinement
The tubing, casing and packer of an injection well must demonstrate integrity during operation.
The operator must immediately notify the Commission and submit a plan of corrective action on
Form 10-403 for Commission approval whenever any pressure communication, leakage or lack
of injection zone isolation is indicated by injection rate, operating pressure observation, test,
survey, or log. If there is no threat to freshwater, injection may continue until the Commission
requires the well to be shut in or secured. A monthly report of daily tubing and casing annuli
pressures and injection rates must be provided to the Commission for all injection wells
indicating pressure communication or leakage.
Administrative Actions
Unless notice and public hearing is otherwise required, the Commission may administratively
waive or amend any rule stated above as long as the change does not promote waste or
jeopardize correlative rights, is based on sound engineering and geoscience principles, and will
not result in fluid movement outside of the authorized injection zone.
Standardized Language for Injection Orders
Date: August 17, 2004
Author: Jim Regg
Demonstration of Tubing/Casing Annulus Mechanical Inte,grity
The mechanical integrity of an injection well must be demonstrated before injection begins, at
least once every four years thereafter (except at least once every two years in the case of a slurry
injection well), and before returning a well to service fol1owing afte.F a workover affecting
mechanical integrity, and at ka~;t once every 4 years while actively injecting. For :;!urry
injection wells, the tubing/casing annulus lnust be tðsted for mechanical integrity every-;&-y·e·ars-:·
Unless an alternate GleanS is approved by the Cornnlission. lnechanìcal integrity iTIUst be
dClTIOnstrated by a tubin.Q: pressure test using a ::çfle MfF-surface pressure of must be 1500 psi or
0.25 psi/ft multiplied by the vertical depth, whichever is greater, that ffiH-St-show3. stabilizing
pressure that doesand lnay not change more than 10Q.:ö- percent during a 30 minute period. --Afl.y
altenlate nlcans of dCtTIonstrating Inechanical integrity l1IUSt be approved by the COlnn1ission.
The Commission must be notified at least 24 hours in advance to enable a representative to
witness pressure tests.
Well Integrity Failure and Confinement
Except as otherwise provided in this rule, +1he tubing, casing and packer of an injection well
must Ekffiorr~~trate lnaintain integrity during operation. \Vhenever any pressure con1ffiunication,
leakage or lack of injection zone isolation is indicated by injection rate, operating pressure
observation, test, survey, log. or other evidence, t+he operatorffi:B-St-shall immediately notify the
Commission and submit a plan of corrective action on a Form 10-403 for Commission approval.:
v,,-henever any pressure C01TIlnUnication, leakage or lack of injection zone isolation .is indicated by
injection rate, operating pressure ob$ervation, test, survey. or log. The operator shall shut in the
well if so directed by the COi1unission. The operator shall shut in the well without a\vaiting a
response tì-om the COlTllnissÎo!l if continued operation \\iould be unsafe or would threaten
contamination of freshwaterIf there is no threat to freslnvater, injection lnay continue until the
COl111nìssion requires the \vell to be shut in or secured. Until corrective action is successfully
cotnplctcd, Aª monthly report of daily tubing and casing annuli pressures and injection rates
must be provided to the Commission for all injection wells indicating pressure communication or
leakage.
Administrative Actions
Unless notice and public hearing is otherwise required, the Commission may administratively
waive or amend any rule stated above as long as the change does not promote waste or
jeopardize correlative rights, is based on sound engineering and geoscience principles, and will not result in fluid movement outside of the authorized injection zone.
·
'[Fwd: Re: [Fwd: AOGCC Proposed WI Lal ,þe for Injectors]]
)
$1J.~;.ect: [Fwd: Re: [Fwd: AOGCCProposed WI Language for Injectors]]
1f~():IR:.WintonAubert ·<winton_aubert@admitl.state.alcus>
~~I~~~~~~t~tl~~Ui~~~.~l~..
This is part of the record for the Nov. 4 hearing.
WGA
-------- Original Message --------
Subject: Re: [Fwd: AOGCC Proposed WI Language for Injectors]
Date: Thu, 28 Oct 2004 09:41:55 -0800
From: James Regg <jim regg@admin.state.ak.us>
Organization: State of Alaska
To: Winton Aubert <winton aubert@admin.state.ak.us>
References: <41812422.8080604@admin.state.ak.us>
These should be provided to Jody as part of public review record
Jim
Winton Aubert wrote:
FYI.
--------
Original Message --------
AOGCC Proposed WI Language for
Tue, 19 Oct 2004 13:49:33 -0800
Engel, Harry R <EngelHR@BP.com>
winton aubert@admin.state.ak.us
Injectors
Subject:
Date:
From:
To:
Winton...
Here are the comments we discussed.
Harry
*From: * NSU, ADW Well Integrity Engineer
*Sent: * Friday, October 15, 2004 10:43 PM
*To: * Rossberg, R Steven; Engel, Harry R¡ Cismoski, Doug A¡ NSU, ADW Well
Operations Supervisor
*Cc: * Mielke, Robert L.¡ Reeves, Donald F; Dube, Anna T¡ NSU, ADW Well Integrity
Engineer
*Subject: * AOGCC Proposed WI Language for Injectors
Hi Guys.
John McMullen sent this to us, it's an order proposed by the AOGCC to replace the
well integrity related language in the current Area Injection Orders. Listed
below are comments, not sure who is coordinating getting these in front of
I Winton/Jim. Overall, looks okay from an Operations perspective. We do have a few
comments, but could live with the current proposed language. Note the proposed
public hearing date is November 4.
The following language does not reflect what the slope AOGCC inspectors are
currently requiring us to do:
"The mechanical integrity of an injection well must be demonstrated before
injection begins, at least once every four years thereafter (except at least once
every two years in the case of a slurry injection well), and___* before* **
1 of 3
10/28/2004 11 :09 AM
[Fwd: Re: [Fwd: AOGCC Proposed WI Lang
for Injectors]]
return5_ng a well to service following a workover affecting mechanical integrity."
After a workover, the slope AOGCC inspectors want the well warmed up and on
stable injection, then we conduct the AOGCC witnessed MITIA. This language
requires the AOGCC witnessed MITIA before starting injection, which we are doing
on the rig after the tubing is run. Just trying to keep language consistent with
the field practice. If "after" was substituted for "before", it would reflect
current AOGCC practices.
It would be helpful if the following language required reporting by the "next
working day" rather than "immediately", due to weekends, holidays, etc. We like
to confer with the APE and get a plan finalized, this may prevent us from doing
all the investigating we like to do before talking with the AOGCC.
"Whenever any pressure communication, leakage or lack of injection zone isolation
is indicated by injection rate, operating pressure observation, test, survey,
log, or other evidence, the operator shall * immediately*_** notify the
Commission"
This section could use some help/wordsmithing:
"A monthly report of daily tubing and casing annuli pressures and injection rates
must be provided to the Commission for all injection wells indicating well
integrity failure or lack of injection zone isolation."
Report content requirements are clear, but it's a little unclear what triggers a
well to be included on this monthly report. Is it wells that have been reported
to the AOGCC, are currently on-line and are going through the Administrative
Action process? A proposed re-write would be:
"All active injection wells with well integrity failure or lack of injection zone
isolation shall have the following information reported monthly to the
Commission: daily tubing and casing annuli pressures, daily injection rates."
Requirements for the period between when a well failure is reported and when an
administrative action is approved are unclear. This document states "the operator
shall immediately notify the Commission and submit a plan of corrective action on
a Form 10-403". If we don't plan to do any corrective action, but to pursue an
AA, does a 10-403 need to be submitted? The AOGCC has stated they don't consider
an AA as "corrective action!!.
Let me know if you have any questions.
Joe
-----Original Message-----
From: Kleppin, Daryl J
Sent: Wednesday, September 29, 2004 1:37 PM
To: Townsend, Monte Ai Digert, Scott Ai Denis, John R (ANC) i Miller,
Mike E¡ McMullen, John C
Subject: FW: Public Notices
FYI
-----Original Message-----
From: Jody Colombie [ mailto:jody colombie@admin.state.ak.us
Sent: Wednesday, September 29, 2004 1:01 PM
Subject: Public Notices
Please find the attached Notice and Attachment for the proposed amendment of
underground injection orders and the Public Notice Happy Valley #10.
Jody Colombie «Mechanical Integrity proposal. ZIP» «Mechanical Integrity of
Wells Notice.doc»
2 of3
10/28/2004 11 :09 AM
#10
)
)
PIIILU'PS
.œ PHilliPS Alaska, Inc.
A Subsidiary of PHILLIPS PETROLEUM COMPANY
To:
Robert Crandall
Wayne Campaign
Meltwater North Aquifer Exemption
July 18, 2001
RECEIVED
JUL 2 6 2001
From:
Subject:
Alaska Oil & Gas CO'ns. Commlsslm
Anchorage -
This document will present the interpretations that support the absence of fresh water aquifers in
the area of the Meltwater development.
Date:
For the purpose of this document, Aquifer is defined as sand that has a reasonable expectation of
producing fluids. From North slope experience, I have defined Sands (aquifers) as having
effective porosity> 18% and shale content < 40%. Fresh Water Aquifer is an aquifer that
contains water of salinity less than 10 Kppm TDS and no hydrocarbons.
Shallow logs were acquired in three nearby wells;
2N-349 (Tarn) Wireline Neutron/Density/Dipole Sonic/Resistivity/GR
Cirque 2 (Exploration) Wireline Neutron/Density/Dipole Sonic/Resistivity/GR, Mudlog
2P-438 (Meltwater) LWD Neutron/Density/Resistivity/GR, Mudlog
Shallow intervals in these wells were evaluated for shale volume, total and effective porosity.
Total porosity and true resistivity were combined to calculate apparent water resistivity utilizing
the techniques from the EPA documentation ("RP" or RWapparent), as outlined in previous
correspondence. This was combined with fonnation temperature to calculate water salinity in
Kppm of Total Dissolved Solids. Sands were identified using the above criteria and results for
the 3 wells are presented in the attachments.
The attachments are log plots graduated in Subsea depth. The first track is a lithology column
with volumetric representations of shale, sand and effective porosity. Depth tracks are next. For
the Cirque and 2P-438, the next log track is the Total Gas (in Units) from the Mudlog. Then
fonnation resisti vity and TDS curves are displayed on a logrithmic grid. The TDS curve is
highlighted in dark blue within the sands as defined above. The last tracks are plots of the
common gas indicator logs available. Plotted curves are the Neutron and Density curves in one
track. Free gas is indicated by close approach or crossover of the curves, which is coded red.
2P-438 is the best example of this. When available, the Dipole sonic curves are plotted in the
final track. Compressional and shear curves are normalized in the shales. Free gas is indicated
when the compressional delta t shifts left relative to the shear value. These intervals of curve
separation are also coded red.
The presentations indicate that virtually all of the Sands defined in this shallow interval contain
gas in one fonn or another. Indications are that the logs are measuring free gas and not hydrates
specifically. This is due to the fact that wireline logs are run long after the zones are drilled.
Warmth from the drilling process probably have thawed any hydrates in the near-wellbore region,
leaving free gas to be detected by the logs at wireline time.
Phillips Alaska, Inc. is a Subsidiary of Phillips Petroleum Company
)
Mr. Wayne Campaign
July 26, 2001
Page 2
From the evidence in these logs, I conclude that there are no likely fresh water aquifers within the
Meltwater Area, as represented by this dataset.
If you have questions, comments or discussion, feel free to contact me.
Wayne Campaign
Petrophysicist, Phillips Alaska, Inc.
() ,Qíì -
.var( .- ldJ~
Phillips Alaska, Inc. Is a Subsidiary of Phillips Petroleum Company
#9
")
)
PHilliPS Alaska, Inc.
A Subsidiary of PHilLIPS PETROLEUM COMPANY
Post Office Box 1 00360
700 G Street
Anchorage, Alaska 99510
Telephone 907 265-6806
RIECEi\fE
,i 2001
Ryan Stramp, Meltwater Coordinator
,Maska Oil (~ Gas COns. Commission
June 6, 2001
Ms. Julie Heusser, Mr. Dan Seamount and Ms. Cammy Taylor
Alaska Oil and Gas Conservation Commission
333 West 7th Avenue
Anchorage, AK 99501
Re: Meltwater Aquifer Exemption
Dear Commissioners:
By this letter, Phillips Alaska, Inc. (PAl) is seeking an Aquifer Exemption for the
Meltwater Injection.
In accordance with 40 CFR 144.7, the Meltwater Injection Area meets the criteria for an
"exempted aquifer".
a) There are no aquifers that currently serve as a source of drinking water in the
region.
b) There are no aquifers that will serve as a source of drinking water in the future.
First, many of the aquifers in the region contain hydrocarbon accumulations (i.e.,
gas and/or gas hydrates) that may be commercially producible in the future.
Second, the aquifers are situated at a depth (> 1500') and location (i.e., the North
Slope of Alaska) that makes recovery of water for drinking purposes
economically impractical.
c) The total dissolved solids content of the ground water is more than 3,000 mg/I,
and it is not reasonably expected to supply a public water system.
The following attachments are submitted in support of a Meltwater Aquifer Exemption:
1. Meltwater accumulations and associated injection area.
2. Meltwater Injection Area relative to regional aquifers exemptions.
3. Log salinity calculation summary for wells in the vicinity of the Meltwater Injection
Area.
4. Meltwater 2P-438 and Cirque #2 shallow log results with mud log data showing
shallow gas and/or gas hydrates.
5. Crossplots of Rwa versus depth for Meltwater 2P-438 and Cirque #2.
Phillips Alaska, Inc. is a subsidiary of Phillips Petroleum Company
')
')
I appreciate your work on the Meltwater Aquifer Exemption application and would be
happy to answer any related questions. I can be reached at 265-6268 or
rstramp@ ppco.com via email.
Sincerely,
~~,
~n Stramp
Meltwater Coordinator
-
Meltwater Aquifer Exemption Application
Page 2/11
Attachment 1
Meltwater Accumulations & Injection Area
10-31-05
Meltwater
Injection Area
01030104C01
Meltwater Aquifer Exemption Application
Page 3/11
Attachment 2
Meltwater Injection Area Relative to
Regional Aquifer Exemption
AlpineAquifer
Exemption
Kuukpik
Kalubik 1
e
Star
Milne Point
Riv3
Kuparuk River
Prudhoe
Alpine Pool
Sections
2N-349
e
2
Greater Kuparuk
Aquifer Exemption
N2
Meltwater
Meltwater Aquifer Exemption Application
Page 4/11
Attachment 3
Log Salinity Calculation Summary
Analysis of all available data indicates there are no potential aquifers with total
dissolved solids <3000 ppm. In addition, log data suggests that shallow intervals
conatin gas and/or hydrates.
No porosity logs were acquired in the surface hole (above approximately 1900' tvd
subsea) of the Meltwater exploratory wells. However, shallow logs were acquired on
Meltwater development well 2P-438.
Wells in the general vicinity of the Meltwater Injection Area (i.e., Kalubik #1, Colville
River St. #1, Cirque #2 and 2N-349, which were previously shown on Attachment 2)
were analyzed for fresh water acquifers using the SP Technique and the Rwapparent
Technique. (The Rwapparent Technique is referred to as the Resistivity- Prosity
Technique, or "RP", in EPA literature.) Both are well known techniques within the
industry. Discussion is provided below on the limitations of each method and the
associated salinity estimates.
Two of the four wells (Kalubik #1 and Colville River St. 1 ) are outside the existing KRU
and Alpine Aquifer Exemption Areas. The other two welsl (Cirque #2 and 2N-349) are
located within the KRU Aquifer Exemption Area.
The following table is a list of salinity calculations for the sand underneath the
permafrost. Calculated fluid resistivities are corrected to 750 F and salinity numbers are
in NaCl equivalent, or total dissolved solids (TDS).
Meltwater Aquifer Exemption Application Page 5/11
Kalubik #1
Colville River St #1
Cirque #2
2N-349
Rmf = 1.19 Q-m @ 69'
Rmf = 2.52 Q-m @ 68'
Rmf = 2.28 K2-m @ 85'
Rmf = 3.3 Q-m @ 63'
Permafrost @ 1510'
Permafrost @ 1360'
Permafrost @ 1 t70'
Permafrost @ 1310'
Sand @ 1740'-90'
Sand @ 1510'-20'
Sand @ 1440'-60'
Sand @ t905'-15'
(D=36 Rt=12f2m
(D=36 Rt=2.1Qm
(D=34 Rt=260m
0=31 Rt=10f2m
Rwa = 1.09 Om
Rwa = 0.24 Qm
Rwa = 2.1 Orn
Rwa = 0.8 Orn
(5.3 Kppm)
(28 Kppm)
(2.5 Kppm)
(6.9 Kppm)
SP = -35 my (@ 350)
SP = -40 my (@ 340)
SP = -20 my (@ 35°)
SP = -20 my (@
RwSP = 0.38 Sim
RwSP = 0.5 Orn
RwSP = 1.03 Orn
440)
(15 Kppm)
(20 Kppm)
(5.4 Kppm)
RwSP = 1.19 f2m
(4.5 Kppm)
Hole badly washed
Zone slightly shaley.
Hydrates known .SP
Hydrates below
out. SP probably
Salinities quite high.
more representative
Permafrost. Rwa
more representative.
though still too low.
more representative.
Best TDS Estimate =
Best TDS Estimate =
Best TDS Estimate =
Best TDS Estimate =
10 - 12 Kppm
—20 Kppm
>5.4 Kppm
>6.9 Kppm
In the Kalubik #1 and Cirque #2 wells, average resistivities drop dramatically below
these sands, indicating much saltier waters. In the Colville Rive St. #1 well, the high
salinities begin at the base of permafrost.
2N-349
Base Permafrost picked at 1310' with the section below interpreted to be hydrate
bearing. This is supported by mud log results from Meltwater 2P-438 (see Attachment
4). Shale resistivities suggest salinities in the 6-10 kppm range. Rwa in the sand at
1910' calculates TDS of 6.9 kppm.
This section of the well has wireline logs to 2330' with LWD below that. LWD resistivity
decreases systematically below 2400', implying an increase in salinity below that depth.
There are no appreciable sands present below in which to verify this salinity, though
estimates from the shales would suggest salinities of 20+ kppm TDS.
Kalubik #1
Water salinities below permafrost are estimated to be in the 10-12 Kppm range (TDS),
increasing to 25 Kppm below 1950'. An analysis of a water sample from Albian aged
sands (5050-5250') in this well tested 24.3 Kppm TDS.
Meltwater Aquifer Exemption Application Page 6/11
.
.
Colville River St. #1
Salinities below permafrost are approximately 25 Kppm TDS.
Cirque #2
Under permafrost, salinities are 6+ Kppm increasing to 21 Kppm below 2200'. The
sand immediately below the permafrost is believed to contain gas and/or gas hydrates,
which causes log based salinity calculation results to be too low. This is supported by
mud log results shown in Attachment 4. Attachment 5 is a plot of Rwa versus depth for
the shallow portion of this well.
2P-438
Meltwater 2P-438 salinity calculation results are not shown in the summary table. All
salinity calculations below the permafrost are affected by presence of gas and/or
hydrates. Apparent salinities in the shales, however, are in the range of 6+ kppm.
Calculated salinities shift to an average value of 10 Kppm below a depth of 2200',
though there are no sands present for confirmation. Attachment 5 is a plot of Rwa
versus depth for the shallow portion of this well.
None of the wells exhibit decreased salinity below these depths.
Meltwater Aquifer Exemption Application
Page 7/11
Attachment 4
Shallow Log Results for 2p..438
LWD.RD 1
Meltwater Aquifer Exemption Application
Page 8/11
Attachment 4 (Continued)
Shallow Log Results for Cirque #2
Meltwater Aquifer Exemption Application
w
o
z
a:
«
f-
I
if!
D-
C
f-
~I
>-
«
D-
u
U
..J
D-
X
ill
Page 9/11
1000
1300
1600
-
tu 1900
W
I.L
- 2200
J:
t-
B:i 2500
C
~ 2800
fJ)
.c
:J
en 31 00
3400
3700
4000
!.t) ,....
0
0 0
0
þ
Attachment 5
R A I DEPTH Crossplot
Well: 2P-438
1000.0 - 4000.0 FEET
Filter: RH08<2.22
o
,....
o
,....
RWA@75 (OHMM)
Color: VSH
Meltwater Aquifer Exemption Application
Page 10/11
þ
Attachment 5 (Continued)
R A I DEPTH Crossplot
Well: Cirque 2
1000.0 - 4000.0 FEET
Filter: RH08<2.42
1600
Hydrates
c::::»
c::::»
c::::»
..
1000
Base Permafrost
1300
1900
-
t-
W 2200
W
I.L
-
J: 2500
t-
n.
2800
(\I")
3100
3400
3700
4000
,....
o
Lti
RWA@75 (OHM
o
Color: VSH
Meltwater Aquifer Exemption Application
Page 11/11
#8
A A
TONY KNOWLES, GOVERNOR
A14"KA OIL A" GAS 333 W. T" AVENUE, SUITE 100
CONSERVATION COM11'IISSION ANCHORAGE, ALASKA 99501-3539
PHONE (907) 279-1433
FAX (907) 276-7542
May 23, 2001
Mr. Ryan Stramp
Meltwater Coordinator
Phillips Alaska, Inc.
P.O. Box 100360
Anchorage, AK 99510-0360
Re: Meltwater Pool Rules & Area Injection Order
Dear Mr. Stramp:
We are writing to follow through on a couple of unresolved issues related to the
Meltwater Pool Rules and Area Injection Order. The first issue is whether PAI needs to
have an aquifer exemption to conduct the proposed enhanced recovery operation in the
Meltwater Pool. Although the proposed Meltwater Pool area lies outside the Kuparuk
River Unit area and is not subject to the existing KRU aquifer exemption for Class II
underground injection, PAI's application for an AIO seeks only authorization to conduct
an enhanced recovery operation in a proposed injection zone that has no freshwater. PAI
has demonstrated that the proposed enhanced recovery operations will not allow
movement of fluid into sources of freshwater. Therefore, PAI does not need to secure an
aquifer exemption in order to conduct this enhanced recovery operation.
However, should PAI have other reasons to request an aquifer exemption for the
Meltwater Pool area, the application requirements can be found at 20 AAC 25.440. You
may wish to keep in mind for future planning purposes that the Commission may grant
underground injection control variances when injection does not occur into, through or
above freshwater. See 20 AAC 25.450.
The second issue is the subject of waste disposal for the Meltwater development.
Although PAI's application does not include a Class II disposal well, PAI acknowledges
it may need one in the future. The Pool Rules testimony indicates that annular disposal of
drilling wastes will be utilized in accordance with 20 AAC 25.080. Although there is
mention of waste fluid being transported to a permitted disposal facility, we would like to
point out that annular disposal may not be used to circumvent the requirements of 20
AAC 25.252 relating to underground disposal of oil field wastes. Similarly, approval to
conduct annular disposal operations requires a thorough discussion of many factors,
¡
)
)
Meltwater Pool Rules & Area Injection Order
May 23, 2001
Page 2 of2
including confining zones, fracture information, injection zone lithology and freshwater
analyses of potential injection zones.
If you have any further questions or comments please feel free to contact either Bob
Crandall or Wendy Mahan at the above number. They would be happy to assist you.
Sincerely,
~j+G
Cammy hylor
Chair
CT\jjc
#7
'-')
--
1
2
3
4 In Re:
"')
ALASKA OIL AND GAS CONSERVATION COMMISSION
PUBLIC HEARING
5 CONSIDER APPLICATION FROM PHILLIPS
ALASKA, INCORPORATED, TO ESTABLISH POOL
6 RULES FOR THE MELTWATER OIL POOL
WITHIN THE KUPARUK RIVER FIELD, AND TO
7 APPROVE THE AREA INJECTION ORDER
AUTHORI·ZING ENHANCED OIL RECOVERY
8 OPERATIONS IN THE POOL.
9
TRANSCRIPT OF PROCEEDINGS
10
11
12
13 APPEARANCES:
. 14 Commissioners:
15
16
17
18
19
20
21
22
23
24
25
Anchorage, Alaska
May 7, 2001
9:06 o'clock a.m.
MR. DANIEL T. SEAMOUNT, JR.
MS. CAMMY OECHSLI TAYLOR
MS. JULIE HEUSSER
* * * * * *
~~c
"t'o%1 o/4J- ~V.t-.
~~q)cf .¡ .¡ '()
-i'~.r ~ <'00/
~~ ~ CQ
i9 0~.
v.s-.£.
~
-
MET ROC 0 U R T R E P 0 R TIN G, INC.
745 West Fourth Avenue, Suite 425
Anchorage, Alaska 99501
(907) 276-3876
·
·
·
()
()
1
PRO C E E DIN G S
2
(On record 9:06 a.m.)
3
COMMISSIONER SEAMOUNT: I would like to call
4 this hearing to order. The date is Monday, May 7, 2001. The
5 time is 9:06 a.m. Location is 333 West Seventh Avenue,
6 Anchorage, Alaska. It's the offices of the AOGCC. I'll start
7 by introducing the bench. My name is Dan Seamount. To my
8 right is Cammy Taylor, and to my left is Julie Heusser. We're
9 the three Commissioners of the AOGCC. Sharon Gaunt of Metro
10 Court Reporting is making a transcript of the proceedings. You
11 can get a copy from Metro Court Reporting.
12 The purpose of this hearing today is to consider an
13 application from Phillips Alaska, Incorporated, to establish
14 pool rules for the meltwater oil pool within the Kuparuk River
15 Field, and to approve the area injection -- an area injection
16 order authorizing enhanced oil recovery operations in the pool.
17 Notice of the hearing was published on March 23, 2001,
18 and an amended notice was published on AprilS, 2001.
19 Proceedings are held in accordance with 20 AAC 25.540. Those
20 are the regulations governing public hearings. The hearing
21 will be recorded. Is that correct? Okay. Sorry fo~ 'calling
22 you at such late notice.
23
COURT REPORTER: It's okay.
24
COMMISSIONER SEAMOUNT: No off the record
25
conversation except among the Applicants themselves during
MET ROC 0 U R T R E P 0 R TIN G, INC.
745 West Fourth Avenue, Suite 425
Anchorage, Alaska 99501
(907) 276-3876
3
745 West Fourth Avenue, Suite 425
Anchorage, Alaska 99501
(907) 276-3876
.
MET ROC 0 U R T R E P 0 R TIN G, INC.
23 providing the initial testimony. Do you want us to introduce
24 ourselves all at once now, or just as we enter into our
25 testimony?
22 themselves and approach the Commission. I'll be the
So, we would like to invite the Applicant to introduce
21
20 today, so I may forget something. Okay.
19 We don't have our assistant attorney general helping me out
18 Commissioners. So, I guess anything to say introductory-wise?
17 wishing to cross examine will be considered by the
16 other testimony such as protest or cross examination. Those
15 then the Commission will ask the question. We'll also allow
14 to write the questions, forward them up to the bench here, and
13 have other interested parties, the way to ask the question is
.
COMMISSIONER SEAMOUNT: Okay. Well, if we do
12
11 took it.
UNIDENTIFIED MALE SPEAKER: Somebody -- Jody
10
9 sign in sheet. Where is the sign in sheet?
8 there other interested parties in here today? I didn't see a
7 opportunity for other interested parties to ask questions. Are
6 expert. We'll hear from the Applicant first. Then we'll allow
5 and the Commission will rule whether to consider you as an
4 be considered an expert, you must state your qualifications,
If you wish to
3 statements. We give greater weight to sworn.
we consider sworn testimony or unsworn
2 provide that
We
1 recess or in camera which will be a confidential session.
.
l)
()
.
)
.' )
It
1
COMMISSIONER SEAMOUNT: I think probably as we
2 enter into the testimony would be appropriate.
3
MR. STRAMP: Okay.
4
COMMISSIONER SEAMOUNT: So, your name is?
5
MR. STRAMP: Okay.
6
COMMISSIONER SEAMOUNT: First of all, are you
7 giving sworn testimony?
8
MR. STRAMP: Yes. Yes, sir, I am.
9
10 hand.
11
12
13
e 14
COMMISSIONER SEAMOUNT: Okay. Raise your right
(Oath administered)
MR. STRAMP: Yes, I do.
COMMISSIONER SEAMOUNT: Please state your name.
MR. STRAMP: My name is Ryan Stramp, and since
15 I will be giving sworn testimony, I would like to briefly state
16 my qualifications. I graduated from the University of Oklahoma
17 with a degree in petroleum engineering in 1977. Upon
18 graduation, I went to work for Arco working on the Permian
19 Basin on fields in West Texas and New Mexico. In 1981, I was
20 transferred to Alaska still with Arco, and have resided in
21 Alaska working on Alaska oil fields since then. In almost
22
twenty-four years of working in the oil industry, initially,
23
with Arco and now with Phillips, I've held a variety of
24
engineering and operations assignments including stints as a
25
reservoir engineer, production engineer, on site production
.
MET ROC 0 U R T R E P 0 R TIN G, INC.
745 West Fourth Avenue, Suite 425
Anchorage, Alaska 99501
(907) 276-3876
4
.
.
.
.
)
.
1 supervision, and most recently for the past several years, my
2 work experience has focused on planning and executing field
3 development projects in and around the Kuparuk Field. One very
4 noteworthy project that you'll hear some references to today
5 that I was very involved in was the Tarn development project.
6 And for about the past year or ever since the meltwater project
7 has been in exi~tence, I've been the project coordinator for
8 that project.
9
COMMISSIONER SEAMOUNT: Do any of the other
10 Commissioners have questions concerning Mr. Stamp's
11 qualifications?
12
COMMISSIONER TAYLOR: I don't.
13
COMMISSIONER HEUSSER: No.
14
COMMISSIONER SEAMOUNT: Okay. Mr. Stramp,
15 you'.re accepted as an expert witness.
16
MR. STRAMP: Thank you. Before we get into the
17 main body of the presentation, I wanted to offer a few
18 introductory comments. As you probably know, just over a year
19
ago, Phillips Alaska announced the discovery of the Meltwater
20
Field, and we're here this morning to present testimony to
21
support classification of this Meltwater reservoir as a new oil'
22
pool, and to request pool rules be formally put in place for
23
that new pool.
24
Phillips Alaska has been designated the operator for
25
the Meltwater development on behalf of the other Meltwater
MET ROC 0 U R T R E P 0 R TIN G, INC.
745 West Fourth Avenue, Suite 425
Anchorage, Alaska 99501
(907) 276-3876
5
6
745 West Fourth Avelzue, Suite 425
Anchorage, Alaska 99501
(907) 276-3876
.
MET ROC 0 U R T R E P 0 R TIN G, INC.
25 II comments, then Steve Moothart will provide some geologic
24 II of our agenda for today. I'll continue with my introductory
23 II number two in the lower left-hand corner. This is an outline
MR. STRAMP: Yes. You'll find the slide with
22
COMMISSIONER SEAMOUNT: This one.
21
20 II the pool rule testimony.
MR. STRAMP: Okay. They're the ones that say
I've got.....
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15 slides today?
16
17
18 would they be?
19
COMMISSIONER SEAMOUNT: Okay. Which slides
MR. STRAMP: Yeah. They.....
COMMISSIONER SEAMOUNT: You delivered some
13 II slides in front of you there that you can follow along on?
12 II put up the agenda, if you would. Do you have copies of the
Put up the first slide, (indiscernible). Go ahead and
11
10 II public record in support of our requests.
911 the summary presentation also be considered as part ,of the
8 II request that the slides that we will be presenting today and
7 II testimony with the Commission. In addition, we would like to
6 II area injection order, and have filed updated copies of that
5 II testimony with the Commission for both the pool rules and the
. 1 owners. In the discussion this morning, we will provide
2 testimony on the geological and reservoir properties as we
3 II currently understand them for Mel twater, and along with our
4 II plans for development of the field. We have prefiled written
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1 insights into the Meltwater Pool. Lamont Frazer will talk
2 about some reservoir and operations and hearing issues. Tom
3 Brockway will discuss some billing and completion items, then
4 I'll take the podium again and close by summarizing some issues
5 related to our surface facilities, and then an overall summary
6 of the testimony.
7 Slide three in the packet is just a regional map of the
8 North Slope to orient you with where Meltwater is. You can see
9 it's on the southwest corner of the what we call the Greater
10 Kuparuk Area, about ten miles south of the Tarn Field. It's
11 about twenty-five miles from Meltwater back to CPF2, and we're
12 about seventeen miles from the Village of Nuiqsut.
13 Slide four provides a little bit of background
14 information on the exploration activities that were taking
15 place about a year ago at Meltwater. In early 2000, we
16 obtained three penetrations into the Meltwater Reservoir, and
17 had the subsequent discovery announced. These were two stand
18 alone wells plus one side track. The green 'dots here on the
19 map represent the penetrations. On the right-hand side of the
20
slide here is a plot of the well test information from the one
21
penetration that we did test showing that the Meltwat~r North
22
Number 1 well tested at a peak rate of approximately 4,000
23
barrels a day and then fell off slightly after that with GORs
24
initially about 500, increasing to about 700 standard cubic
25
feet per barrel.
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The next slide provides a very brief overview of the
2 Meltwater project as we know it now. One of the key points is
3 that this is going to be another satellite to the Kuparuk Field
4 that will share the infrastructure, such as the processing
5 facilities and injection facilities that exist in that field.
6 The actual scope of the development of the project is a single
7 drill site with approximately twenty-six wells, and the
8 infrastructure that I referred to here are things like the
9 production flow line and the injection flow line and the road
10 and the power lines that are necessary to tie Meltwater into
11 the existing infrastructure in the Greater Kuparuk area.
12 We're targeting to have production on line later this
13 year. This will be an EOR project, enhanced oil recovery
14 project, from the very start. As you'll hear more about later,
15 our recovery process will be implemented as MWAG or miscible
16 water alternating gas, and our expected reserves using that
17 process are
18 recovery.
19 This
approximately fifty-two million barrels of oil
slide discusses the status of the project as of
20 today. We began construction activities on the Slope in
21 January this year. I'm happy to say that as of now, basically,
22 all of the other -- all of the other on tundra construction
23 work such as installation of the flow lines and the gravel road
24 and the powerline are now complete. And, in fact, we actually
25
have a drilling rig on the pad drilling the very first
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1 development well right now as we speak. We also have the
2 construction work underway on pad to install the construct-
3 or the drill site facilities on pad, and those activities will
4 be ongoing until approximately on or before October 1st we hope
5 to have everything in place to be ready to begin production.
6 Slide seven discusses some issues related to the Unit
7 and PA status for Meltwater. We've had several discussions
8 with the Alaska Department of Natural Resources regarding these
9 issues. Our plans are to expand the existing Kuparuk River
10 Unit to include all of the lands that we envision associated
11 with the Meltwater development, and also form a new Meltwater
12 participating area. We'll be filing the applications
requesting those actions to take place this week. And in that
packet of information will be our formal plan of development
and operations and exploration, and we will copy the Oil and
Gas Commission on that application.
Page eight is a map of the area that shows three
different outlines that we feel are pertinent to consider. The
outline and the solid black line is the area that we are asking
to be included or the Kuparuk River Unit to be expanded to
include -- the current southern boundary of the Kuparµk River
Unit runs right along this line, and we are asking to add these
two additional leases to the Kuparuk River Unit.
The dashed line that I'm outlining here is the area
25 that we're requesting to be included in the initial Meltwater
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1 participating area, and the contoured outlines on the map
2 represent our current net sand map for the Bermuda sand
3 accumulation in the Meltwater Reservoir. There's one other
4 outline that's kind of difficult to see, but the kind of
5 purplish outline on the slide illustrates the area that we'll
6 be talking about more today. This is the area that we're
7 requesting be included in the definition of the Meltwater Pool,
8 and also the area that the Meltwater area injection order would
9 apply to.
10 Slide nine lists the ownership percentages of the
11 companies owning rights to the oil accumulation. These
12 percentages are· a function of the leasehold ownership of the
13 leases involved in the participating area, and the relative
14 amount of net sand that we have mapped on each one of those
15 leases. This is similar but not exactly the same as the
16 satellite ownership in the rest of the Greater Kuparuk area due
17 to some minor differences in the leasehold ownership in this
18 area, but these ownership decimals have been agreed to amongst
19 the parties, and do represent the equity agreement for
20 Meltwater.
21
COMMISSIONER SEAMOUNT: Is that over all four
22 sections then, those percentages?
23
MR. STRAMP: Let me back up to the map. It
24 will -- I think we're upside down there. It's kind of hard to
25 do backwards. It applies specifically to the participating
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· 1 area, and it was derived by calculating the relative amount of
2 net sand on the southern lease here and the northern lease and
3 the ownership of those leases. If the participating area were
4 expanded in the future, those decimals possibly would change,
5 but as far as the initial operations in a specific
6 participating area, those are the equity decimals.
7 As we move through the testimony this morning, we will
8 be providing not only some background information for the
9 Commission and the Commissioners but also suggesting some pool
10 rules.
I wanted to list these four items as kind of the
11 guidepost that we use as we were coming up with the recommended
12 language.
It should look pretty familiar to the Commission.
13 You know, certainly, we're interested as you are in preventing
· 14 waste and promoting conservation and protecting correlative
15 rights, promoting maximum ultimate recovery from the field, and
16 you also see that we've tried to keep things consistent with
17 the pool rules in the immediate area including the Kuparuk, PA,
18 West Sag, Tarn, and other North Slope pools.
19
So, that concludes my portion of the testimony for
20 right now. I would like to turn it over to Steve Moothart next
21 to begin the geological discussion.
22
COMMISSIONER SEAMOUNT: Okay. Would you wish
23 to be considered an expert witness?
24
MR. MOOTHART: Yes.
25
COMMISSIONER SEAMOUNT: Raise your right hand,
·
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MR. MOOTHART: Yes, I do.
4
COMMISSIONER SEAMOUNT: Please state your name,
5 who you represent, what your qualifications are.
6
MR. MOOTHART: My name is Steve Moothart. I'm
7 a staff geologist with Phillips Alaska. Qualifications, I
8 graduated with my BS in geology from Oregon State University in
9 1986. Did independent contract work after that upon
10 receiving -- until receiving my masters in geology from Oregon
11 State University in 1992. I was hired by Arco Alaska in 1991.
12 Since that time, I've worked in Alaska up here working the
13 Kuparuk River Field as development geologist, and then also
14 working the developments of Tabasco and Tarn Fields. For the
15 past year, been working the Meltwater development plan.
16
COMMISSIONER SEAMOUNT: Do any of the
17 Commissioners have any questions regarding Mr. Moothart's
18 qualifications?
19
COMMISSIONER TAYLOR: I don't, thank you.
COMMISSIONER HEUSSER: No.
COMMISSIONER SEAMOUNT: Okay. Mr. Moothart,
20
21
22 you are being accepted as an expert witness.
23
MR. STRAMP: Can I visit with Mr. Moothart for
24
just a second?
25
(Side conversation)
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MR. MOOTHART: Brian just wanted to make a
point that within my presentation there is a point where we'll
be calling a confidential session, and we'll flag it, and at
that point, we would like to present to you confidential
session.
COMMISSIONER SEAMOUNT: Okay. Just let us know
when you get to that point.
MR. MOOTHART: Okay. My first slide is --
9 basically, it's the type log that we'll be using in talking
10 about for the Meltwater accumulation. It's the log of
11 Meltwater North Number 2A. From this slide, I want to discuss
12 the vertical definition of the Meltwater Pool. The Meltwater
13 Pool as we're defining it is a sequence of reservoir sandstones
14 and associated mud stones that are located between depths of
15 4,958. These are subsea tvd depths, and 5,297 subsea within
16 this Meltwater North A or 2Awell, and its offset equivalents.
17 This interval is Late Cretaceous in age, Cenomanian-Turonian
18 within the CB formation. It's approximately 350 feet thick,
19 and it's comprised of two genetically distinct and separate
20 intervals. And I'll discuss those now in descending
21 stratigraphic order.
22 First interval is the Cairn Interval. This is located
23 between the T4.1 and T3 correlatable markers. The -- in this
24
particular well, reservoir quality sands were not encountered
25
within the Cairn Interval, but we think that we do have
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· 1 reservoir quality sands in a lateral location. The Bermuda
2 Interval located between the markers T3 and T2, these were the
3 hydrocarbon bearing sands in this well, and then also in the
9
10
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4 two offset wells, and then these are
this was the interval
5 that's tested in the Meltwater North Number 1 well that Ryan
6 mentioned earlier, and that well flow tested at about 4,000
7 barrels a day, 36 API gravity oil. The Bermuda is the primary
8 development target. The prospective locations in the
stratigraphically younger Cairn Interval carry more risk, and
fewer potential reserves, and those will be tested on an
opportunistic basis as we develop this reservoir.
COMMISSIONER SEAMOUNT: Are you going to
discuss your reasons for believing that there's lateral
reservoir quality sands in the
MR. MOOTHART: Yes, I will.
COMMISSIONER SEAMOUNT:
in the in
17 camera session?
18
MR. MOOTHART: Yes.
19
COMMISSIONER SEAMOUNT: Okay.
20
MR. MOOTHART: Actually, they'll be in the
21 public session.
22
COMMISSIONER SEAMOUNT: Okay.
23
MR. MOOTHART: So, the vertical limits of the
24
pool that we're proposing are the T4.1 interval at 4,958 subsea
25
tvd, and the T2 interval at 5,297.
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. 1 This is a map similar to what Ryan showed earlier.
2 This is a map showing the aerial extent of the proposed pool
3 area. That's this bold line here. Ryan also pointed out its
4 relationship to the current southern boundary of the Kuparuk
5 River Unit through exploration penetrations. And what you see
6 on the map also is in the green contours, this is a current
7 interpretation of the net pay within the Bermuda Interval, and
8 then in the red contours is net pay for prospective Cairn
9 Interval that we're proposing, although this does not encompass
10 all of Cairn potential out here. The pool name, Meltwater, is
11 based upon the -- both the prospect and the exploration well
12 names.
13 Next, I'm going to show a seismic line that basically
. 14 trends from the northwest to the southeast down across this
15 area. This northwest/southeast trending seismic line,
16 basically, it extends from the shelf margin up here, Cenomanian
17 aged shelf margin up here down into the shelf slope. The
18 yellow lines here are faulting that is evidenced up on the
19 shelf margin. The Bermuda Interval, again, our primary
20 development is -- this interval here, it's -- the top of it,
21 T3, is noted by this yellow to orange line, here, pick, and E2
22 by this green pick here. These sands are deposited as slope
23 apron deposits on the Cenomanian aged slope. This faulting
24
that we see at the shelf slope margin likely helped create some
25
of the accommodations space that allowed for these sands to
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1 accumulate. In the seismic line, you see this brighter red to
2 green, upper portion of the Bermuda Interval, and then this
3 black to dark blue coloring here, these are just some of the
4 amplitude signatures that we see associated with this interval.
5
6 Over to the east or southeast of Bermuda and
7 stratigraphically higher, we see some of the amplitude
8 signatures th~t we associate with Cairn Interval. These are
9 deposited in a stratigraphically higher section. They're also
10 offset to the east from the Bermuda Interval, distinctly, a
11 separate accumulation, and the trend of these deposits are more
12 into the page here on the map. They trend more north to south
13 rather than the northwest/southeast direction of the Bermuda
14 Interval, and they're generally more linear to sinusoidal in
15 map view, and I'll show that in the next map. This bright
16 reflector down here is the C35 interval, and this is a regional
17 sequence boundary that can be mapped out here.
18 Next, this is basically a map view of the maximum
19 seismic amplitude between the C35 interval that was down below
20· the Bermuda, and the T4.1 seismic picks which defines the top
21 of the Cairn Interval. What this map shows is the maximum
22 amplitude within that window. The seismic line, again, that we
23 just looked at ran from the northwest to the southeast. In
24
this location up in here is the shelf margin where we saw some
25
faulting taking place so this is amplitudes from the sands
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1 deposited down on the slope. These sands are fed to the slope
2 by a system of gullies that are insized into the shelf margin
3 at the time of sea level low stand. The Bermuda Interval,
4 itself, is channelized to lobate in geometry. The trend of the
S accumulations are generally from the west to the east
6 southeast. The Cairn Interval, I've got outlined here further
7 to the east. As you can see that these tend to be narrower,
8 more linear to sinuous in geometry, and that the trend of these
9 accumulations generally are more north to south.
10
COMMISSIONER SEAMOUNT: Do you have any feeling
11 for net pay in the Cairn relative to the Bermuda?
12
MR. MOOTHART: It's thinner.
13
COMMISSIONER SEAMOUNT: Okay.
14
MR. MOOTHART: The Cairn Interval tends to be
IS more a nested series of channels that are backfilling a larger
16 channel complex, so they tend to be thinner than the Bermuda.
17 And these are more oriented parallel to the base slope. Both
18 accumulations are thought to be stratigraphic traps. Sand
19 distribution is what controls the hydrocarbon distribution, and
20 one thing about the slope apron deposits is that these tend to
21 be very discreet accumulations that are controlled by the local·
22 accommodation space available for these sands to come to rest
23 on the slope.
24 This is a map of the top of the Bermuda Interval, the
25 T3 interval structure map. What you see is generally the
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1 structure out here dips about two to three degrees from the
2 west northwest down to the south or east southeast, excuse me.
3 The top of the Bermuda Interval generally runs from about
4 4,700 -- approximately 4,700 feet subsea tvd to 5,500 feet
5 subsea down here to the east. There is some faulting in the
6 updip portion. This was the faulting at about the shelf slope
7 margin that I showed in the cross section, and some of these
8 other features along the southern and northern boundary and
9 then also to the east here are younger shale-filled -- what
10 appear to be shale-filled channels that act as boundaries .to
11 our sand accumulation. This feature here is actually a younger
12 slump feature which appears to cut out part of the Bermuda
13 Interval. This map is the top of the Cairn or T4.1 interval
.
14 structure map. The dips out - - the Cairn Interval are similar
15 to that of the Bermuda Interval, generally, west to east or
16 southeast. Faulting is the same. These -- this interval
17 generally is about 150 to 200 feet the structure above that of
18 the Bermuda. One thing to note, and I made mention of it in
19 the cross section, was that due to the offset of prospective
20 Cairn Intervals off here to the east, and, in fact, the
21 structural dip, the Cairn Interval -- respective Cairn
22 Intervals are generally structurally level to or below those
23 depths of the Bermuda.
24
Let's hold on to that slide just for a second. What
25
I'm going to do now is talk a little bit about the discreet
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1 nature of these accumulations, these slope apron fan deposits,
2 and what I want to do is I want to use Tarn as an analogue.
3 Tarn, of course, is located as Ryan mentioned earlier about ten
4 miles north of Meltwater. It's another slope apron fan, another
5 deposit fed by slope gullies off the Cenomanian Age shelf. A
6 couple points to make again is that these tend to be discreet
7 accumulations controlled
sediment controlled by local
8 accommodation space, and stratigraphic traps. No gas or water
9 legs were encountered in any of the exploration wells at
10 Meltwater within the Bermuda Interval.
11 Let's put that in the -- so, this is a net sand map of
12 Tarn. Again, this is nine miles north of Meltwater. At Tarn,
13 the Bermuda Interval is also the pay interval, and it is mapped
· 14 into two separate lobes, basically, the northern lobe that I'll
15 refer to as here. This is off of drill site 2L pad, and the
16 southern lobe here drilled off of 2N 'pad. I'm using this as an
17 analogue to kind of point out the discreet nature of these
18 accumulations.
19
COMMISSIONER SEAMOUNT: Does Phillips have any
20 present day analogues?
21
MR. MOOTHART: By present.....
22
COMMISSIONER SEAMOUNT: It says stratigraphic
23 analogues, sedimentary analogues, for example, off the Coast of
24 California, anything like that, if they.....
25
MR. MOOTHART: Okay, you're -- modern.
·
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25 the approximate location of that. That was at 5,141 subsea.
24 cap or gas oil contact that's noted by the red line on the map,
20 wells that they drilled 2L3 29A, and this location in the up
21 dip location at 2L Pad encountered a gas cap. We had sand in
22 the well, and tested a gas out of it. Based upon RFT data and
23 2L 329 and 2L 315, we were able to interpret a estimated gas
Okay. At Tarn, in the drilling of Tarn, one of the
19
18 more as gullies. These are single point sources.
17 aren't anywhere near that scale. That's why we refer to them
16 be a kilometer to three kilometers maybe wide. These features
15 are discussed, they talk about canyons feeding them that will
MR. MOOTHART: A lot of times when turbidites
14
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COMMISSIONER SEAMOUNT: Okay.
13
MR. MOOTHART: I don't have a feel for that.
12
11 extent of these compare?
COMMISSIONER SEAMOUNT: How does the aerial
8 gullies, there's
9 onto the shelf.
10
actually gullies that come all the way back
7 California or Oregon. I'm thinking Point Reyes, some of those
6 analogue, you'd probably be looking at off the Coast of
MR. MOOTHART: If I had to pick a modern day
5
COMMISSIONER SEAMOUNT: Modern day analogues.
4
MR. MOOTHART: Modern day analogues.
3
2 that to where you know what it looks like?
COMMISSIONER SEAMOUNT: Or have you gone beyond
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1 And the point I want to make is that at 2N Pad in the southern
2 lobe, no gas has been encountered, and, in fact, we've got oil
3 present and production at 2N approximately 400 feet higher than
4 the gas-oil contact at 2L Pad. So, that's even as close as
5 these two sand bodies are, there is fluid isolation between
6 them. And I want to note, again, that no water life has been
7 found within the Bermuda at either Tarn or the exploration
8 wells at Meltwater.
9 Kind of building off the wells that I talked about on
10 the last map, this is a lot of RFT data from Tarn and
11 Meltwater. off· to the left here, this leftmost set of data,
12 that is from Tarn 2N or Tarn 3A, excuse me. This is from the
13 southern lobe at Tarn. This well here with the blue circles,
14 that's 2L 315. That's in the - - located in the northern lobe
15 down dip of the gas-oil contact. This is the RFP pressure from
16 2L 329. This was a well updip within the gas lag of the
17 northern lobe, and then I'll talk about the Meltwater wells
18 here. This is Meltwater North 2A, the pink color, and
19 Meltwater North Number 1 in green. What we see scale on the
20 bottom is the divisions are 50 psi difference. What we see in
21 the 2N to 2L is roughly about a same oil gradient plQtted but
22 roughly about ten to fifteen psi difference between the
23 pressures. This is gas gradient down from the RT pressure
24 updip at 2L Pad. The point where that intersects, the oil
25
gradient from the 2L 315 downdip in the oil lag, that's our
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1 interpreted gas-oil contact, and 1,541 at 2L in the northern
2 lobe.
3 What you notice from the Bermuda Interval RFT data at
4 Meltwater is they have essentially the same oil gradient as at
5 Tarn. There is about a thirty to fifty psi difference between
6 pressures between Tarn and Meltwater that's nine miles to the
7 south. Also, there's about a fifteen to twenty psi difference
8 between individual wells at Meltwater, and this is potentially,
9 we could have some communication problems between different
10 wells or different elements in different facies. This has b~en
11 noted and is taken into account in our development plan.
12
COMMISSIONER SEAMOUNT: What are the precision
13 of these RFT? Do you have any feel on that? Plus or minus
14 twenty-five, is that - - or are they a lot more precise than
15 that?
16 MR. MOOTHART: They're a lot more precise than
17 that. I don't have a good handle on that but, generally, I
18 think they're between, you know, maybe plus or minus five.
19
COMMISSIONER SEAMOUNT: So, you believe those
20 differences are real then?
21
MR. MOOTHART: I believe.....
22
COMMISSIONER SEAMOUNT: Okay.
23
MR. MOOTHART:
.... .the differences are real.
24 Now, I want to talk a little bit about the sands themselves.
25
This is a quartz feldspar lithic ternary diagram, or FL
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1 diagram, that plots the concentrations of quarts feldspar and
2 lithic fragments of the sand in its relation to each other.
3 One thing that we notice -- well, on this plot I've got both
4 Tarn data plotted. The Meltwater, which is in the red to
5 orange colors that you see here, and then a Meltwater South
6 well. One thing to notice right off the bat is how all these
7 rocks plot way down in the lithic corner. These are generally
8 quartz poor rocks. That quartz makes up about twenty percent
9 of the bulk volume. They're largely comprised of sedimentary
10 and metamorphic rock fragments as well as organic rock
11 fragments. The sedimentary rock fragments and metamorphic rock
12 fragments are typically composed of philites to sedimentary
13 extrabasinal fine grain silt stones, clay stones. The volcanic
14 rock fragments are generally composed of largely pyroclastic
15 glass shards. A lot of volcanics in this section. Most the
16 time these are
a lot of these are altered to analcite, and
17 one of the things that we see common in the Bermuda Interval is
18 an analcite cement due to the alteration of this volcanic
19 glass.
20 Next slide is basically the same core data plotted
21 again but this time on a lithic ternary diagram to where we
22 have sedimentary rock fragments in the uppermost corner of the
23 triangle, volcanic rock fragments in the left lower, and
24 metamorphic rock fragments in the right lower. One thing that
25
I want to point out with this plot, again, Meltwater is in the
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1 red to yellow-orange colors, Tarn is in the blue, the dark blue
2 colors is that at Meltwater, these are generally, you know,
3 again, overplotting the Bermuda composition, sand compositions,
4 very similar sands suggesting the same provenance or sediment
5 source for these. As we would expect they're the same age,
6 same general setting. But one thing to notice is that the
7 Meltwater sands, if anything, may show slightly less volcanic
8 content than the Tarn Interval. There's a slight shift in the
9 data.
10 This plot is a porosity permeability cross plot.
11 Again, following the same color scheme as on the previous two
12 slides. The Meltwater wells are plotted in the red to kind of
13 yellow-orange color, and Tarn in the dark blue colors.
14
I want to talk a little bit about the porosity and
15 permeability and also some of the saturation, the rock quality
16 characteristics of Meltwater. For the sands in Meltwater, the
17 porosity averages rough- -- porosity ranges from seventeen to
18 twenty-five percent, averages approximately twenty percent.
19 That's in this area here. Permeability ranges from one
20 millidarcy to eighty millidarcies, and averages approximately
21 ten to fifteen millidarcies. This is somewhat facies-dependent·
22 within the accumulation. I'm not going to show a plot of water
23
saturation from the cores but basically, the raw uncorrected
24
saturation measurements from the core, when I say uncorrected,
25
I mean uncorrected for fluid invasion from fresh water drilling
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1 fluids. They average fifty-one percent in these rocks. That's
2 too high. We've got evidence of fluid invasion into those
3 cores. One of the key things we're doing now with the first
4 development well that we're drilling is gathering a low
5 invasion core with tracers so that we can make an accurate
6 determination of our water saturations and some of our other
7 properties. But if we take our log model and start
8 calculating, trying to calculate some water saturations for the
9 wells here, what we. generally see is that in the high energy
10 channelized facies our average calculated water saturations
11 at -- are about forty-five percent. This also seems a little
12 high to us, and is thought to be the result of because this
13 high energy channelized facies carries a lot of mud stone rip
. 14 ups, that there's a lot of scouring power within these facies
15 as they're being deposited and coming down the channel. So,
16 they entrain a lot of the finer grain material that was
17 deposited before them. If you get enough of these, then you
18 get a conductive pathway set that affects your resistivity
19 measurements, and as such, the resistivity affects the
20 saturation calculation. The.....
21
COMMISSIONER SEAMOUNT: Have you produced any
22 water at all. ....
23
MR. MOOTHART: No.
24
COMMISSIONER SEAMOUNT:
. . . . .on any of these
25
tests?
.
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MR. MOOTHART: No water was -- no water was
2 produced in the tests at all. And it's good to note that
3 Meltwater North Number 1 was testing the high energy, this high
4 energy facies that has all these mud stone rip ups, and that's
5 the well that tested 4,000 barrels a day.
6 So, in the lobe facies are more lobate facies at
7 Meltwater. Calculated water saturations average about thirty-
8 two percent. This is pretty much in line with what we're
9 seeing at Tarn, too.
10 The net pay cutoff set we use out here within our model
11 basically use a one millidarcy permeability cut off. This
12 equates to roughly a seventeen percent porosity cut off, and
13 also to a sixty percent water saturation cut off. Net pay
. 14 model that we use at Meltwater at this point is very similar to
16
17
18
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20
21
22
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25
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15 that that was used at Tarn as you would expect with the
lithologies being similar, and the log response is basically a
function of lithology, the main difference being that we
correct Meltwater for its electrical -- measured electrical
properties from the core plugs.
I think at this point is when we'd like to go into
confidential session.
COMMISSIONER SEAMOUNT: Okay. Could you
describe what the information consists of without divulging any
confidential information?
MR. MOOTHART: Just a summary?
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questions.
25
COMMISSIONER HEUSSER: I don't have any
24
COMMISSIONER TAYLOR: Thank you.
23
MR. MOOTHART: Potentially.
22
21 proprietary information?
20 that information, would Phillips lose the value in that
COMMISSIONER TAYLOR: Okay. And by disclosing
19
MR. MOOTHART: Yes, it is.
18
17 information to Phillips?
16 information that you're going to present, is this proprietary
COMMISSIONER TAYLOR: Mr. Moothart, is this
15
COMMISSIONER SEAMOUNT: Okay.
14
MR. MOOTHART: Yes, it does.
13
12 or.....
11 you saying it identifies potential outside the proposed PA
COMMISSIONER SEAMOUNT: Does it identify -- are
10
9 haven't been drilled on yet.
8 and prospects that exist within our exploration groups that
MR. MOOTHART: Because it is upside potential
7
6 holding the information confidential?
COMMISSIONER SEAMOUNT: What's the reasons for
5
4 show is upside potential in this area.
MR. MOOTHART: Basically, what we're going to
3
2 information is it?
COMMISSIONER SEAMOUNT: Yeah, what kind of
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the Meltwater oil pool that we're proposing within the Kuparuk
24 I discussed Rule Number 1, the field, and pool name. This is
MR. MOOTHART: To summarize my testimony here,
COMMISSIONER SEAMOUNT: Okay. Thank you.
21 seismic mapping.
20 domain yet for roughly another year, and then also some of the
19 exploration wells at Meltwater, which aren't in the public
MR. MOOTHART: Showed the well logs for the
17 information -- what kind of data did you show?
COMMISSIONER SEAMOUNT: What kind of
prospects.
potential in the area, and showed some of the exploration
MR. MOOTHART: Basically, I discussed upside
confidential information?
could you summarize what you talked about without divulging any
COMMISSIONER SEAMOUNT: Okay. Mr. Moothart,
(Public summoned to room)
(Confidential session)
(Public excused from room)
COMMISSIONER SEAMOUNT: Okay.
won't be very long as it is.
employees, and Oil and Gas Conservation Commission staff. It
MR. MOOTHART: Basically, the Phillips'
2 the room and identify who you would like to stay?
COMMISSIONER SEAMOUNT: Okay. Could you peruse
C)
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25
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3
4
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9
10
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13 Okay.
.' 14
15
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17 hand.
18
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a)
1 River Field. Rule 2, pool definition. Meltwater North Number
2 2A type log, the vertical pool is defined between a T4.1
3 interval on that -- in that well at 4,958 feet subsea tvd, and
4 the T2 interval or pick at the base at 5,297 feet subsea tvd.
5 The geolo- -- the geographic limits of the Meltwater Pool are
6 Sections 1 through 36 of Township 8 North Range 70s. And that
7 concludes my testimony for this part. If there's any
8 questions, I'll take them.
9
COMMISSIONER SEAMOUNT: I don't have anymore
10 questions at this time. Does.....
COMMISSIONER HEUSSER: No.
COMMISSIONER SEAMOUNT: . . . . . anybody else?
We may be asking questions later then.
Would you like to be considered an expert witness?
MR. FRAZER: Yes, I would.
COMMISSIONER SEAMOUNT: Okay. Raise your right
(Oath administered)
MR. FRAZER: Yes, I do.
COMMISSIONER SEAMOUNT: Please state your name,
21 who you represent, and what your qualifications are to be
22 considered as an expert witness.
23
MR. FRAZER: My name is Lamont Frazer. I
24 represent Phillips Alaska. My qualifications include a degree
25
in chemical engineering from the University of Michigan in
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23 that is relatively close to the Meltwater field. That MI is
24 from CPF2 at Kuparuk. And this is a plot showing slim tube
25 simulation results indicating that that misc- -- that that MI
Meltwater is that we have an MI or a miscible injectant source
22
One of the things that is advantageous for us ctt
21
proposed pool rules associated with those topics.
20
development plan, our plan surveillance program, and the
19
18 reservoir engineering. I plan to cover recovery mechanism,
15 you're being accepted as an expert witness.
16 MR. FRAZER: Thank you. What I would like to
17 talk about is primarily some of the topics associated with
10 COMMISSIONER SEAMOUNT: Thirteen. Do the other
11 Commissioners have any questions?
12 COMMISSIONER HEUSSER: No.
13 COMMISSIONER TAYLOR: I don't.
· 14 COMMISSIONER SEAMOUNT: . Okay. Mr. Frazer,
MR. FRAZER: Thirteen.
9
8 Alaska?
COMMISSIONER SEAMOUNT: How many years in
7
6 reservoir engineering.
5 years I have worked in Alaska primarily in the discipline of
4 Texas, Louisiana, and the Gulf of Mexico. The last thirteen
3 years of petroleum engineering in the states of Oklahoma,
2 University of Alaska-Anchorage in 1995. I have almost twenty
1 1981, a masters in environmental quality engineering from the
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1 is miscible at Meltwater conditions with the Meltwater crude.
2 And this is a plot showing recovery as a function of slim tube
3 operating pressure. And when there is a slope change between
4 these two lines, that is indicative of the MMP or the minimum
5 miscibility pressure. It suggests that we have a minimum
6 miscibility pressure at Meltwater of approximately 2,250, and
7 we measured,the reservoir pressure in the Meltwater North
8 Number 1 exploratory test at 2,400 psi. So, what that
9 indicates is that the MI that we're going to be -- that we
10 would like to use at Meltwater is actually overrich. We could
11 lean it up with produced gas and still have it be miscible at
12 Meltwater reservoir conditions.
13 Because we have a miscible source available to us, we
14 wanted to look at the advantage of going with the miscible
15 recovery process, so we constructed a series of pattern models
16 to evaluate that. We used Tarn as an an~logue to help us
17 develop some of the reservoir properties. This is a plot
18
showing porosity as a function of permeability for the higher
19
energy facies or the combined flow Turbidite facies at Tarn.
20
This is a similar plot, again, showing reservoir
21
properties for our Tarn analogue, and it shows water ,gaturation
22
as a function of porosity.
23
Those previous plots were used to help construct the
24
reservoir model that your -- the depiction of the reservoir
25
model that you see in front of you, and this is a model showing
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1 permeability for a slice of the reservoir. The warmer colors
2 represent higher perm rock, and the cooler colors represent
3 lower perm rock. This model was based on a Stochastic
4 description so every cell has variable properties that we find
5 within various Turbidite facies. Simulation results from that
6 idealized model when using a five -- idealized five spot
7 pattern, provide the following recovery plots. And this is a
8 plot showing recovery as a function of total HCPVI or total
9 hydrocarbon pore volume injected. The squares represent the
10 recoveries that we would expect to get with an lean gas type of
11 a flood, a non-miscible process. The green circles represent
12 the type of flood response we would see with a MI floor or a
13 miscible gas flood. Triangles represent a water flood
.
14 response. But what's really interesting is the -- I should say
15 diamonds represent a water flood response. What is really
16 interesting though is the type of response we get with an MWAG
17 recovery process, which is represented by the triangles. In an
18 idealized five spot pattern model, it shows that we have an
19 incremental recovery benefit of approximately thirteen percent
20 OOIP over water flood. And this is using a twenty percent
21
22
23
24
25
.
HCPVI cumulative slug size for both the MWAG process, which is
a miscible alternating water -- miscible gas alternating water
cycle project, and we also use the twenty percent HCPVI
cumulative slug size for the MI flood.
Unfortunately, we don't often get the idealized
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1 response that we get from our simulation models, so I would
2 like to briefly step through the process that we went to to
3 scale up those to field level results. What we did is we ran
4 our Stochastic pattern models fully compositional so we're
5 looking for incremental recovery on a miscible basis, and we're
6 running those for different lithofacies, the higher Turbidite
7 energy facies and the lower energy facies as well. We then
8 combine those models into a -- dimensionless curves, and we
9 volumetrically weighted each model to represent that portion of
10 the reservoir that we think is relative to that facies. For
11 example, we had about forty percent of our Meltwater facies
12 fall into the higher energy Tarn analog, and about sixty
13
percent falling into the low energy Tarn analog. We combined
14
those into a dimensionless curve
set of curves I should say.
15 We then ran a set of homogeneous models. We ran them with
16 black oil so we didn't worry about tertiary recovery response,
17 and we looked at various pattern configurations that we thought
18 would be representative of what we would actually encounter in
19 the field. Because we cannot accurately predict where the sand
20 lies, we expect to have some irregular patterns, and we expect
21 our well spacing to be non-ideal. Some wells will b~ 'closer
22 than others to each other. We then ran those models on a
23
homogeneous, and compared those to an idealized five spot
24
pattern on a homogeneous basis, and developed a relationship
25
describing the aerial inefficiencies associated with what we
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think will be real world type patterns. We then applied those
radial -- those aerial inefficiencies to our dimensionless
Stochastic model to come up with what we expect in the field.
That is, that the MWAG which previously showed a thirteen
percent incremental recovery over water flood, we actually
expect to get results approximately nine percent incremental
recovery over water flood.
And that ties into the initial MWAG justification. The
reasons that we're going MWAG initially, they include the MWAG
recovery benefits which are estimated at approximately nine
11 percent incremental over water flood. They also include the
12 impact that we're hav- -- that we would have the Kuparuk.
13 Because Meltwater is a new reservoir that has not previously
e 14 seen gas injection, it would be -- it's a very efficient place
15 to inject MI and store gas relative to Kuparuk. Since Kuparuk
e
16 is gas handling limited, any reduction in recycled gas coming
17 from gas that's injected into the ground and recycling through
18 the reservoir would have a beneficial effect in terms of rate.
19 So, Meltwater is expected to have a beneficial impact at
20 Kuparuk in terms of storing gas. In addition, looking at the
21 targeted drill sites at Kuparuk, where we want to inject MI in
22 the future, we will
we see no change in getting to tnose
23 drill sites whether or not we go to Meltwater. So, there is no
24
appreciable adverse recovery impact estimated at Kuparuk.
25
Another reason for initial MWAG justification is the MI
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1 availability. We have the infrastructure in place as well as a
2 MI that is miscible with the Meltwater crude at Meltwater
3 conditions. But the -- one of the key reasons though that we
4 want to go initial is because of the infrastructure opportunity
5 window. What I mean by that is this. Even though we have the
6 infrastructure in place, the MI distribution system that we
7 will be using at Meltwater carries MI to the Western Kuparuk
8 drill sites. Those drill sites are relatively mature on an
9 MWAG basis, and, hence, we will likely be -- unlikely be
10 injecting MI five to ten years down the road. If we were to
11 wait and not inject MI initially at Meltwater, that
12 infrastructure may not be available. And the reason is there's
13 several uses for the piping that carries the MI. It's a
IIÞ 14 potential high pressure gas lift opportunity for the Western
15 Kuparuk drill sites. It could help us debottle neck our water
16 injection, or debottle neck our production. So, taking
17 advantage of Meltwater initially with a MI distribution that's
18 al- -- system that's already in place, we will not adversely
19 affect Kuparuk.
20
21
22
23
24
25
.'
COMMISSIONER HEUSSER: Now, did I hear you say
that these Western Kuparuk drill sites, that the MI p~dcess
there is not time and pressure sensitive?
MR. FRAZER: I'm sorry?
COMMISSIONER HEUSSER: So, delaying MI
injection at those Western Kuparuk drill sites is not going to
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recovery at Kuparuk by doing MWAG at Meltwater.
25
and to our best ability, we don't see any appreciable change in
24
23 handle the gas. So, when taken together, those two counteract,
22 reserve because they have to shut in wells because we can't
21 Kuparuk would realize. But they would also realize some lost
20 cycled gas, there would be some incremental recovery that
19 gas because we would be cycling it so much. But with that
16 handling limits, that would offset that reserve loss. Does
17 that make sense? If we did not do Meltwater, we would have to
18 shut in more wells at Kuparuk because we couldn't handle the
15 that, but because we would have to shut in wells due to gas
14 so there would be some reserve loss associated at Kuparuk from
·
13 benefit by continuing to cycle MI at a very mature drill site
12 that would result from that. There would be a slight recovery
11 sizes if we didn't ,do Meltwater, so there would be two effects
10 we would probably have to inject larger c~mulative MI slug
9 not we pursue MWAG at Meltwater. The difference being is that
8 at Kuparuk, we would be able to reach regardless of whether or
7 was the same drill sites that we're targeting for MWAG process
6 process five to ten years in the future. What I said earlier
5 Therefore, they will likely not be undergoing an MWAG recovery
4 mature, and their life on a MI -- on a MWAG process is limited.
3 components. The Western Kuparuk drill sites are relatively
MR. FRAZER: That -- what -- there is two
2
1 affect recovery?
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23 sea sands that are not in the western side. They're more in
24 the 2X, 2Z side of CPF2, which is the eastern side. The
25 western side is also mature, but it's not as mature as the sea
time, the most mature areas that we're dealing with are mature
22
us with some of the mature areas, but the -- at this ,point in
21
MR. FRAZER: We would use that capacity to help
20
19 you're describing as the western mature flood drill sites?
18 that additional gas handling at CPF2 to handle the -- what
COMMISSIONER HEUSSER: So, you wouldn't use
17
MR. FRAZER: No.
16
15 Meltwater?
14 would you revisit your decision to reroute thatMI to
.
COMMISSIONER HEUSSER: And if that happens,
13
12 to help de-bottleneck the gas train, so the answer is yes.
MR. FRAZER: We do have plans in place at CPF2
11
10 increase gas handling at Kuparuk?
COMMISSIONER HEUSSER: Are there any plans to
9
8 the injection machines that inject the gas back into reservoir.
7 CPFl has a bottleneck primarily in the third stage, which is
6 machines which is our first and second state of compression.
5 injection machines. CPF2 has a bottleneck in the gas-lit
4 CPF2 is primarily -- we have our gas-lit machines and then our
MR. FRAZER: The field is gas handling limited.
3
2 it, CPF2 that's gas handling limited?
COMMISSIONER HEUSSER: Is it just -- what is
1
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1 sands I just described, the 2X and 2Z. We are in the process
2 of abandoning drill sites sea sand MWAG floods at some of the
3 eastern drill sites as we speak. We're giving up on MI
4 injection. We've already given it up at 2Z, for example. We
5 predict that we'll be giving up on MI injection on the Western
6 drill sites within the next few years.
7
COMMISSIONER HEUSSER: Okay. Thank you.
8
MR. FRAZER: Okay. In terms of development
9 drilling, as Ryan mentioned earlier, or Steve mentioned
10 earlier, we are currently drilling our first development well
11 at Meltwater right now. We spudded the end of last month, and
12 we plan to drill approximately seventeen wells this year. We
13 plan to drill the wells on a phase basis with regard to
·
14 regions. We would like to go ahead and better understand what
15
16
17
18
19
20
21
22
23
24
25
·
various regions can provide in terms of long-term staple
production before we go ahead and fully develop the offset
wells.
We also plan to test Cairn early in the program, and
our strategy is to develop the best portions of Meltwater early·
for the rate benefits or the sweep spots, at the same time
testing some of the peripheral regions to better understand the'
long-term performance of those regions.
With regard to 2002, we plan to complete our drilling
program which is another nine wells to give us a total of
twenty-six, and we will likely have a drilling break during the
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e 1 exploration season, which would be the end of December this
2 year through the first quarter of next year.
3 In terms of our injection management strategy, our
4 plans are to maintain reservoir pressure at a sufficient basis
5 to ensure that we do not jeopardize tertiary recovery benefits.
6 We also plan to minimize a number of injectors that we have to
7 give us an opportunity to better underst~nd which wells are
8 talking with what. The reason that's an advantage is with
9 complex geology, we simply cannot go out there and implement a
10 pattern flood because as Steve showed earlier there may be
11 various facies with wells right next to each other that simply
12 do not talk or communicate with one another. So, this will
13 give us a better opportunity to understand what is talking with
e 14 each other before we finalize our patterns.
15 We plan to have an aggressive initial MI injection
16 schedule, and the reason for this is as I mentioned earlier, it
17 will help the GKA from a rate standpoint by allowing us to put
18 gas in a place that has a very high gas storage efficiency. We
19 also plan to optimize our cumulative MI slug size on a pattern
20 basis. Obviously, there will be some patterns that will have a
21 faster MI breakthrough than we desire. If we cannot ,Correct
22 that through pattern conversations -- I'm sorry, through
23 producer conversions to injectors, then we will likely have to
24 live with an overall slug size that's smaller than most
25 patterns. Likewise, if we have patterns and we found that
.
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1 there is very little MI breakthrough, that we have a very
2 efficient sweep process, we'll be able to increase the slug
3 size in those patterns.
4 Finally, late in the life of the field, we plan to have
5 a lean gas sweep, and the reason for that is it will allow us
6 to recover some of the NGLs that are in the MI that are trapped
7 in the reservoir during the MWAG process.
8
9 you.
10
11
12 injection
COMMISSIONER HEUSSER: I've got a question for
MR. FRAZER: Sure.
COMMISSIONER HEUSSER: You -- under your
management strategy, maintain reservoir pressure to
13 ensure tertiary recovery be'nefits, and then you're going to
. 14 minimize injectors, how else are you going to maintain your
is reservoir pressure?
16
MR. FRAZER: We can -- at a produ- -- our
17 calculations plus field data at Tarn suggest that we can
18 maintain reservoir pressure at a two to one producer to
19 injector ratio. From a sweep standpoint though, we would like
20 to have a one to one producer to injector ratio. So, our
21 initial plan would go in -- we would go in with a two, to one
22 producer to injector ratio, maximize rate, understand what is
23 talking with what, and still maintain reservoir pressure, and
24 then convert within the next few years to better improve sweep.
25
Slide 33 represents a production profile. It's a plot
.
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1 showing oil production as a function of time. The green
2 circles represent Meltwater production, and the red dìamonds
3 represent the impact to the GKA as a whole. Now, what this
4 illustrates is that there will be some back out that occurs at
5 Kuparuk and Tarn and some of the other satellites. And the
6 reason is even though Meltwater is a very efficient place to
7 store gas, there will still be gas production associated with
8 the oil production, and that gas production will cause some of
9 the highest fuel oil wells elsewhere at the GKA to be shut in
10 because of our surface facility handling limits on gas
11 compression.
12 Given the number of uncertainties we have, there is
13 quite a bit of optimization that we still need to do. Some of
· 14 it will be simulation based, and some of it will be performance
15 based. With regard to that, we plan to optimize the cumulative
16 slug size. As 'I talked about, that will be done on a pattern
17 basis. The MI enrichment is another level that or another
18 issue that we talked about briefly. Because we have an overly
19 rich MI, there is a possibility that in the future, we may want
20 to lean that up and customize it for Meltwater by mixing it
21 with produced gas.
22 Well spacing, we are currently planning on having
23 nominally a hundred acre well spacing. Again, given the
24
inability we have to predict which wells are talking with what,
25
we may have to go ahead and have infilled -- an in fill program
·
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1 to help us recover areas that are having some communication
2 problems.
3 Horizontal and high angle wells, we plan to use those
4 to help us address some of the communication problems that we
5 talked about. For example, two facies that do not communicate
6 with one another,' we can penetrate them both with a single well
7 and ensure that there is communication across that through that
8 one well bore. In addition, horizontal wells could offer some
9 rate benefits on our producers.
10 Pattern configuration, as I mentioned, we will rely on
11 field data to tell us which are the best wells to convert in
12 the future to optimize our sweep.
13 And well location refinement, as we begin to delineate
· 14 Meltwater and better understand what our seismic attributes are
15 telling us, we'll have to refine our current plans for where we
16 would like to place our wells.
17 In terms of well issues, we expect over half the wells
18 to flow naturally. They'll flow against about 350 pounds back
19 pressure. We are equipping the well bores though for gas lift.
20
Since we don't have any lean gas available at Meltwater for
21
lift, we would use MI initially for lift, and then on~e the
22
MWAG process is over with, the MI distribution system would
23
likely carry lean gas to Meltwater and offer a lift gas source
24
at that time.
25
Another means that we plan to use for artificial lift
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MET ROC 0 U R T R E P 0 R TIN G, INC.
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1 is jet pumps. And what's interesting about jet pumps is not
2 only will they provide a means for us to lift some of our
3 weaker wells, but because we will use injection water coming
4 from CPF2, which is nominally 120 degrees Fahrenheit, that will
5 also mitigate paraffin deposition. And at Meltwater we have a
6 crude that's three and a half percent wax by weight, with a
7 cloud point of a 100 degrees F. So, by using jet pump lifts
8 with injection water as the power fluid, we will be able to
9 mitigate paraffin deposition in our tubulars. Ano-
10
COMMISSIONER HEUSSER: When you said natural
11 flow, what percentage of your wells would be able to flow
12 without artificial lift?
13 MR. FRAZER: We expect over fifty percent.
.'
14 COMMISSIONER HEUSSER: Over fifty percent.
15 MR. FRAZER: Another possible artificial lift
16 scheme that we have is a possible back pressure reduction. If
17 Meltwater flows at higher rates than we expect, or if some of
18 the prospective that Steve showed you comes to fruition' and we
19 do have additional production in the area, there may be a
20 possibility that we'll install a booster station that will help
21 us overcome some of the backpressure problems.
22 Another well issue is our secondary targets,
23 principally, thin marginal Cairn. Now, what Steve had shown is
24 the heart of the Cairn, this southern Cairn play, and it was
25 relatively thick. Our concern is from a well bore standpoint
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· 1 is what happens if it's very thin, say, nominally ten feet. Is
2 it economic or if it isn't. And for us to understand that, we
3 will need to collect some production data and evaluate this
4 over a longterm basis. One of the things that we're asking the
5
6
7
8
9
10
11
12
13
· 14
·
Commission to help us with though is to allow us to evaluate
this and still honor annular isolation concerns, and that's
shown on the next slide.
Since the Cairn is about 200 feet tvd above the Bermuda
Interval, if we were to go ahead and have annular isolation
within a hundred feet of the Bermuda Interval, it really
provides us no way of accessing the Cairn at a later date. If,
however, on some of our early wells we're still on the data
gathering standpoint we don't initially perf the Cairn and
stimulate the Cairn, until we determine its economic viability,
15 we will be setting the crossover point and have no annular
16 isolation unle- -- for 200 feet tvd above the Bermuda. So,
17 what this scheme possibly could lead to is let's say we had a
18 ten foot zone of Cairn that we deemed uneconomic and we never
19 perforated or stimulated it and it was in this well bore, and
20 we wanted to use this well in the future as an injector, as I
21 mentioned earlier, we're going to have about half our injector
22 conversions occurring as we learn more.
If that were the case,
23 it would leave us with a situation where we have an injector
24 with annular isolation that's approximately 200 feet tvd above
25 our perforated interval. And that is one area that we're
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1 asking the Commission for help in helping us preserve the
2 option to go after some of this marginal Cairn and still honor
3 annular isolation regulations.
4 In terms of surveillance, we'll rely on well tests, gas
5 samples, and with gas samples, we will test and look at
6 compositional analyses to tell us if we're having MI
7 breakthrough or not, and we'll likely also use chemical tracers
8 to help us understand which wells are talking with what
9 producers. We'll also be using pressure measurements to help
10 us understand what portions of the reservoir are seeing
11 pressure support, and finally, we'll have surveillance logs to
12 help us.
13 Now, with regard to surveillance logs, we will run
14 those in our injectors. We don't have plans to run them in our
15 producers though because we will be fracture stimulating our
16 producers, and it really will not give us any beneficial
17 information.
18 In terms of the.....
19
COMMISSIONER HEUSSER: Excuse me.
20
MR. FRAZER: Yes.
21
COMMISSIONER HEUSSER: Your pressure
22 measurements, what's the frequency and the number that you
23 anticipate doing per year?
24
MR. FRAZER: In terms of the regulations that
25 we're proposing, I have that outlined in two slides. They're
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2 COMMISSIONER HEUSSER: Okay. That's good
3 enough then.
4 MR. FRAZER: But, verbally, we would do it
5 whenever we saw the need to do it. We want to make sure
6 that -- we're investing a tremendous amount of money injecting
7 MI into the formation, and we want to make sure that that MI is
8 being put to use, and as a result, we will make sure that we
9 maintain the pressure. We're getting pressure support as
10 needed, and we're getting the sweep as needed. So, there is no
11 minimum frequency that we will -- that we have as a mindset
12 right now. We'll do what we need to do.
13
COMMISSIONER HEUSSER: Okay.
.'
14
MR. FRAZER: In terms of pool rules that relate
15 to some of the topics that I've been talking about, they
16 include spacing units or injection well completion, reservoir
17 pressure monitoring, GOR exemption, timing of injection
18 startup, and reservoir surveillance reporting. And I'll go
19 through each of those.
20
The first is spacing units. We're proposing a minimum
21 of ten acre spacing. That will give us the flexibility to go
22 after areas where we do see non-communication issues. We're
23
also proposing that the wells be drilled no closer than 300
24
feet from an ownership change.
25
With regard to proposed rule 5, we're proposing that we
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1 do have less than 200 feet of annular is- -- less than 200 feet
2 to annular isolation from our top perforation except in cases
3 we're pursuing secondary targets as we outlined before.
4 With regards to pressure monitoring, the proposal we
5 have at minimum, an initial pressure survey on each well, and a
6 minimum number of pressure surveys that on an annual basis that
7 equates to the number of governmental sections. Now, this is
8 different than most of the pressure requirements that we have
9 pool rules for including Tarn and Kuparuk. On those pools,
10 what's typically done is there is a annual pressure required
11 for each governmental section. On small accumulations of this
12 nature though, it would make more sense to go ahead and target
13 pressures in areas where they're of most value as opposed to
14 each governmental section~ For example, we could have a single
15 well from a governmental section and be getting an annual
16 pressure on that one well every year, and it will add no value
17 because there's no issues associated with that, whereas if we
18 could use this to collect data elsewhere in the field, that
19 is -- that would be of more value, that would be of great help.
20 We're also proposing to have a pressure datum of 5,400
21 feet subsea, and we're proposing that the pressure surveys
22 consist of either stabilized static pressure measurements,
23 follow ups, build ups, multi rate tests, fill stem tests, or
24 open hole tests. We're proposing to report the results
25
quarterly, and we're also proposing that we'll report special
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MR. FRAZER: Yes.
25
24 authorization to drill within 300 feet of the boundary.
COMMISSIONER TAYLOR: Where you're asking for
23
MR. FRAZER: Yes.
22
21 ,proposed rule 3.
COMMISSIONER TAYLOR: I have a question on
20
19 there any questions?
And that concludes my testimony for this portion. Are
18
17 plans.
16 evaluation, and we also will include our future development
15 We're proposing that we have well allocation and well test
14 injection logs. Again, Cairn and Bermuda, distinct intervals.
13 reservoir pressure analysis, multi-interval production and
12 has a Cairn and Bermuda Interval that are distinct within it,
11 referring to interval, I'm referring to if we have a zone that
10 update, produced in injection fluids by interval, and when I'm
9 report, we propose that it include' a reservoir management
8 six months of production, and for our annual surveillance
7 We're proposing that we have injection start up within
6 make a lot of sense.
5 injecting gas into the reservoir, GOR producing limits do not
4 have a GOR exemption because on a MWAG process where you're
3 Proposed rule 9, GOR exemption, we're proposing that we
2 well.
1 tests or interference or pulse tests on a quarterly basis as
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MET ROC 0 U R T R E P 0 R TIN G, INC.
MR. FRAZER: No.
25
24 wells within the 300 feet?
23 plans? Are those wells that you've described, are any of those
COMMISSIONER TAYLOR: And do you currently have
MR. FRAZER: Yes, exactly.
17 300 feet or
18 right?
19
20
21
22
MR. FRAZER: Uh-hum (affirmative).
COMMISSIONER TAYLOR: All the way around?
more away from that boundary change on the inside,
16 if we could proceed without special approval so long as we were
MR. STRAMP: I think what we're requesting is
MR. FRAZER: Yes.
12
13
.- 14 now?
15
COMMISSIONER TAYLOR: Do you have plans right
9 close to -- that border right there would be one, for instance.
10 COMMISSIONER TAYLOR: Is your request then 300
11 feet within that exterior boundary?
MR. STRAMP: Yeah. There can be if you get up
.... . there is not an ownership
MR. FRAZER:
3 boundaries?
4
5
6
7 change.
8
COMMISSIONER TAYLOR: Thank you.
MR. FRAZER: Within the pool rule.....
2 change? Is there an ownership change between these pool rule
COMMISSIONER TAYLOR: What's the ownership
1
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MET ROC 0 U R T R E P 0 R TIN G, INC.
25 Brockway. I'm a drilling engineer for Phillips Alaska. My
MR. BROCKWAY: Okay. My name is Thomas A.
24
23 qualifications are.
COMMISSIONER SEAMOUNT: And what your
22
MR. BROCKWAY: Yes, sir.
21
20 witness?
19 who you represent, and do you want to be considered an expert
COMMISSIONER SEAMOUNT: Please state your name,
18
MR. BROCKWAY: I do.
17
(Oath administered)
· 14
15 hand.
16
COMMISSIONER SEAMOUNT: Please raise your right
MR. BROCKWAY: Yes, I am.
13
12 you giving sworn testimony?
COMMISSIONER SEAMOUNT: Okay. Let's see, are
(On record)
5
6
7
8 record.
9 here?
10
11
MR. STRAMP: Mr. Brockway will be next.
It's 11:08, and let's see, where are we going from
COMMISSIONER SEAMOUNT: We're back on the
(Off record)
4 Be back at 11:00. We're off the record.
3 further questions. I think -- let's take fifteen minute break.
COMMISSIONER SEAMOUNT: I don't have any
2
COMMISSIONER TAYLOR: Okay.
1
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Brockway's. . . . .
25
COMMISSIONER SEAMOUNT: . . . . .Mr.
24
COMMISSIONER HEUSSER: No.
23
22 there any questions on. ....
21 thirteen years. Family still lives there. Sorry. Qkay. Are
COMMISSIONER SEAMOUNT: I lived there for
20
COMMISSIONER SEAMOUNT: Really? What town?
MR. BROCKWAY: Casper. True oilfield town.
19
18
MR. BROCKWAY: I was born there.
17
COMMISSIONER SEAMOUNT: Are you from Wyoming?
16
MR. BROCKWAY: Yes, sir.
15
COMMISSIONER SEAMOUNT: University of Wyoming?
14
13
12 Tabasco, Kuparuk infill work, gas storage work, to name a few.
11 Meltwater. I've worked on eastern boundary area expansion,
10 and now Phillips, planning and executing developments such as
9 I've been working as a drilling engineer with Arco, first Arco,
8 drilling and completion designs. And for the past five years,
7 Staff Engineer for Baker Hughes Intech designing and executing
6 and international. I spent four years as the Alaska Region
5 on the North Slope, Cook Inlet, throughout the United States
4 directional drilling, and running MWD tools. Vàrious locations
3 From there I spent about eight years working on the rigs,
2 the University of Wyoming in petroleum engineering in 1984.
1 qualifications, I obtained a bachelor of science degree from
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COMMISSIONER TAYLOR: No.
2
COMMISSIONER SEAMOUNT: Okay. You are being
3 Mr. Brockway, you are being accepted as a expert witness.
4 Please proceed.
5
MR. BROCKWAY: We were -- as far as our well
6 construction and development plans for Meltwater, we're really
7 not reinventing the wheel here. What we tried to do is base
8 our development on past successful developments out at Tarn,
9 and in the Kuparuk in field work that we've done over the past
10 several years. What we've got is just really one standard
11 design in two different sizes. The well on the left here I
12 guess you consider our -- to be our conventional monobore
13 design, and what that consists of is a twelve and a quarter
14 surface hole in which you set nine and five-eighths inch
15 surface casing, and you drill out with an eight and a half inch
16 production hole through the reservoir zone, and run a seven
17 inch by four and a half inch tapered production casing string.
18 The slim hole version on the left is a similar design. The
19 surface hole on this is a nine and seven-eighths inch surface
20 hole in which you set seven and five-eighths surface casing
21 k,then drill out with a six and three-quarter inch prdduction
22 hole and run a five and a half by three and a half inch tapered
23 production string.
24
Couple of the key features on this -- on these
we
25
call them monobore completions, the production strings in both
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1 cases are solid cemented liners which we will go in and
2 selectively perforate based on our well logs. The casing seal
3 receptacle right here basically takes the place of a production
4 packer. We can use that -- we'll set that above the production
5 zone as Lamont discussed earlier possibly above our shallower
6 test intervals. That will give us a test of our annulus down
7 to that point under the seal bore point here. And what the
8 monobore design allows us to do is to have a full bore access
9 from surface to tv allowing us really ease of perforating,
10 running post rig logs, and doing remedial work in the well
11 bore.
12
COMMISSIONER HEUSSER: Excuse me. I see that
13 you've got nipples for possible K valves. Do you intend to
14 install some sort of subsurface safety valve for all of those
15 wells capable of natural flow to surface? Or in your injection
16 wells?
17 MR. BROCKWAY: Well, we put this - - as a
18 general design, where we put this in put these nipples in up
19 there for that purpose. I guess. . . . .
20
MR. STRAMP: I might respond to that. We
21
we'll follow the -- our intention is to follow the same
22
guidelines as the rest of Kuparuk Field, and a couple years ago
23
those -- conventions changed where the only wells that meet
24
certain criteria of very high rates or very high gas potential
25
that we install subsurface safety valves in, so we do not
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1 intend to install carte blanche subsurface safety valves in
2 these wells. Having the nipple at that location provides the
3 opportunity to do that in the future if we should need to or if
4 deemed by the Commission or others that it's needed I guess.
5 COMMISSIONER SEAMOUNT: What's your definition
6 of a very high rate?
7 MR. STRAMP: I don't remember the numbers off
8 the top of my head. There's a field standard operating
9 procedure that I'm pretty sure has been shared with the
10 Commission that specifies that information. We can get that to
11 you separately.
12
COMMISSIONER HEUSSER: Yes, please.
13
COMMISSIONER SEAMOUNT: Okay.
14
MR. FRAZER: It's a function of rate. .It's
15 also a function of locale. Wells near the airstrip are
16 required by these regulations to have some sort of safety
17 valves. So, it's a requirement of -- it has two components to
18 it.
19
COMMISSIONER SEAMOUNT: Okay.
20
MR. BROCKWAY: The other nipples here are --
21 and the sliding sleeve are in there to accommodate ou~' jet
22 pump, possible jet pump type completions. We'll also have
23
probably one to five gas lift mandrels for a possible gas lift
24
depending on whether the wells are a producer or an injector,
25
and, of course, the departure and depth of the well.
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1
Let's talk a little bit about casing and cementing
2 practices here. We'll -- I guess the bottom line on casing and
3 cementing is that we will operate all of our wells for drilling
4 and completion operations within the existing AOGCC
5 requirements with -- and Kuparuk -- approved Kuparuk Field
6 rules. Conductor will set at seventy~five feet, at least
7 seventy-five feet below ground level. That will allow us a
8 structure to attach our surface diverters to. We'll set our
9 surface casing at least to 500 feet below the permafrost, and
10 we hope to allow -- give ourselves some allowance for annular
11 disposal. operations in the future.
12
COMMISSIONER HEUSSER: Tom, how does that
13 surface casing depth of at least 500 feet below the permafrost
· 14 compare to the Alpine Field?
15
MR. BROCKWAY: I believe Alpine is deeper.
16 It's a different structure, of course, out there. We're
17 farther up dip. I can't give you the exact numbers but I know
18
in this area, for example, the West Sak is quite a bit
shallower, if you base it on a West Sak type of formation.
It's quite a bit shallower here at Meltwater than it is even in
19
20
21 the main Kuparuk Field.
22
COMMISSIONER HEUSSER: So, it's kind of an
23 arbitrary 500 feet below the permafrost? You're not heading
24 for some sort of.....
25
MR. BROCKWAY: It's a minimum 500 feet.
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COMMISSIONER HEUSSER:
.... ..shale or.....
MR. BROCKWAY: We're looking for a competent
shale or silt stone type tormation to set in. Based on what
we've seen in the past on the exploration wells, that will give
us what we believe that -- anywhere from that point on down
will give us a competent shale to set in. On our first well,
actually we set quite a bit, deeper and obtained a very high
leak off test.
MR. STRAMP: Yeah. Typically, we -- we're down
around the 2,500 foot.....
MR. BROCKWAY: Yes.
MR. STRAMP: . . . . .tvd, which is well below the
13 base permafrost, looking for a good competent place, et cetera.
14
MR. BROCKWAY: That 500 feet isa minimum
15 number. You know, operationally, we would normally want to set
16 deeper. That's a minimum number for a competent shoe depth.
17
We're going to be using a standard Kuparuk type tree,
18 and wellhead assemblies are FMC Gen 5 wellheads. We've gone to
19 these pretty much standard throughout the Kuparuk Field on all
20 of our new wells. They offer a metal to metal seal, which is a
21 little bit better seal protection for overall operatiQhal life.
22 They've all got on the trees these fail safe surface safety
23 valves installed really in the upper master valve position on
24 the tree. Those are high-low pressure valves. All of our
25
wells out of Meltwater will have these whether they're
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1 producers or injectors.
2 The design, there's really no design difference the
3 large bore size for the Gen 5 wellhead and the slim hole. It's
4 just a change in the internal casing hanger that we used to
5 hang casing off. So, from the surface if you were to go out to
6 the pad, you wouldn't be able to tell whether it was a big bore
7 or a slim bore well by looking at the wellheader tree system.
8 As I mentioned, all of our trees will have these fail
9 safe surface safety well -- surface safety valves, and we'll be
10 testing those every six months. That is per our policy and per
11 regulation.
12 A couple of other regulations that I would like to
13 address. We have not seen either on any of the exploration
14 wells or on our current development well that we're drilling
15 any evidence of hydrogen sulfide, but as per regulations, we
16 will have HzS monitors throughout the rig. It's a standard
17 operating practice for us, PA, operating practice. We'll also
18 due to the remote distance this pad from the main Kuparuk Field
19 will have all of our HzS mud scavengers on location to allow us
20 quick response in the event that any HzS is seen.
21 As far as data gathering requirements, all of our data'
22 gathering plans center around the use of LWD tools in the hole.
23 We'll be running those primarily below the surface shoe, and
24 we'll be requesting some exemptions from this particular data
25 gathering requirement set under the regulations. Our first
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1 well, we are obtaining a full set of logs, mud logs, from
2 surface, gamma ray resistivity down to the surface shoe and
3 then gamma ray resistivity neutron density logs below that to
4 tvd as well as a pretty full set of wireline evaluation logs.
5 The first -- the next few wells we will -- the second
6 well will be obtaining a shallow neutron porosity log for
7 freshwater evaluation as requested by the Commission. We'll
8 also be running wire line logs in the production hole, and the
9 third and fourth wells will also have wire line logs in the
10 production hole below the surface shoe. But for the most part,
11 we will be running MWD tools primarily as our primary data
12 gathering tool.
13 I guess with that short overview, that ends my
-
14 testimony, unless there are any questions.
15
COMMISSIONER SEAMOUNT: Thank you, Mr.
16 Brockway.
17
MR. STRAMP: Okay. This is Ryan Stramp again.
18 I'm going to pick up the testimony now. I assume I'm still
19 sworn in before, or do I need to do something?
20
COMMISSIONER SEAMOUNT: Right.
21
MR. STRAMP: Okay. I'm going to spend just a
22 few minutes, and in the interest of time since it's getting
23 relatively close to lunch, I'm going to try to hit the
24 highlights on these. Please stop me or ask any questions as we
25
go, but in the absence of that, I'm going to hit the highest
-.
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1 high points.
2
I'm going to talk about facilities a little bit. I've
3 hit this before. The main aspects of that are a gravel road
4 and a pad. The road and pipeline are each - - are all about ten
5 miles long. We cross four drainages along the way that require
6 bridges, pipelines, including a twenty-four inch production
7 line, and two injection lines, overhead power lines, and then
8 one drill site at the end of it.
9 The next slide I think is a map showing a little bit of
10 the topography. Apologize for the quality of the reproduction
11 but here's the southernmost Tarn drill site, Drill Site 2N.
12 Here's our new drill site, Drill Site 2P, by the way is what
13 we're calling the Meltwater drill site,and the road route and
· 14 pipeline route paralleling it.
15
Slide 52 is a schematic showing a little bit more
16 detail on the pipeline installation. I was talking to Mike
17
Katowski (ph) during break, you know, this really is one of the
18
key facets of this project is it's a long way back to CPF2, and
19
we were unsure early on if, you know, we could expect to flow
20
all that distance back to CPF2 with just pipelines, and our
21
simulation efforts suggest that with this pipeline ins'tallation
22
that includes a twenty-four inch production line all the way
23
from 2D to 2N, and then we also at the same time installed a
24
new twenty-four inch production line loop from the 2N Tarn
25
drill site all the way back to this point, back close to CPF2,
·
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1 that this will allow us to flow the majority of the wells
2 naturally and with our -- help of artificial lift be able to
3 produce all the wells at a long distance back to CPF2. We also
4 see the MI line and water injection lines that will tie in to
5 the infrastructure at the Tarn drill site.
6 The on pad facilities consist of trunk and lateral well
7 manifolding system, very similar to what we installed at Tarn.
8 The lateral or the trunks will include a production trunk, a
9 test trunk, water injection, miscible injectant trunks. The
10 wellhead spacing will be twenty feet, minimum well to well.
11 We're going to install a conventional well test separator at
12 Meltwater. This is a change from Tarn. At Tarn, we used
13 Accuflow test equipment. You know, we still believe that
IIÞ' 14 Accuflow can and does give reliable accurate well tests.
15 However, we feel like after our experience with Tarn that, you
16 know, there's an operating and maintenance cost associated with
17 that that is higher than what we can achieve with a
18 conventional test separator. So, that's why we're going this
19 route. We will have the ability to remotely switch wells in
20 and out of test, as well as control the choke settings on the
21 injectors and the producers. There will be an ESD skid to be
22 able to, you know, shut in the drill site remotely, as well as
23 a small electrical control room.
24 This is a -- slide 54 is a schematic of the pad at
25 drill site 2P. This is the row of wells. We've talked
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1 previously that we expect to drill approximately twenty-six
2 wells, although the drill site is sized to handle roughly twice
3 that many wells, ultimately. The trunks of the trunk and
4 lateral manifold -- or trunk and lateral system will be running
5 along this pipe rack. We have the facilities located here at
6 this end of the pad, and, you know, there really is not a lot
7 there. There's the small control room, the test separator. We
8 will have a small heater for heating the flows before they go
9 onto test, the ESD skid, and also pigging, a pigging module.
10 So, it's a fairly bare bones drill site.
11
A little bit more about well testing. We mentioned
12 it's going to be a conventional vessel. It will be designed to
13 separate gas and liquid only. The metering devices will be the
14 same metering devices as is the standard throughout the rest of
15 the Kuparuk Field. We'll use a micro motion mask flow meter
16 for total liquid measurement, phase dynamics meter to be able
17 to discern how much of that total liquid stream is water versus
18 oil, and vortex shedding meters for gas.
19 This is our proposed rule 7, which has to do with the
20 commingling of fluids from different reservoirs on the surface.
21 We would request that this rule specifically allow th~'
22 commingling of the Meltwater fluids with other produced fluids
23 from the Greater Kuparuk Area. We have a change to the
24 production allocation methodology that has been under
25 discussion for several months. Initially, it was brought up by
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1 the Alaska Department of Revenue with involvement from the
2 Department of Natural Resources and AOGCC, and this stemmed
3 from the Department of Revenue's concern about possibly --
4 well, it's related to the fact that the satellite fields at
5 Kuparuk and the other
Prudhoe, as well, oftentimes have a
6 lower severance tax rate than the main fields do. And the
7 Department of Revenue wants to be very sure as we all do that
8 production allocation is done as fairly and accurately as
9 possible to ensure that the barrels are appropriately taxed
10 from a severance tax standpoint. And we came up with this new
11 scheme that instead of having a allocation factor of one, and
12 this allocation factor is basically how you adjust the well
13 test estimated production to make it match the actual meter
14 production from the field, instead of assuming that the
15 satellite fields all have an allocation factor of one, which
16 has been the case for West Sag, Tabasco, and Tarn so far, this
17 new scheme, and I'll have a slide that talks about this in a
18 moment, has all those -- all the satellite fìelds plus the main
19 Kuparuk Field basically all floating on a spe- -- on a
20 allocation factor month to month. There's no preprescribed
21 allocation factor of one point over the satellites anymore.
22 I'll talk about that in a minute. I know that sounded very
23 confusing. Hopefully, I'll clear it up. The more
24
straightforward part of this is that we intend to continue the
25
standard of the minimum of two well tests per month, and, of
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1 course, monthly reports of allocation and test data. So, the
2 next slide hopefully I'll -- will help me explain a little bit
3 more about the allocation factor.
4 Again, this is new, and one of the terms that's used to
5 describe it is a floating or a float-float system, and that's
6 opposed to the old system, which had a prescribed allocation
7 factor of one for all satellites. In this new system, you
8 would calculate an overall allocation factor for Kuparuk
9 participating area, plus all of the existing satellite fields,
10 and so long as that calculated.allocation factor was less than
11 1.02, all of the PAs involved would have that same allocation
12 factor. If" however, that allocation factor is calculated to
13 be greater than 1.02, and this is a relatively arbitrary number
14 and I'll talk in a minute about why this is here, but it is
15 calculated to be greater than 1.02, but in the allocation
16 factor for all the satellites would be set at that 1.,02 level,
17 and that would result in some additional residual as yet
18 unallocated production that would be shifted to the KPA. And
19 the Department of Revenue's goal here I believe is to minimize
20 the chance of any barrels that should have been counted as
21 Kuparuk production being counted as satellite productión at a
22 lower severance tax rate. And they feel and we feel, as well,
23
the that this system will place emphasis on Phillips as the
24
operator to keep the well test systems tuned up and operating
25
as close to an allocation factor of one as possible, and help
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1 us have the highest quality overall well tests that we can
2 attain. So, if there are questions about that, it's a
3 confusing topic, I know, but -- and it still is a bit of an
4 open topic although we're very close to coming to closure on
5 that with all the involved parties.
6
COMMISSIONER HEUSSER: Ryan, I have a.....
7
MR. STRAMP: Yeah.
8
COMMISSIONER HEUSSER:
. . . . . couple of
9 questions.
10
MR. STRAMP: Okay.
11
COMMISSIONER HEUSSER: Just to make sure I
12 heard you correctly, basically, Kuparuk and all the satellites
13 are going to be thrown into the same pot?
. 14 MR. STRAMP: For calculating allocation factor.
15 Severance tax-wise, they still will have their separate
16 severance tax status, and be taxed at their own severance tax
17 rates, but for calculating every month how much production is
18 attributable to the Kuparuk PA versus the TabascoPA versus the
19 Tarn PA versus Meltwater, this allocation factor scheme that
20 I've talked about will be a change from the way it's happened
21 in the past.
22
COMMISSIONER HEUSSER: Okay. So, you don't
23
even though this production is actually going to be processed
24
through CPF2, all of Kuparuk and all of the satellites are
25
going to enter into the calculation of the factor?
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MR. STRAMP: Yeah. Due to the way that the
2 Kuparuk Field is set up, and it's really because of the fact
3 that CPF3 contributes production of both CPFl and CPF2, there's
4 no single good master meter that you can say that -- or you
5 can't say that just because Meltwater produces to CPF2, that
6 you can look at CPF2 sales meter and say that that's somehow a
7 master meter for all of CPF2 because there's some CPF3
8 production that's in there, as well, so you have to look at the
9 field as a whole, and this is as straightforward a system as
10 we've been able to come up with to do that.
11
COMMISSIONER HEUSSER: Now, I heard you say
12 that 1.02 is arbitrary. Were you going to talk a little bit
13 more about that?
MR. STRAMP: Yes, I can. It's -- the
Department of Revenue requested that there be some upper limit
to what the floating allocation factor can float to, and I
guess as an example, if a given satellite, for instance, if the
well test based estimate of production was that the satellite
for any given month made 1,000 barrels a day, for actual
monetary purposes, if you had an allocation factor of 1.02, you
21 would actually take that 1,000 barrels a day and multiply it by'
22 1.02, so you would have a number that was slightly bigger than
23 1,000 barrels a day that would actually be the value that taxes
24 would be paid on, for instance. And the Department of
25
Revenue's concern as I understand it is that they want to
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1 minimize the chance of a satellite which typically is being
2 taxed at a much lower severance tax rate having its production
3 volume inflated to a larger volume than it might actually be.
4 So, they wanted to put a cap so that if it -- if for some
5 reason you calculated -- and it would never happen, but if you'
6 calculated a very, very large allocation factor, large in terms
7 of greater than one, that the operator would have some reason
8 to figure out, well, you know, why is that. You know, there's
9 something wrong if you calculate this to, you know - - you know,
10 potentially, if you calculate a number that's much, much higher
11 (indiscernible - background noise) the operator should have
12 some impetus that identify the problem and fix it. And by
13 putting this cap, and, you know, there's no science about what
IIÞ 14 it should be other than there is I think a -- let me back up a
15 little bit. If perfection is measured by an allocation factor
16 of 1.0, if everything was tuned up as perfect as you could get
17 it, you probably are going to get month to month a little bit -
18 - you know, one month a little bit higher, the next month a
19 little bit lower than 1.0, so we felt like that there probably
20 should be a little bit dead band in there such that there would
21 be, you know, little or no external influence to the $ystem
22 whenever it's just operating normally. But putting this cap in
23 there says that if it gets far enough away from one on the high
24 side, that the system does change, and it changes in a
25 direction that would be in the operator's interest probably to
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2 COMMISSIONER HEUSSER: Now - - so, that's for
3 severance tax purposes. Are you going to use the same factor
4 for reservoir management?
5 MR. STRAMP: Yes. And one of our goals was to
6 have just one set of books. It's challenging enough to keep
7 one good set of books much less one for severance tax and one
8 for royalty and one for production reporting, so our goal, yes,
9 is to have this be a single allocation algorithm that applies
10 for all purposes, royalty, severance tax, as well as production
11 reporting. And we feel like it will. Within the guidelines
12 that are outlined here, it will have negligible, if any, affect
13 we think on long term reporting of volumes. And our allocation
.'
14 factory -- or factor history has that we look back at Kuparuk
15 is we very seldom have been above one at all. Typically,
16 we're, you know, .97 to .99 type numbers is where we typically
17 run. And so we, frankly, don't foresee the situation occurring
18 but if it does, there'll be rules to handle it.
19
COMMISSIONER HEUSSER: Thank you.
20
MR. STRAMP: Okay. Thank you. That's a
21 confusing issue.
22 A couple of other proposed rules, Rule 12" as stated
23 here has to do with how we would handle production anomalies or
24 proration events. Our first goal would be to attempt to cut
25 all pools by equal percentages. However, we would be asked to
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1 take into account, you know, modifications to that to avoid any
2 equipment damage or significantly increased operating costs,
3 and that's fairly straightforward and similar to other rules
4 that are in place now.
5
And the last one, Rule 13, has to do with the ability
6 of the Commission to modify or amend pool rules in an
7 administrative fashion.
8 So, that I think is what we had prepared specific to
9 the pool rules testimony. Again, there are in all thirteen
10 rules that we've -- I think we did today. We've touched a
11 little bit on each of them as our suggestions.
COMMISSIONER HEUSSER: Ryan, I find that I have
one last question.....
MR. STRAMP: Sure.
COMMISSIONER HEUSSER:
. . .. .on allocation.
Now, I understand from a severance tax standpoint why you want
to shoot for something around one, but if you're going to use
this for reservoir management, too, and you end up being --
having an allocation factor of, what, you know, .98 or nine
seven for months on end, isn't this going to affect the way you
manage your reservoir?
MR. STRAMP: The number -- you know, the
23 deviations that we're talking about from one are so small that
24 they're really within the range of meaSurement uncertainty we
25 feel on the well tests anyway. So, we're not concerned about -
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1 - you know, from that standpoint about conceptually having our
2 numbers off by, you know, two percent or one and a half
3 percent. I mean I don't know exactly, you know, what precision
4 we would attribute to typical well testing but it's not plus or
5 minus two percent I don't think. You know, it's
so, we
6 think that there is -- you know, it's within the range of
7 uncertainty. Directionally, we do still feel that the testing
8 of the satellite fields due to the fact that, you know, there's
9 fewer wells. We've, you know, got newer, better equipment
10 associated with -- or newer equipment I should say associated
11 with the test facilities. In some cases we do have some more
12 sophisticated test equipment involved. We think directionally
13 that the testing of the satellites probably is incrementally
. 14 more accurate than the testing of a typical Kuparuk well, but
15 how to blend the two together we don't have a perfect way to
16 do. We had erred or jointly, the agencies involved anyway had,
17 you know, started off by assuming an allocation factor of 1.0.
18 It basically assumes that the well test adjusted for up time
19 and down time
20 Kuparuk test.
21 good it is.
for the satellites was perfect relative to the
It's probably an overstatement in terms of how
Saying that it's exactly the same as Kuparuk
22 probably is an overstatement of how bad it is. The right
23
answer is probably somewhere in between but that in between is
24
so narrow that we're not uncomfortable about going ahead and
25
letting it float.
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. 1 COMMISSIONER HEUSSER: So, is it safe to say
2 that you've set an upper limit of 1.02 but you didn't feel the
3 need to set a lower limit because the allocation factors that -
9
10
11
12
13
. 14
.
4 - the historical allocation factors at Kuparuk have run between
5 .97 and .99 for years?
6
MR. STRAMP: Yeah. And there, you know,
7 probably had been some excursion somewhere outside that range
8 but they've been short term. And the Department of Revenue had
a external consultant come in late in the year last year and
take a look on site at our metering and allocation procedures,
and one of the things that he came back with was that he felt
like that, you know, the overall Greater Kuparuk Area
allocation methodology was well within industry standards
for and, in fact, he commended us as I recall for having it
15 run as well as it does. So, you know, we agree with that and
16 ,feel like that overall we're doing, you know, a job that meets
17 industry standards, if not exceeds it in terms of overall
18 accuracy of our testing and allocation. So, yes, we're
19 comfortable with it as representing good numbers to run the
20 field by.
21
COMMISSIONER SEAMOUNT: Mr. Stramp, dp' you have
22 any estimates of when you would be finished with the evaluation
23 of the Cairn?
24
MR. STRAMP: We're going to get some
25
significant insights here in just a couple months, and I mean
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22 haven't -- you intend to evaluate Cairn and Bermuda separately,
23 but you don't have a plan, a method to do it yet?
24 MR. FRAZER: Well, the plan is the Cairn
25 location does not anticipate encountering Bermuda. We don't
COMMISSIONER SEAMOUNT: Okay. So, yoµ'
21
20 discussed.
19 just delay completing the Bermuda is something we have not yet
18 injection and production logging packages, or whether it would
17 evaluation purposes. Now, whether that entails separate
16 have an evaluation dedicated strictly for the Cairn for
13 Where are first Cairn penetration of any significance is
· 14 planned, there is no Bermuda being mapped at that location. If
15 we do find Bermuda pay at that location, we would, in fact,
MR. FRAZER: Yeah, I'll take a stab at that.
12
MR. STRAMP: Do you guys want to.....
11
10 out what ,to allocate?
9 commingle then test? How would you do -- how would you figure
8 evaluate, are you going to evaluate separate from the Bermuda
COMMISSIONER SEAMOUNT: How are you going to
7
MR. MOOTHART: Which would be July.
6
COMMISSIONER SEAMOUNT: Are you going to.....
5
4 interval, and evaluate it with our fifth well.
MR. MOOTHART: We plan to penetrate that
3
2 be over soon. So, I.....
1 depending on the results of that, if they're negative, it could
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2
COMMISSIONER SEAMOUNT: Uh-hum, right.
3
MR. FRAZER:
. . . . . would - - so it'll be a simple
4 plan. We'll go in and we test it and the well represents
5 Cairn. If we are mistaken and there is Bermuda potential
6 there, it would depend on the size of the Bermuda potential
7 relative to the size of Cairn, and then we would develop a plan
8 for testing the zone separately at that time.
9
COMMISSIONER SEAMOUNT: Okay. I see by the map
10 that you -- that the Cairn and the Bermuda are aerially
11 isolated, and Mr. Stramp was saying that evaluation would
12 proceed very quickly on the Cairn. Do you have a well plan for
13 the Cairn?
14
MR. FRAZER: Yes, we do.
15
COMMISSIONER SEAMOUNT: Okay.
16
MR. MOOTHART: Our first penetration like I
17 mentioned was
of the Cairn prospective interval is set for
18 our fifth well. And that's basically the best location right
19 out here. So, t's outside of what we currently map as our zero
20 edge for the Bermuda Interval, but there's still potential for
21 that, and it's hitting the heart of the Cairn trend, so it's
22 kind of a dual delineation well. And right now on the schedule
23 I think that's probably looking mid to late July.
24
COMMISSIONER HEUSSER: Would you use a similar
25
completion design, three and a half inch tubing?
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to have deviations within the field.
25
24 communication between injector and producers. So, we do expect
23 patterns where that's just not possible due to non-
22 2,400, it would be 2,400. However, there will likely be
21 voidage, so on an overall basis, if the initial pressure is
MR. FRAZER: Our target will be to net (ph)
20
19 via injection?
18 maintenance. What reservoir pressure are you going to maintain
17 have another question. We heard talk about reservoir pressure
Okay. Thank you.
10 COMMISSIONER HEUSSER:
11 ask for extended confidentiality?
12 MR. MOOTHART: No.
13 COMMISSIONER HEUSSER:
.- 14 COMMISSIONER SEAMOUNT:
15 questions before we proceed?
16 COMMISSIONER HEUSSER:
Oh, I do. I lied. I do
Are there any other
So, you don't intend to
9 year from now.
8 drilled in May of 2000, so I think they get released about a
7 by the State for two years, I believe, and those wells were
MR. MOOTHART: There's -- the well data is held
6
5 will continue to be considered confidential?
4 currently still under confidentiality. Any idea how long those
3 regarding the confidential information, the wells that are
COMMISSIONER HEUSSER: I have a question
2
(Nods yes)
MR. STRAMP:
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25 Phillips on this issue.
24 injection order. Again, my name is Ryan Stramp testifying for
23 flip -- we'll move into the testimony related to the area
MR. STRAMP: Okay. Why don't you go ahead and
22
21 a little bit so -- at least.
COMMISSIONER SEAMOUNT: Well, I need to starve
20
19 finish just before we starve to death.
I believe we'll
MR. STRAMP: Okay. Let's
18
17 continue on then until we starve to death?
COMMISSIONER SEAMOUNT: Well, why don't we
16
15 we're flexible.
14 would be happy to continue on unless you choose otherwise, but
MR. STRAMP: I ask you for your preference. We
13
12 recess, continue after lunch.
11 you guys the option if you want to continue now or take a
COMMISSIONER SEAMOUNT: Okay. Well, we'll give
10
9 forty-five minutes to an hour I would guess.
MR. STRAMP: Yeah. It could well be another
8
7 time do you estimate on this, on area injection order?
6 there are. Now I have a question. Do we want -- how much more
COMMISSIONER SEAMOUNT: It doesn't look like
5
4 testimony focused on the area injection order to follow.
3 pool rules? We've got a separate packet of information and
MR. STRAMP: Any other questions related to the
2
COMMISSIONER HEUSSER: Okay. Thank you.
1
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. 1 As we read the regulation 20 - - AAC 25.402 (c) , we see
2 that there are fifteen requirements related to establishing an
3 area injection order. We hope to rely upon the testimony that
4 you've just heard on the pool rule hearing for -- before those,
5 and that leaves eleven more to talk a little bit about here,
6 specifically. You know, the -- from the pool rule discussion,
8
you know, we discussed how we're going to operate, develop and
operate the field, the depth and name of the pool, how we're
going to complete the wells, and what we see is the incremental
7
9
10 increase and ultimate recovery associated with recovery
11 process. And that leaves this list of items that we have yet
12 to discuss, and we hope to spend the next few minutes going
13 over these .to the satisfaction of the Commission. So, with
. 14 that, Steve's going to take off again.
15
MR. MOOTHART: Okay. This map you've seen
16 before. It's the Bermuda and Cairn anticipated net pay contours
17 and what I want to show here is just that the proposed
18 injection area for Meltwater is coincident with the pool area.
19 Flip forward.
20 The operators and surface owners of the injection area,
21 the operator is Phillips Alaska, Incorporated, and th~' surface
22 owner is the State of Alaska. Just want to note that faxed
23 copies of the pool rules or the injection order were sent to
24 these operator and surface owner on March 12th.
25
Type log, you've seen this before. The injection area,
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1 again, is coincident with the vertical definition of the
2 Meltwater Pool, the top being T4.1 at 4,958 subsea tvd in
3 Meltwater North 2A, and the base of the injection area would be
4 in T2 at 5,297 feet subsea tvd, and includes both the Cairn and
5 Bermuda Intervals.
6 This is the Meltwater North 2A log again but just
7 showing the shallow interval of the well, the Bermuda· Interval.
8 T3 to T2 is down here at the bottom. This is to show that our
9 first prospective reservoir zone out here is the C80 or Tabasco
10 interval. And this was meant to show that the injection
11 interval in these Meltwater wells are separated from the C80 by
12 about 2,700, 2,800 feet of impermeable shale. Should also be
13 noted that out here at the Meltwater, the Tabasco C80, I don't
14 see any reservoir sands, but elsewhere on the western margin of
15 Kuparuk there are some.
16 Initial development plans do not include plans fora
17 Class II disposal well, but if future needs require one, we
18 have basically identified the Ivishak sandstone of the
19 Sadlerochit Group as being an interval for Class II injection.
20 This is shown in the Sinclair Colville well number 1 well. The
21 Ivishak is this interval down in here. This well, exploration'
22 well, is to the north and west. It's drilled along the western
23 margin of the Kuparuk Field. Seeing this well, we would expect
24 in the Meltwater area that the Ivishak is down around 8,500
25 feet deep, so it's considerably below the reservoir zone. We
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1 would expect about sixty feet of sand that -- of greater than
2 fifteen percent porosity. These -- this well and all the other
3 Ivishak wells on the western side here have been deemed wet, as
4 well as up in the Sag River Formation. The Ivishak out in this
5 area is separated from the Kuparuk River Interval by at least
6 or approximately 1,800 feet of Kingak shale, so impermeable
7 shales, and then also by about 400 feet of the Sag River and
8 Shublik.
9
COMMISSIONER SEAMOUNT: Mr. Moothart?
10
MR. MOOTHART: Yeah.
11
COMMISSIONER SEAMOUNT: How much
what did
12 you say the porosity was at the Ivishak?
13
.' 14 about sixty
15
16
17
18
MR. MOOTHART: We had -- in this well you have
feet that's greater than fifteen percent.
COMMISSIONER SEAMOUNT: Sixty feet that's.....
MR. MOOTHART: Yeah.
COMMISSIONER SEAMOUNT:
..... .greater than. ....
MR. MOOTHART: Fifteen percent.
19
COMMISSIONER SEAMOUNT:
.... .fifteen. It looks
20 like there's a lot more sand there than sixty feet.
21
MR. MOOTHART: Yeah.
22
COMMISSIONER SEAMOUNT: So, most of that's
23 pretty tight. Okay.
24
MR. MOOTHART: At Meltwater, I mentioned
25
earlier in the pool rules no water zones were encountered by
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1 Meltwater, or by the exploration wells at Meltwater. Connate
2 water was obtained from core plugs using a miscible extraction
3 process for analyzing that water. Chlorides were then measured
4 by ion chromatography. Chloride content of the Bermuda at
5 Meltwater range from twenty to 40,000 parts per million total
6 dissolve solids. The range in the chlorides is due to
7 diffusion of the chlorides by freshwater drilling fluids. As I
8 mentioned earlier, we're currently gathering a core with tracer
9 data to pin down that composition.
10 This plot is to start walking into the issue of aquifer
11 exemption. What I wanted to show here was the existing Greater
12 Kuparuk Area exemption zone here. Here's Alpine and its
13 aquifer exemption zone, and then the pool area for the
14 Meltwater here kind of tacked onto the south side of the
15 Kuparuk exemption area. Initial wells, while the
let me
16 state Kuparukexemption area was granted by the EPA in 1984.
17 No porosity logs were gathered in the shallow holes of the
18 Meltwater North wells. What we want to talk about now is
19 saliniti~s, water salinities in the shallow portion, shallow
20 intervals out here. The wells specifically that I'm going to
21 talk about are Kalubik Number 1 up here, Arco Colvill.e' River
22 State here, and then two wells within the Tarn area, 2N-349,
23 and then also located very close to this 2N-30S, and then the
24 Cirque 2. All four of those five wells, all the wells except
25
for 2N-305 have shallow porosity logs so we're able to
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1 calculate water salinities in the shallow intervals.
2
COMMISSIONER SEAMOUNT: What kind of porosity
3 logs are they?
4
MR. MOOTHART: Density and neutron. And
5 they're all wire lined, density and neutron.
6
COMMISSIONER SEAMOUNT: Thank you.
7
MR. MOOTHART: You'll note that two of the
8 wells are located outside of any existing aquifer exemption
9 zone, while the Tarn wells and Cirque 2 are within the Greater
10 Kuparuk exemption zone.
11 This is just a table listing the shallow interval.
12 Intervals within the shallow portion of the wells that appear
13 to be water bearing and some of their calculated salinities.
14 The technique for calculating these salinities is using the SP
15 and Rw apparent. These are denoted -- both these -- this
16 technique is denoted as the resistivity porosity or RP
17 technique in the EPA guideline document. Both using the SP and
18 Rw apparent are standard techniques within the industry.
19 Should be noted on this table that all the salinity or fluid
20 resistivity measurements have been corrected to 75 degrees
21 Fahrenheit for comparison technique.
22 The salinities measured are in NaCl or total dissolved
23 solids. And just step through these. Remember Kalubik 1 and
24
Colville River State 1 where wells outside of any current
25
aquifer exemption zone, permafrost as you move towards the
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1 coast, of course, gets a little deeper. Permafrost is at 1,510
2 and Kalubik, 1,360. Kalubik, we're looking at a water-bearing
3 sand from about 1,740 to 1,790 feet in depth, and the water
4 salinities for the two zones range from just over 5,000 parts
5 per million to 15,000 parts per million. Should be noted that
6 the hole is badly washed out, and that the SP measurement is
7 probably more representative. Colville River State Number 1,
8 permafrost is about 1,360 feet. There's a water-bearing sand
9 at 1,510 to 1,520 in depth, and in this well, our water
10 salinities are very high, even this close to the shallow and
11 this close to permafrost. The two measurements range from
12 about twenty to 28,000 parts per million.
13 Cirque 2,which is exploration well sitting kind of
· 14 between Tarn and Meltwater, permafrost there is at 1,170. The
15 Rwa and Rwsp calculations should note we're looking at sand
16 between 1,440 and 1,460 at depth. In measurements that we get,
17 salinity measurements, range in Rwa from 2.5 Kppm to 5.4 Kppm.
18 It should also be noted that hydrates are known in this shallow
19 portion of this well. Remember, this well had the lot when it
20 was drilled. SP is probably more representative, although our
21 petrophysicist thinks it's still too low of a measure~ent.
22 Hard to -- you can't calculate the salinities in the presence
23 of -- accurately within the presence of hydrates because its
24 solid nature.
25
COMMISSIONER SEAMOUNT: Well, do you believe
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22 sands present below that 2,400 foot depth to test that, though
23 measurements, estimates from the shales would suggest
24 salinities of 20,000 Kppm.
25 COMMISSIONER SEAMOUNT: In the 2N-349, you
21 salinity with -- below that depth. There are no appreciable
20 systematically below about 2,400 feet implying an increase in
19 noted that below this sand interval, LWD resistivity decreases
18 more representative of the two measurements. Should also be
17 got hydrates below permafrost, and that the Rwa is actually
16 SP is roughly 4.5 Kppm. Now, here, we also believe that we've
Rw from the
15 calculations from logs, Rwa is 6.9 Kppm, and Rwa
14 water interval 1,905 to 1,915 subsea depth. Our salinity
.'
13 2N-349 permafrost is about 1,310. We have a sand that we see,
12 Field it's interesting where we can measure the hydrates. Tarn
11 we'll check on that. I will show you at 2N-349 and in the Tarn
10 in that interval of that particular well. I will show you
MR. MOOTHART: Don't -- I haven't looked at one
9
8_ on that sand, a gas reading?
COMMISSIONER SEAMOUNT: Did you have a mud log
7
6 hydrates, I can't tell you.
MR. MOOTHART: If that individual sand contains
5
4 that you use to determine if it's hydrate or not?
COMMISSIONER SEAMOUNT: What are your criteria
3
MR. MOOTHART: Yeah.
2
1 that sand contains hydrates?
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1 might have said this already but are there sand -- additional
2 sands between 1,300 and 1,900 that show different log
3 characteristics?
4
MR. MOOTHART: Again, that we think are
5 hydrate-bearing, and that's what we'll go into now.
6
This is a plot of Rwa versus depth. What you see here
7 is at an Rwa. This is
so, a little over one and a half you
8 would expect your salinity calculation to be about 3,000 Kppm
9 total dissolved solids. In 2N-349, that one sand that we
10· looked at, we see Rwa of about .8, and that comes to about that
11 6.9 Kppm. But here's base permafrost up in here. This is zone
12 that petrophysicists feels hydrate-bearing down to about 1,700
13 feet. And what you really want to focus in on are these blue
14 dots shown, and below that hydrate-bearing zone there's this
15 blue dot, trail of blue dots here at about 1,850. Here at
16 about 1,900, this is a sand that we did the calculations in,
17 and then there's a few blue dots down here at about 2,100 feet.
18 This sand right here is a tight streak. What the blue dots
19 represent are a low V shale content. This cross plot then is
20
color coded by beach shale, so you want to calculate a clean
21
sand.
22
This zone though it calculates low V shale is a tight
23 streak carbonate cemented. Like I mentioned, this is the sand
24 that we looked at here, and the next area that calculates any
25 type of low V shale is actually a pyrite cemented zone or
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1 pyrite streak in the well.
2
You asked about hydrates. Our next plot is going to be
3 from 2N~305. This is a gas sample log that was taken in 2N-305
4 as part of a USGS study here last year on gas hydrates. And
5 2N-349 and 2N-305 are -- at this shallow interval are about 950
6 feet apart from one another. At the Bermuda Interval, they're
7 much further than that, but they're shallow in the hole. What
8 we -- what you see here are the gas measurements for Cl through
9 C4, actually up into C5, and up into C6, and what we see is at
10 about 1,300, a little under -- over 1,300, we see a strong Cl
11 peak here, and when you combine all the gas sampling, you see a
12 strong response just below the permafrost here. This is
13 associated with hydrate deposits. They had also made note of
14 some contamination of the shallow portion of the shallowest
15 portion of the hole that they thought was there, and an
16 interesting spike down around 2,400 that Tim Collett with the
17 USGS raised the question do we have hydrates even down that
18 far, that deep, below permafrost.
19
Next is -- slide is just another.
20
COMMISSIONER SEAMOUNT: Why would you
21 necessarily think that's hydrates other than it had ~ 'gas
22 shelf? I mean couldn't it be free gas?
23
MR. MOOTHART: Yeah.
24
COMMISSIONER SEAMOUNT: Okay.
25
MR. MOOTHART: It could be free gas in the
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1 interval, too. There's nothing there that pointed to hydrates.
2
Next, this is just another plot from the same well,
3 again, showing gas sampling versus mud temperature and the
4 depth. Again, all I wanted to show was, again, righü below
5 permafrost we see the large increase in the gas presence of the
6 hydrates.
7
So, our conclusion to this is that we see no apparent
8 fresh water zones in the Meltwater area suitable for human
9 consumption, and that we would líke to apply for an aquifer
10 exemption for the Meltwater pool. And that's my portion of
11 this. Any further questions?
12
COMMISSIONER SEAMOUNT: Any questions?
13
e 14 Frazer.
15
16 Moothart.
MR. MOOTHART: Then I'll turn it over to Lamont
COMMISSIONER SEAMOUNT: Thank you, Mr.
Mr. Frazer?
17
MR. FRAZER: Yes. What I'm first going to
18 cover is the injection data. And this is the injection data
19 showing the water composition coming from CPF2. And this is a
20 typical sample that was obtained during calendar year 2000.
21 There is a written copy of this in the area injection order
22 written testimony.
23
With regard to gas compositions, this is, again,
24
provided in the written testimony, but it shows the lean gas
25
and MI compositions coming from CPF2 during calendar year 2000,
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1 and this is an average on an average basis.
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COMMISSIONER SEAMOUNT: Are you done?
3
MR. FRAZER: No.
4
COMMISSIONER SEAMOUNT: Sorry.
5
MR. FRAZER: One last slide.
6
COMMISSIONER SEAMOUNT: We -- sorry. We had to
7 take a little break for a second.
8
MR. FRAZER: That's all right. On this last
9 slide I'm going to talk about estimated injection pressures,
10 injection zone confinement, and the conditions of the existing
11 penetrations. With regard to our estimate injection pressures,
12 we expect water pressures -- injection pressures to range from
13 1,600 to 2,600 psi. The best estimate is that we'll have about
. 14 a 2,00 psi water injection pressure based on our hydraulic
15 modeling.
16 With regard to gas injection pressures, we expect them
17 to range between twenty-six and 3,600 psi. And, again, based
18 on hydraulic modeling, our best estimate is 2,800 psi is the MI
19 injection pressure we'll see on site.
20 With regard to injection confinement, what we did is we
21 used a model stim plan that relies on a Nolte Smith ~ódeling
22 technique to predict fracture height, and that modeling
23 technique assumes a single fracture plan, which is a worst case
24 scenario from a height growth standpoint. If there was more
25 than one fracture plane, height growth would be reduced. We
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1 looked at an MI injection case at 15 million a day, which is
2 the highest end that we would expect to inject MI at, ·and there
3 was no appreciable height growth whatsoever. We then looked at
4 water injection at an injection rate of 10,000 barrels of water
5 per day, and we saw only ten feet -- approximately ten feet of
6 upward height growth. We then looked at a prop fracture height
7 assuming some worse case prop fracture assumptions. We assume
8 we had a seventy foot interval of gross thickness, half of
9 which was pay, nominally thirty-five feet of pay, and we pumped
10 a 200,000 pound job. Under that scenario, we got a fracture --
11 upward fracture height of about 200 feet. This is well within
12 the confining zones that Steve Moothart had showed earlier.
13 With regard to the mechanical condition of our existing
exploratory well penetrations, they have all been P and A'd in
accordance with AOGCC regulations, and we have cut the casing
strings off three feet below ground level, again, in accordance
with regulations. And that concludes my testimony. Are there
any questions?
COMMISSIONER SEAMOUNT: Do you have any 200,000
pound frac jobs planned?
MR. FRAZER: Yes, we do.
COMMISSIONER SEAMOUNT: Okay.
MR. FRAZER: Two hundred thousand pounds is a
24 fairly typical type fracture stimulation. And thirty-five feet
25
of net pay and seventy feet of gross interval is about the
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necessary to proceed with implementation of our EOR project.
but, you know, we want to ensure that we have all the approvals
exemption is kind of the further guarantee beyond that, that
so I mean our -- we -- but as I understand it, the aquifer
don't see any fresh water zones, and do not -- as we ,t'estified,
20 me if you need an aquifer exemption to do that. I mean we
19 requesting the area injection order, and it's a bit unclear to
MR. STRAMP: Yeah. As I see it, we're
17 rules?
16 the aquifer exemption later or I guess included within pool
COMMISSIONER SEAMOUNT: Are you applying for
14 things.
13 We got done faster than I thought. Hunger can do amazing
MR. STRAMP: I guess I made a liar out of me.
11 questions?
COMMISSIONER SEAMOUNT: Are there any other
COMMISSIONER HEUSSER: Okay.
rates.
well that has the tubing size sufficiently to approach those
at 10,000 barrels of water per day, and we'll only have one
MR. FRAZER: The water injection rate was run
scenario water injection rate?
COMMISSIONER HEUSSER: What was the worst case
than that is likely uneconomic.
worst type of conditions we would go after. Anything thinner
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MR. MOOTHART: No.
25
24 injecting into those zones?
23 planning on -- I guess I missed that. Are you planning on
22 COMMISSIONER SEAMOUNT: But they're not
21 exemption requires review by EPA before it can be approved.
COMMISSIONER TAYLOR: Okay. The aquifer
20
19 exemption then.
18 apologize for misstating it. We are applying for the aquifer
MR. STRAMP: Okay. So, I retract our
17
MR. MOOTHART: Right.
16
MR. STRAMP: So, we're in the middle case then.
15
14 about, you don't have to have an exemption for.
13 exemption, and anything un- -- over ten you don't have to worry
you could apply for an
12 to ten you applied for an exempt
11 anything with. You know, it had to be protected. From three
10 been kind of put forth was anything under 3,000 you couldn't do
9 per million, but if I remember right, the guidelines that have
MR. MOOTHART: We've seen under 10,000 parts
8
7 that shows what that water. . . . .
6 anything under 10,000 parts per million? Do you have any data
COMMISSIONER TAYLOR: So, you haven't seen
5
MR. STRAMP: Yes, I believe so.
4
3 drinking water the way our regulation defines fresh water?
2 fresh water, the way EPA defines underground sources of
COMMISSIONER TAYLOR: Are you using the term,
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COMMISSIONER SEAMOUNT: It's.....
25
COMMISSIONER TAYLOR: Well, that's not clear.
24
23 one, right, for this injection program?
COMMISSIONER SEAMOUNT: So, they don't need
22
21 know, where we're 20 to 40,000 Kppm.
MR. MOOTHART: That's our connate waters, you
20
19 we're concern- -- we're not concern- --.....
COMMISSIONER SEAMOUNT: I think that's what
18
MR. MOOTHART: Yeah.
17
MR. MOOTHART: Oh, yeah.
COMMISSIONER TAYLOR: Okay.
16
15
.' 14 that injection zone?
COMMISSIONER TAYLOR: Do you have data as to
13
MR. MOOTHART: Pardon?
12
11 to that injection zone that you could provide?
COMMISSIONER TAYLOR: And do you have data as
MR. STRAMP: No.
. 1
2
3 the Bermuda?
4
5
6
7 those zones.
8
9 feet.
10
MR. MOOTHART: The injection zone is 4,000
MR. STRAMP: Right.
MR. MOOTHART: Right.
MR. STRAMP: We intend to remain isolated from
COMMISSIONER SEAMOUNT: Your injection zone is
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MR. STRAMP: Maybe I'm not as stupid as I
2 thought.
3
COMMISSIONER SEAMOUNT: I think what you're
4 you have to do an evaluation of the zone you want to inject in,
5 am I -- no, I'm not correct. Okay.
6
COMMISSIONER TAYLOR: It also deals with what
7 other requirements they would need an exemption from, so maybe
8 what we can do is contact Mr. Stramp with any additional
9 questions we have.
10
MR. STRAMP: Yeah, that would be fine. I don't
11 know if we have to leave the record open or what we have to do,
12 but, certainly, we are very interested in getting this as
13 resolved as we can.
14
COMMISSIONER SEAMOUNT: Okay. We'll get it
15 straightened out. Do we have to leave the record open?
16
COMMISSIONER TAYLOR: Mr. Stramp, why don't we
17 leave it that we will follow up with a letter. If we request
18 additional information from you, we'll put it in writing. That
19 way, it will keep the record open to receive whatever
20 additional information we might need.
21 MR. STRAMP: Whatever works for you.
22 COMMISSIONER TAYLOR: Okay.
23 COMMISSIONER SEAMOUNT: Any other questions?
24 Shall we close?
25
MR. STRAMP: We appreciate the opportunity to
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END OF PROCEEDINGS
8
(Off record 12:20 p.m.)
7
6 on your project, and I guess we can close now. Off the record.
5 outstanding and interesting presentation. Wish you good luck
COMMISSIONER SEAMOUNT: Thank you for a very
4
COMMISSIONER TAYLOR: Thank you.
3
2 your patience and sitting through it all, and.....
1 present this information to you this morning, and thank you for
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CERTI F I CATE
UNITED STATES OF AMERICA)
) ss.
STATE OF ALASKA )
I, Laura Ferro, Notary Public in and for the State of
Alaska, and Reporter for Metro Court Reporting, do hereby
certify:
That the foregoing Alaska Oil & Gas Conservation Public,
Hearing was taken before Sharon Gaunt on the 7th day of May,
2001, commencing at the hour of 9:06 o'clock a.m., at the
offices of Alaska Oil & Gas Conservation Commission, 333 West
Seventh Avenue, Suite 100, Anchorage, Alaska;
That the meeting was transcribed by myself to the best
of my knowledge and ability.
IN WITNESS WHEREOF, I have hereto set my hand and
affixed my seal this llth day of May 2001.
Notary Public 'n r k o u c i .and for Alaska
Y
My commission expires: 06/03/01
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ALASKA OIL AND GAS CONSERVATION COMMISSION
Date: /l?llv 7, 2 Of/ I
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PHilliPS Alaska, Inc.
A Subsidiary of PHilLIPS PETROLEUM COMPANY
Post Office Box 1 00360
700 G Street
Anchorage, Alaska 99510
Telephone 907 265-6806
Ryan Stramp, Meltwater Coordinator
RECEIVED
MAY 07 2001
Alaska Oil & Gas Cons. Commission
Anchorage
May 7,2001
Ms. Julie Heusser, Mr. Dan Seamount and Ms. Cammy Taylor
Alaska Oil and Gas Conservation Commission
333 West 7th Avenue
Anchorage, AK 99501
Re: Meltwater Area Injection Order
20 AAC 25.402
Dear Commissioners:
Phillips Alaska, Inc. (PAl) is pursing development of the Meltwater Reservoir. PAl
initially briefed the Commission on Meltwater during a January 30, 2001 meeting. PAl
subsequently submitted an application to the Commission on March 12, 2001 to
conduct an enhanced recovery operation involving MW AG (Le., alternating water and
miscible gas injection), consistent with 20 AAC 25.402 (a). Approval of the application
would permit these operations to be conducted within the proposed Meltwater Pool.
This letter provides updated technical details supporting the original application.
The following attachments are submitted pursuant to 20 AAC 25.402 (c):
1. Plat with location of all existing wells that penetrate the injection zone within one-
quarter mile of the area covered by this application.
2. List of operators and surface owners within one-quarter mile of the proposed
injection operations.
3. Affidavit showing that operators and surface owners within one-quarter mile of the
area affected by the Meltwater Area Injection Order were provided a copy of the
March 12 application.
4. Full description of the proposed operation.
5. Description, depth, and name of the pool to be affected.
6. Description of the formation into which fluids are to be injected and the associated
confining zones.
7. Type well log.
8. Casing description and proposed method for testing injection well casing.
9. Injection fluid data.
10. Estimated injection pressures.
11. Evidence and data to support a commission finding that injection wells will not
initiate or propagate fractures through the overlying strata.
12. Analysis of the water within the formation.
Phillips Alaska, Inc, is a subsidiary of Phillips Petroleum Company
')
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13. Reference to offset freshwater exemptions issued under 20 AAC 25.440 and data
suggesting no freshwater aquifers in the region.
14. Incremental increase in ultimate hydrocarbon recovery.
15. Mechanical condition of each well that has penetrated the proposed injection zone
within a one-quarter mile radius of the Meltwater Oil Pool.
I appreciate your work on the Meltwater Area Injection Order application and would be
happy to answer any related questions. I can be reached at 265-6268 or
rstramp@ ppco.com via email.
Sincerely,
11j~~~~
RUn Stramp
Meltwater Coordinator
cc: Mike Kotowski
Meltwater Area Injection Order
Page 2/32
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Meltwater Area Injection Order
Attachment 1
20 AAC 25.402 (c)(1)
Plat of Wells Penetrating Iniection Zone
The attached map (Attachment 1 A) shows all existing wells that penetrate the injection
zone in the proposed injection area. The map also shows Meltwater Reservoir seismic
anomalies and the proposed Kuparuk River Unit expansion area. Although the exact
acreage of the expansion has not yet been finalized, this map shows its largest
possible extent based on current expansion efforts. In addition, the map shows
Meltwater development wells (with their expected initial service) planned to be drilled
during 2001 and 2002 and Meltwater exploratory well penetrations. Initial well location
and service plans will likely change as net pay and well performance data are gathered.
The total number, type and locations of wells ultimately drilled into the Meltwater Pool
will also be a function of net pay and well performance data.
Since Meltwater Reservoir distribution is stratigraphically controlled and sand
accumulations are localized, sand continuity is expected to be difficult to predict.
Producer/Injector interactions will likely be difficult to predict in the absence of field
data. Development plans call for minimizing the number of injection wells until
producer/injector interactions are better understood. Producers will be converted to
injection service as necessary in order to provide pressure support and minimize
injectant cycling. Hence, to as large of an extent as possible, plans are to let reservoir
performance be a guide in optimizing pattern configurations.
Although initial development plans do not include a Class II disposal well, future needs
may eventually require one. The Ivishak Sandstone of the Sadlerochit Group has been
selected, if needed. This zone is expected to have at least 60 feet of sandstone with
porosities greater than 15% in the vicinity of the Meltwater Participating Area. The
Ivishak depth is expected to be approximately 8500 feet subsea. Several exploration
wells have been drilled to this horizon in the vicinity of the Meltwater Participating Area,
in particular, the Union Kookpuk, Union Itkillik River and Sinclair Colville wells. The
Ivishak Sandstone was wet in each of these wells and is therefore also expected to be
wet in the vicinity of the Meltwater Participating Area wells (see Sinclair Colville log
section, Attachment 11 c). The Ivishak Sandstone, as well as the overlying Shublik
Formation and Sag R. Sandstone, was wet in each of these wells. This zone is
therefore also expected to be wet in the vicinity of the Meltwater Participating Area.
The Ivishak Sandstone is separated from the overlying Kuparuk River Formation by
approximately 1800 feet of shales of the Kingak Formation, as well as approximately
400 feet of Shublik and Sag River Sandstone.
Meltwater Area Injection Order
Page 3/32
Attachment 1 A
Net Pay Map with Planned Wells
eltwater Bermu a
Int rval et Pay Map
PLANNED BERMUDA INTERVAL WELLS
PRIXJI..':ER.
INJR.'TQR J.
PLANNED CA.IRN INTEFi\lA.L WELLS
PROD'JCER .
INJEC1CR
Meltwater Area Injection Order
Page 4/32
~)
)
Meltwater Area Injection Order
Attachment 2
20 AAC 25.402 (c)(2)
Operators and Surface Owners within One Quarter Mile of Iniection Operations
Operator:
Phillips Alaska, Inc.
Attention: Dan Kruse A TO-1220
P.O. Box 100360
Anchorage, AK 99510-0360
Surface Owner:
State of Alaska
Department of Natural Resources
Attention: Mike Kotowski
P.O. Box 107034
Anchorage, AK 99510
Meltwater Area Injection Order
Page 5/32
)
Meltwater Area Injection Order
Attachment 3
20 AAC 25.402 (c){3)
Affidavit of Ryan L. Stramp Regarding Notice to Surface Owners
Ryan L. Stramp, on oath, deposes and says:
1. I am the Meltwater Coordinator at Phillips Alaska, Inc., the designated operator of
the Kuparuk River Unit (which will include the Meltwater Pool).
2. On March 12, 2001, I caused copies of the Area Injection Order Application to be
provided to the surface owner and operator of all land within a quarter mile of the
unit as listed below:
State of Alaska
Department of Natural Resources
Attention: Mike Kotowski
P.O. Box 107034
Anchorage, AK 99510
Phillips Alaska, Inc.
Attention: Dan Kruse A TO-1220
P.O. Box 100360
Anchorage, AK 99510-0360
~ 7<ya~~
......
STATE OF ALASKA )
) ssP
THIRD JUDICIAL DISTRICT )
SUBSCRIBED AND SWORN to before me this 12th day of March, 2001,
?{cd:J,u..v A:. ù....D~,,~
NU I ARY ~U[UG IN À~LJ¡:-OK ALA~KA
\\\l((({{/(((
\.\.\ ,I ~ E. Ho (/"/:
\\: n.."'\ . ' ' , '. <.< ~
\.."~'),.v. ---' .ar.,..-
.:;.- ~ -.' 0 TAb' , \I~~
.:::- 'q": ~ ~ .:.~--;'
'-~. --- .......=
~*: PUBLiC ;z~
::. ", " *-
~ . --- . ~
-::". .' '"
....." ~p).. . . hoc "
. ,', "."'~. . . . . .....l~ :\'
···;'"T'F'o-"" ~~\:\
., '.. . ~ ,......t'. '\ '\
//jJ},';j)j\
My Commission Expires: ~ t \ SI"2ëo (
Meltwater Area Injection Order
Page 6/32
)
Meltwater Area Injection Order
Attachment 4
20 AAC 25.402 (c)(4)
Description of the Proposed Operation
The Meltwater Area Injection Order is needed to develop the Meltwater Reservoir. The
expected scope of the current development project involves drilling approximately 26
wells to develop 52 MMBO associated with an estimated 132 MMBO original oil in
place (OOIP) seen by existing exploratory wells in the Bermuda Interval of the
Meltwater Reservoir. Although Attachment 1 A shows 41 penetrations, this is
considered an upside case.
Field Development
Development wells will be drilled from a single new drill site. Initial development drilling
operations are planned to start during the second quarter of this year, The drilling
program will initially focus on developing the main portion of the reservoir and testing
the periphery, Well performance data and improved seismic calibrations acquired from
the initial development wells will help guide the extent of the overall development drilling
program,
Exploratory drilling targeting other zones within the Meltwater Reservoir will be
conducted concurrently with development drilling operations, Successful exploratory
drilling results could alter existing plans by (1) changing the location and target interval
of the initial development wells and (2) expanding the scope of the project to include
additional wells, An expanded project scope would likely involve additional
development drilling phases and may require an areal expansion of the proffered
Meltwater Area I njection Order.
Recovery Mechanism
Initially employing an MW AG recovery process, which consists of alternating cycles of
water and MI, is a key aspect of the planned development. Following are the main
reasons for the
1, Numerical simulation indicates that MW AG provides higher recoveries than any
other competing recovery process (Le" primary drainage, waterflood, miscible gas
flood, and lean gas flood), For example, simulation results suggest that an
MW AG process, with a 20% cumulative hydrocarbon pore volume slug of injected
miscible gas, would provide an incremental recovery of 90/0 001 P compared to a
waterflood process,
2, Enriched natural gas used at Kuparuk is miscible with Meltwater fluids at reservoir
conditions. (Henceforth in this document, enriched natural gas will be referred to
as "MI" for Miscible Injectant.) This is supported by slim tube simulation results
and is consistent with actual slim tube experiments run on Tarn crude. (Given that
the composition of Meltwater and Tarn crudes are very similar, they should behave
in a similar fashion from a phase behavior and fluid displacement standpoint.)
Meltwater Area Injection Order
Page 7/32
')
)
3. Greater Kuparuk Area (GKA) MI is currently piped to offset Tarn Drill Site 2N and
is transportable to Meltwater for a relatively small premium,
4, Initially pursing MW AG is imperative if this EOR process is to be employed,
Meltwater's MI supply is dependent on existing west-end GKA infrastructure, The
MW AG floods in this part of the GKA are relatively mature, Delaying
implementation of MW AG at Meltwater would therefore jeopardize this project's
EOR reserves, as critical GKA infrastructure may not be available in the future to
transport MI. (Other potential uses of the GKA MI distribution system include de-
bottlenecking production/injection lines and providing high pressure lift gas),
After the cumulative target slug size of MI has been injected into the formation,
pressure support will be maintained with water injection. Current plans are to
eventually inject lean gas into the reservoir to help recover light liquid hydrocarbons
(used to manufacture MI) that will be trapped in the reservoir by the MWAG process,
Injectant Sources
The miscible injectant employed at Meltwater will initially be the same injectant as that
currently used at Tarn and the Kuparuk River Unit Large Scale EOR Project. This
injectant is manufactured at Kuparuk's CPF-1 and CPF-2 by blending lean gas from the
Kuparuk River Unit's production facilities with light hydrocarbon liquid streams from the
Prudhoe Bay Unit and Kuparuk River Unit. The light liquid hydrocarbons from the
Prudhoe Bay Unit are NGLs from the CGF. The light liquid hydrocarbons from the
Kuparuk River Unit consist of scrubber liquids from artificial lift gas compression
systems at CPF-1 and CPF-2, NGLs from CPF-1 and naphtha from the Topping Plant.
During the flood, there is a possibility that Meltwater produced gas may be blended with
Kuparuk River Unit MI to generate a lighter MI blend customized for the Meltwater
Reservoir pressure and oil properties, Slim tube simulation results and slim tube
experiments on similar (Tarn) crude indicate that Kuparuk MI is richer than needed to
achieve miscibility with Meltwater oil at reservoir pressure (2400 psig in the Meltwater
#1 well),
After the cumulative target slug size of MI has been injected into the formation,
pressure support will be maintained with water injection, Current plans are to
eventually inject lean gas into the reservoir to help recover light liquid hydrocarbons
(used to manufacture MI) that will be trapped in the reservoir by the MWAG process,
The source of the lean gas will be Kuparuk River Unit's CPF-2, Potential gas
accumulations in the area will also be considered as possible supplemental sources,
Meltwater Area Injection Order
Page 8/32
')
')
)
Fluid and Cost Allocation
Meltwater production will be commingled with Tarn and Kuparuk production in surface
facilities prior to final processing and ultimate custody transfer in accordance with the
Meltwater Pool Rules (currently being developed), The Greater Kuparuk Area
Alignment Agreement, which set new tract ownership and facility sharing terms in the
Meltwater area, will help govern business issues associated with sharing infrastructure,
A portion of the Meltwater accumulation extends outside the existing GKA onto a
PAI/BP lease (see Attachment 4A), All GKA owners, except Exxon-Mobil (with a
.3648% GKA working interest), have agreed to buy interest in the lease. Mobil heritage
interest was proportionately split between Phillips and BP based on an estimate that
40.6042% of total Meltwater net sand volume is located on this lease, No future
production interest adjustments will be made, The resulting Meltwater cost and
production working interests, pending approval of the Supplemental Provisions, are as
follows:
Cost Production
Phillips Alaska, Inc, 0,55957929 0,55379056
BP 0,39754111 0.39342864
U nocal 0,03960480 0,04950600
Mobil 0,00218880 0,00218880
Chevron 0.00108600 0,00108600
Total 1 .00000000 1 ,00000000
I njection Area
The proposed area of injection, which corresponds to the proposed pool area, is
depicted in Attachment 4B.
Meltwater Area Injection Order
Page 9/32
•
e
Attachment 4A
Meltwater Accumulation Outside Existing GKA
Meltwater Area Injection Order Page 10/32
Attachment 413
Proposed Injection Area
PAI55.29377
PAI55129377
T
BP 39.28223
BP 39.28223
S �1
UCL 4.9506
UCL 4.9506
MOBB 0.3648
MOB 0.3648
Delta
CH 3y.N86
C�1y116i086
Ku+paru
Rive
Unit
JC
Un
t 36
31
ALK4292
ALK4294
ALK4296
ALK4299
ADL375072
ADL375076
ADL375080
ADL375079
A
'A! lU0
PAI55.29377
PAI 55.28377
BP 39.28223
BACHN
6 BP 39.28223
UCL 4.9506
UCL 4.9506 1
6 FORSG
MOB 0.3648
MOB 0.3648
CHV 0.1086
CHV 0.1086+
+ +
+
10-31-05
10 �8
a e
11-30-98
00-
No
+ +
+
e
North
o
ADL389056
Q 2
ALK4710
ADL373111
ADL3
AP
AI 56.4649
BP 41.5351
_ �_
ATOFI
Cairn South
+
+North
Interval Netpay
Bermuda
10-31-05
10-31-05
Interval Netpay
10-3
PAI 55.507024
PAI 55.507024
+
BP 39.433776
+ UCL 4.950f-
SP 39.43377
+UCL 4.9506�
4-
CHV 0.1086
CHV 0.1086
(Subject to DNR Approval)
(Subject to DNR Approval)
36
31
36
31
DL389057
ADL389058
ADL389059
ADL3
PAI 58.4649
PAI 58.4646
PAI 58.4649
APC
BP 41.5351
BP 41.5351
BP 41.5351
ATOFI
1
1
6
Proposed Meltwater
+
Iniection Area
+ +
+
10-31-05
10-31-05
10-31-05
10-3
PHILLIPS Alaska, Inc.
+
+ +A
Subaldlery o� PHILLIPS PETROLEUM COMPANY
O /2 1 2
MILES
Proposed Meltwater
DL389043 -
ADL389046
1
Injection Area
Al 58.4649
PAI 100
P 41.5351
-- -
4-24-01 01030104C01
Meltwater Area Injection Order Page 11/32
)
)
Meltwater Area Injection Order
Attachment 5
20 AAC 25.402 (c)(5)
Description and Depth of Pool to be Affected
The Meltwater Reservoir is the sequence of reservoir sandstones and associated
mudstones found in the interval between 4958' and 5368' tvd subsea in the Meltwater
North #2A well, and in its lateral equivalents. The Meltwater Reservoir is late
Cretaceous in age and stratigraphically within the Seabee Formation. The reservoir is
approximately 400' thick and is composed of two intervals. The initial Meltwater Oil
Pool includes the entire Meltwater Reservoir, however, the pool definition may change
as additional information from development and exploratory activities becomes·
available.
Both Meltwater and Cairn Reservoir intervals are shown in the wireline log from the
Meltwater North #2A well (see Attachment 7). Brief summaries of these intervals are
given below in descending order.
. The 'T4.1', or Cairn Interval, was encountered between 4958' and 5187' tvd subsea
in the Meltwater North #2A well. The boundaries are correlatable markers T 4.1 and
T3, respectively. Reservoir quality sands were not encountered at this location, but
may be present laterally.
. The Bermuda Interval was encountered between 5187' and 5297' tvd subsea in the
Meltwater North #2A well. The boundaries are correlatable markers T3 and T2,
respectively. Hydrocarbon-bearing sands in this interval were encountered in the
Meltwater North #2A and in two offset wells.
Two Meltwater Reservoir intervals, the Bermuda Interval and Cairn Interval, are
sufficiently understood to be included in development plans. Initial injection will be
restricted to these two intervals. An expansion of injection operations (both vertically
and areally) may be sought in the future depending on results from upcoming drilling
activities.
Meltwater Area Injection Order
Page 12/32
')
)
Meltwater Area Injection Order
Attachment 6
20 AAC 25.402 (c)(6)
Description of the Formation
The proposed injection zone includes the Cairn Interval and the Bermuda Interval within
the Meltwater Oil Pool. This zone lies between 4958' and 5368' tvd subsea in the
Meltwater North #2A well (Attachment 7). The Cairn Interval lies between reservoir
markers T3 and T 4.1 while the Bermuda Interval lies between reservoir markers T2 and
T3.
The Meltwater Pool sands are fine- to very fine-grained and have common shale
laminations and interbeds. Sands are compositionally heterogeneous: the major
components include quartz, heterolithic rock fragments, plagioclase and zeolite. Shale
laminations are common.
Reservoir sands, which are locally developed within each interval, are lobate to linear in
form, and are separated from adjacent reservoirs by mudstones and shales. The top of
the Meltwater Reservoir is separated from the Tabasco Sandstone equivalent, the first
overlying potential reservoir zone, by a confining layer of approximately 3000' of
impermeable shale (Attachment 11 A). The base of the Meltwater Reservoir is
separated from the underlying Kuparuk River Formation by approximately 500' of shale.
Meltwater Area Injection Order
Page 13/32
Meltwater Area Injection Order
Attachment 7
20 AAC 25.402 (c )(7)
LOQ of Meltwater Tvpe Well
MELTWATER NORTH 2A
Meltwater Area Injection Order
Page 14/32
\)
)
Meltwater Area I njection Order
Attachment 8
20 AAC 25.402 (c)(8)
Casing Description and Proposed Method for Testing Casing
The proposed casing programs for a typical Meltwater well resembles the casing
programs employed in the Kuparuk River Unit (KRU). Although the standard program
incorporates maintaining a tubing annulus with isolation and pressure integrity within
200' of the initial producing interval, exceptions to this design criterion will be required
to optimize recovery from potentially productive secondary targets.
Standard Casing Program
As in KRU wells, conductor casing will be set below 75 feet to provide anchorage and
support for the rig diverter assembly. The surface casing size may be 9-5/8 or 7-5/8
inch, depending on casing setting depth and production tubing size. Surface casing will
be set below the base of the West Sak interval, effectively casing off the permafrost,
Ugnu, and West Sak formations.
Meltwater wells utilize a tapered casing string tied back to surface, that serves as the
combination production casing / tubing string installation. The casing adjacent from the
producing interval is the same size as the tubing is at the surface (monobore). The
casing across the production interval is then tied back to surface with a string of 3Y2 or
4112 inch tubing inserted into a seal bore or polished bore receptacle (positioned above
the top pay zone perforation.) This provides a tubing annulus with isolation and
pressure integrity (see diagrams shown in Attachment 8A).
There are three casing programs proposed for the Meltwater development:
Case 1) 3Y2 inch Slimhole Monobore completions. This casing program utilizes a
7-5/8 inch (L-80, 29.7 pound) surface casing string with a production string of
5Y2 inch (L-80, 15.5 pound) casing crossed over to 3Y2 inch (L-80, 9.3 pound)
casing across the Meltwater interval. These monobore wells will be
completed with 3112 inch (L-80, 9.3 pound) production tubing.
Case 2) 4Y2 inch Monobore completions. This casing program employs 9-5/8 inch
(L-80, 40 pound) surface casing with 7 inch (L-80 or J-55, 26 pound)
production casing crossed over to 4Y2 inch (L-80, 12.6 pound) production
casing.
Case 3) 3Y2 and 4Y2 inch Conventional completions. This casing program employs
a string of 9-5/8 inch (L-80, 40.0 pound) casing and an intermediate 7 inch (L-
80 or J-55, 26 pound) intermediate casing string set above the Meltwater
formation top. A 3Y2 inch (L-80, 9.3 pound) or 4Y2 inch (L-80, 12.6 pound)
liner would then be set across the Meltwater formation and tied back to
surface with either 3Y2 inch (L-80, 9.3 pound) or 4Y2 inch (L-80, 12.6 pound)
production tubing.
Meltwater Area Injection Order
Page 15/32
')
)
Each of these three well types may be completed for either production or injection
service. The service of the well will be determined after logging operations. Drilling
and completion plans for future Meltwater wells may vary with time as experience and
knowledge are gained.
The proposed method casing testing method for Meltwater injectors is to follow the
requirements of 20 AAC 25.412 (c & d). Sufficient notice of pressure tests will be given
so that a Commission representative may witness the test.
Secondary Targets
The Bermuda Interval will be the primary target of initial development efforts. Current
plans are to focus initial development efforts on that portion of the interval most likely
have good reservoir characteristics. As previously shown on Attachment 7, potentially
productive secondary targets in the Cairn Interval may be encountered during these
development efforts. Secondary targets in the Cairn Interval are expected to generally
be within 400' tvd of the Bermuda Interval. These thin, potentially productive zones
contain insufficient reserves to merit separate wells or extensive completion design
modifications. Although fracture stimulations are planned for Bermuda Interval
producers, fracture modeling indicates these stimulations will only grow approximately
100' upwards. Potentially productive secondary pay zones can therefore only be
developed if they can be inexpensively commingled with Bermuda production.
Given the initial uncertainty of producer/injector interactions, most producers will be
candidates for conversion to injection service. In order to maintain conversion
flexibility, there are no casing design differences between production and injection
wells. (Casing connections will be designed for gas or liquid service.) The flexibility to
convert wells to injection service on an as needed basis is an integral part of the
Meltwater development strategy. This complicates secondary target development as
these targets can only be pursued if they are not isolated by more than one casing
string.
Pursing secondary targets may result in exceeding the AOGCC guideline that injectors
provide annular isolation within 200' measured depth of the highest perforated interval.
Plans are to provide annular isolation within 200' measured depth of the perforated
zone, unless secondary targets are encountered with a pay thickness approaching or
exceeding 10' tvd. Based on current drilling and facility hook-up plans, the productive
nature of these secondary targets can not be fully ascertained during initial drilling
operations. If future evaluations indicate that developing secondary targets can not be
justified, there is the potential of having either current or future injectors with annular
isolation located more than 200' measured depth above the perforated zone. Meltwater
Oil Pool Rules are written to help ensure that well service flexibility is not sacrificed by
attempting to pursue thin secondary targets.
Meltwater Area Injection Order
Page 16/32
')
)
Meltwater Area Injection Order
Attachment SA
20 AAC 25.402 (c)(8)
3-1/2" Slimhole Monohore
Completion
FMC Prudhoe Gen V L., i
9-5/8x5V,x3V, I
;:;,:~ ~~;~ J:J'i
~
2.875" CAMCO~/
DS nipple for Ii
Possible K-Valve
I
! I
9-7/8" Hole
!
],.
7-SI8" Surface Casing
al 2.500' TVD
6*" Hole
~
I~
I
-
I
I
I
l
I
I
I
f
I :
I .]
I
Í¡ .Wz"lubing
¡~
I
¡
Baker CMU Sliding ~ ¿ -
Sleeve w/2.813" DS' ~
Cameo profile ~
: . CAMCO 2.75"
Cameo 3V,' x 1" ........---.... DS nipple
side pocket GLM ., j I
...~
St¡¡" Casing
S~aL R~ceptack
(CSR)
Cross~d owr to
.Wz"lubing
aI5.000· '[V)
Meltwater Area Injection Order
~
~I/Z" Produclion Casing
at 5.200' TVI)
13:1SC of
p~nnafrosl
at 1.250' M)
13as~ of
West Silk
at I ,800' 'IV [)
FMC Prudhoe Gen V L.,
9-5/8x7 x 4V, I
L,
~
12'1/' Hole I
I
I
l...
9-SI8" Surf. Csg.
at 2.500' TVD
81h" Hole
7" Casing
S~aL R~œptadc
(CSR)
Cross~d ov~r 10
4t¡¡" casing
at 5.000' TVD
3-112" or 4-1/2"
Monohore Completion
~
~
-r
rOO';bI' K "..
I
~
Jt¡¡" or 4'/Z"
~akerCMU
Sliding Sleeve
wl3.812" Cameo
~"""
side pocket GLM
-.¥~
~
\
CAMeo 3.75"
DB nipple
('
! 1 '
. ~t¡¡', or41/z"
L-,LI Ja( 5,200' TVI)
Page 17/32
)
)
Meltwater Area Injection Order
Attachment 9
20 AAC 25.402 (c)(9)
Injection Fluid Analysis
The vast majority of the MI initially employed at Meltwater will originate from Kuparuk
River Unit's CPF-2. During 2001, both MI and water will be employed to provide
pressure support and maximize sweep. After completing the MWAG recovery process,
plans are to eventually inject lean gas into the Meltwater Oil Pool to maximize recovery
of the light hydrocarbon liquids that were injected into the reservoir as part of the
miscible injectant stream.
The source of the lean gas will likely be Kuparuk River Unit's CPF-2. However, other
potential gas sources will also be considered. The initial water injection source will be
CPF-2 produced water. Local separation and reinjection of water at Meltwater may be
considered in the future. Fresh water collected in well cellars from snowmelt may also
be injected for short time periods to minimize road traffic during the caribou calving
season.
The average MI and lean gas composition produced at the Kuparuk CPF-2 facility
during 2000 is presented below. Also shown below is a CPF-2 produced water analysis
from February 2000.
Maximum MI/lean gas and water injection rates into the Meltwater Oil Pool are
estimated at 80 MMSCFPD and 65 MBWPD, respectively.
There is no evidence from laboratory core flood experiments or compositional studies
that indicate the fluids proffered for long-term injection would pose any appreciable
compatibility problems for either the Meltwater Formation or its confining zones. Short
periods of fresh water injection are also not expected to cause any appreciable
compatibility problems. If injectors do incur damage from fresh water injection,
remedial treatments (e.g., acid stimulations, high pressure breakdowns, etc.) can be
employed.
Meltwater Area Injection Order
Page 18/32
)
)
Miscible Injectant & Lean Gas Composition Supplied by
the Kuparuk River Unit's CPF-2
Component Lean Gas MI
(Mole 0/0) (Mole 0/0)
CO2 0.89 0.5
N2 0.27 0.3
C1 81.37 69.6
C2 8.79 6.7
C3 5.10 5.0
i-C4 0.92 2.2
n-C4 1.99 6.3
i-C5 0.30 2.0
n-C5 0.28 2.5
C6 0.07 2.1
C7 0.01 1.8
C8+ 0.00 1.0
CPF-2 Produced Water Analysis
Sulfate
Sulfide
Bicarbonate
Aluminum
Ammonia
Barium
Boron
Calcium
Chloride
Chromium
FI uoride
Iodide
Iron
Lithium
Manganese
Magnesium
Phosphorus
Potassium
Silicon
Sodium
Strontium
Concentration
(m gll)
159
12
1,920
<0.15
20
35
18
137
13,131
<0.06
<10
12.6
0.74
1.2
<0.003
99
<0.5
60
20
8,800
6.7
Component
Meltwater Area Injection Order
Page 19/32
)
)
Meltwater Area Injection Order
Attachment 10
20 AAC 25.402 (c)(10)
Estimated Pressures
The maximum MI and water injection pressures available at the plant will be 4,400 psi
and 3000 psi, respectively. Due to pressure losses in the distribution system, actual
maximum wellhead pressures will vary. Injection wells may also be choked to avoid
exceeding injection targets. MI and water wellhead injection pressures are expected to
range from 2,600 - 3,600 psi and 1600 - 2600 psi, respectively.
Meltwater Area Injection Order
Page 20/32
)
)
Meltwater Area Injection Order
Attachment 11
20 AAC 25.402 (c )(11 )
Fracture Information
Injection into the Meltwater Formation will not breach the reservoir's confining zones.
Neither injection nor formation fluids will be able to enter any freshwater strata.
Although bottom-hole pressures may exceed the formation parting pressure during
enhanced recovery operations (Le., water and MI injection), the Meltwater producing
sands are separated by over 2000' of confining shales and mudstones which act as an
impermeable barrier (see Attachment 11 A). These confining layers provide a
substantially greater barrier than necessary to contain fractures within the Meltwater
interval. Fracture modeling using Stimplan (Le., Nolte/Smith's quasi 3-D model)
confirms this as predicted fracture heights are entirely contained within the perforated
interval. For example, injecting water at a rate of 10,000 BWPD at a surface pressure
of 2200 psi would result in upward fracture growth of only 10'. Injecting MI at an
injection rate 15 MMSCFPD at a surface pressure of 3500 psi would cause no
appreciable height growth.
The above-mentioned fracture modeling is based on single, planar, vertical fractures
that result from relatively short duration injection. Since these modeling captures
neither dentritic fractures nor disaggregation (i.e., destruction of the rock matrix), model
predicted fracture growth associated with long term injection is too large.
Hydraulically propped fracture stimulations are planned for Meltwater producers. The
1500' of confining shales and mudstones also provide a substantially greater barrier
than necessary to contain these fracture stimulations. Fracture modeling using
Stimplan suggests that typical fracture stimulations will grow upward approximately
100'. Model runs with worst case assumptions (which cause the most upward growth)
suggest the stimulations will not exceed 300' of upward growth. For example, a
fracture stimulation with 200,000 pounds of proppant with only 70' of gross interval is
forecasted to result in a maximum upward fracture height of approximately 200' (see
Attachment 11 B).
As previously mentioned, no disposal injection is initially planned in the Meltwater
Participating Area. However, the Ivishak sandstone is being permitted for Class II
disposal to address potential future needs. Approximately 2000' tvd of confining rock
separate this zone from Meltwater Reservoir strata. In addition, there are no potential
fresh water strata within several thousand feet of the zone (see Attachment 11 C). If the
Ivishak is used for disposal injection in the future, modeling will be conducted at that
time using the best available tools to help ensure that the planned disposal volumes
pose no risk to either potential freshwater strata or hydrocarbon recoveries.
Meltwater Area Injection Order
Page 21/32
Attachment 11 A
Meltwater North #2A Confining Intervals
MELTWATER NORTH #2A
GAMNA RAY í RESISTIVITY
~
::J
~ ~
~ f.!:
!!...
ID
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j¡ u
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I I!M)_O~ I
~ .......1 111I
MElí'lllAT!;'Fc
POOL
Meltwater Area Injection Order
Page 22/32
Attachment 11 B
Stimplan Results-Worst Case Height Growth
Stress (Jsi)
,¡
,
,
,
,
,
·
,
·
.......
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,
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5400
5800
Max Width 0 93 in
Il)
ro
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en
.. .. ... + .. ..
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...+.....+...+.+...+~......+~++...+...
... '" '" . .. '"
.. .. .. . .. ..
Phillips Alaska Inc.
t'-1eltwater Frac 2
,A,t Closure
=
o
Il)
(IJ
s:::.
f.l)
-0 .E-O .4-0 .::<-0.0 0.2 0.4 0.6
5200
·
·
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,
·
'" '" .. '" ..
++*+++++*+++++++++-++++++++9+++++++++.++++++++-++++++++
'" '" ., '" '"
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., '" '" '" ...
... .. ... '" ...
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.. .. .. '" .
.. -+ '" -+ ..
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+++.+++++++++_++++++++_+++++++++ø++++++++*++++++++
'" '" . .. ..
· '" '" '" ..
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· : Pad: : :
: Area: : :
: I : : :
.. I .. .. '"
++.J+++++++9+++++++++.++++·+++*++++++++
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......1.........[........1....11..
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.++#.++++++++~+++++.++#+++++++++~+.++++++~++++++++
· '" '" .. ..
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+ .. .. '" '"
'" '" '" .. 0/1
'" -+ '" '" '"
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5300
5400
5500
5600
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100
200 300 400
Fracture Penetration (ft)
500
.
.
o -+ .. + + .. 0/1 .. '" '" ..
CJ ++++++++i+++++++++++}+++++++~+++·++·+~·++·+++++++t++·+++++t+;¡¡++++.++...+....+~.++.+++·;·+·++·++}+++++·++++
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.. .. .. .. .. .. .. .. .. +
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++++++++)++++··+++++~+++++·+~··++·+··.·++·++··++·i++++++++t++··+··+t++++··+++·+~+++··+++>·+++++++>+++··+·+·+
.. .. .. .. .. .. .. .. .. ..
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++++.++*~++++.+++++~+.++.++~++++.+.+~.++.++.++++~++.+..++.+.+++.+.~+++++.+++++~+++++++~+++++++~++++++++++
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++...+...+......+..~......+~..+...+.........+..~...+.*.+.+........+++++.+.+++.+...+.+~+++...+~.++.+..+.+
.. .. *' '" -+ .. .. -+ + -+
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.. -+ .. .. . -+ . .. .. ..
+++++.++~++++++++++~+.++.++~+..++++~+++++++++++~.+.++.++~......+++++..+.+++++~+.+.+.+~.++++++~++...+++..
.. .. -+ .. .. . . .. . .
· . '" . .. .. . . + -+
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Il)
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E:' lD
CL
.µ
Il)
z
0
N
0
20
50 100
Time (min)
200
500
1000
2000
Meltwater Area Injection Order
5.0
10
20
Page 23/32
Attachment 11 C
Sinclair Colville #1 Confining Intervals
Meltwater Area Injection Order
1m
iU'J
/ri.
i
iJit.
, ::J
\ L-
IfO
\g.
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--
C
---
Sinclair
Colville #1
Well
Page 24/32
Meltwater Area Injection Order
Attachment 12
MC 25.402 (c)(12)
Formation Fluid
No oil-water or gas-water contacts within the Meltwater formation have been
encountered.
In the Bermuda interval at Tarn, average salinity estimates from immobile connate
water were estimated from low invasion cores. Connate water was obtained from core
plugs using a miscible (CHCI3 / CH30H) extraction process. Subsequent water
volumes were estimated using Karl Fisher analysis and chlorides were measured using
ion chromatography. The resultant estimated connate water NaC! concentration was
30 Kppm.
Anomalous lab results on Meltwater cores indicate a chloride content in the Bermuda
Interval at Meltwater North of 20 Kppm NaCL Due to uncertain lab procedures, Core
Labs has little confidence in this value and estimates the actual value (based upon
anion calculations) to be in the 35-40 Kppm NaCI range. Further testing on subsequent
cored wells at Meltwater is planned.
Meltwater Area Injection Order
Page 25/32
Meltwater Area Injection Order
Attachment 13
20 MC 25.402 (c)(13)
AQuifer Exemption
The proposed Meltwater pool lies just south of the current Kuparuk River Unit (KRU)
exemption area established by the EPA on May 11, 1984 (see Attachment 13A). An
extension of the existing KRU Aquifer Exemption Area is being sought. Analysis of all
available data indicates there are no potential fresh water sands suitable for human
consumption in the proposed Meltwater injection area.
No porosity logs were acquired in the surface portion (above approximately 1900' tvd
subsea) of the Meltwater North wells.
Wells in the general vicinity of the proposed Meltwater injection area (Le., Kalubik #1,
Colville River St. #1, Cirque #2 and 2N-349) were analyzed for fresh water acquifers
using the SP Technique and the RWapparent Technique. (The RWapparent Technique is
referred to as the Resistivity-Prosity Technique, or "RP", in literature.) Both are
well known techniques within the industry. Discussion is provided below on the
limitations of each method and the associated salinity estimates.
Two of the wells (Kalubik #1 and Colville River St. 1) are outside the existing KRU and
Alpine Aquifer Exemption Areas. The third well (Cirque is located within the KRU
Aquifer Exemption Area.
following table is a list of salinity calculations for the sand underneath the
permafrost. Calculated fluid resistivities are corrected to 75° F and salinity numbers are
NaCI equivalent, or total dissolved solids (TDS).
Kalubik #1 Colville River St 1 Cirque 2 2N-349
Rmf = I.l9 Q-m @ 69° Rmf = 2.52 Q-m @ 68° Rmf = 2.28 Q-m @ 85° Rmf = 3.3 Q-m @ 63°
Permafrost @ 1510' Permatì'ost @ 1360' Permafrost @ 1170' Permatì'ost @ 131 0'
Sand @ 1740'-90' Sand @ 1510'-20' Sand @ 1440'-60' Sand @ 1905'-15'
$ = 36 Rt = 12 Qm $ = 36 Rt = 2.1 Qm $ = 34 Rt = 26 Qm $=31 Rt = 10 Qm
Rwa = 1.09 Qm Rwa = 0.24 Qm Rwa = 2.1 Qm Rwa = 0.8 Qm
(5.3 Kppm) (28 Kppm) (2.5 Kppm) (6.9 Kppm)
SP = -35 mv (@ 35°) SP = -40 mv (@ 34°) SP = -20 mv (@ 35°) SP = -20 mv (@
RwSP = 0.38 Qm RwSP = 0.5 Qm RwSP = 1.03 Qm 44°)
(15 Kppm) (20 Kppm) (5.4 Kppm) RwSP = 1.19 Qm
(4.5 Kppm)
Hole badly washed Zone slightly shaly. Hydrates known .SP Hydrates below
out. SP probably Salinities quite high. more representati ve Permafrost R wa
more representative. though still too low. more representative.
Meltwater Area Injection Order
Page 26/32
In the Kalubik and Cirque wells, average resistivities drop dramatically below these
sands, indicating much saltier waters. In the Colville well, the high salinities begin at
the base of permafrost.
2N-349
Base Permafrost picked at 1310' with the section below interpreted to be hydrate
bearing. This is supported by a shallow gas sample log obtained in the 2N-305 well
(see Attachment 138). Shale resistivities suggest salinities in the 6-10 kppm range.
Rwa in the sand at 1910' calculates TDS of 6.9 kppm.
This section of the well has wireline logs to 2330' with LWD below that. LWD resistivity
decreases systematically below 2400', implying an increase in salinity below that depth.
There are no appreciable sands present below in which to verify this salinity, though
estimates from the shales would suggest salinities of 20+ kppm TDS. Included as
Attachment 13C is a plot of Rwa versus depth for the shallow portion of this well.
Kalubik
Water salinities below permafrost are estimated to be in the 10-12 Kppm range (TDS),
increasing to 25 Kppm below 1950'. An analysis of a water sample from Albian aged
sands (5050-5250') in this well tested 24.3 KPPM TDS.
Colville River St. 1
Salinities below permafrost are approximately 25 Kppm TDS.
Cirque 2
Under permafrost, salinities are 6+ Kppm increasing to 21 Kppm below 2200'. The
sand immediately below the permafrost is believed to contain gas hydrates. This
causes log based salinity calculation results to be too low.
None of the wells exhibit decreased salinity below these depths.
Meltwater Area Injection Order
Page 27132
Attachment 13A
Regional Aquifer Exemption Map
AlpineAquifer
Exemption
Kuukpik
Kalubik 1
.
S:ar
Milne Point
Kuparuk River
Prudhoe Bay
Alpine Pool
Sections
2N-349
.
Proposed
Meltwater Pool
2
Greater Kuparuk
Aquifer Exemption
N2
Meltwater Area Injection Order
Page 28/32
Attachment 138
Tarn 2N...305 Shallow Cuttings Samples
T RN 2N-305 SHALLOW CUTTINGS GAS SAMP S
C02
neoG5
Meltwater Area Injection Order
Gas
Hydrates
Page 29/32
Attachment 13C
Rwa vs.. Depth for 2N....349
W ¡ EP
C ssp I
(OHMM)
Meltwater Area Injection Order
Page 30/32
.
.
Meltwater Area Injection Order
Attachment 14
20 AAC 25.402 (c)(14)
Incremental Hydrocarbon Recovery
The Meltwater Sand was tested in the Meltwater #1 exploration well. Fluids recovered
from the test indicated the interval contains 36° API gravity crude with a solution GOR of
approximately 620 SCF/B. There is no evidence that this zone is in contact with either
an aquifer or gas cap to provide pressure support.
Simulation results indicate that an MWAG process with a cumulative 20% hydrocarbon
pore volume slug of MI would provide an overall recovery factor of approximately 38%
OOIP. This recovery factor is approximately 9% OOIP higher than that obtained from
waterflood and more than 20% OOIP higher than that obtained from primary depletion.
Meltwater Area Injection Order
Page 31/32
.
.
Meltwater Area Injection Order
Attachment 15
20 AAC 25.402 (c)(15)
Mechanical Condition of Existing Penetrations
There are no active wells within a one-quarter mile radius of the Meltwater Oil Pool.
However, two exploratory wells and a sidetrack were drilled to evaluate the area.
These penetrations have been plugged and abandoned as per AOGCC regulations (20
MC 25.112). All casing strings were cut three feet below the original ground level with
well abandonment markers installed as per 20 MC 25.120. The well cellars were
removed and the remaining holes back filled to ground level with gravel.
Meltwater Area Injection Order
Page 32/32
I
I I
I
eti
eo I
Reservoi
IIi 9 a
S a
S a
Stra
Steve ootha
La 0
o pletio s
eil es
ya Stra
Stra
"* A Written Brief Has Also Been led
2
May 7, 2001
3
May 7, 2001
4
III Drilled Wells
IIITested MWN#1
1 Sidetrack 1 Q2000
Meltwater North
Well Test Rates & Pressures
5000
4500
4000
"C 3500
Q.
.Q 3000
~ 2500
~ 2000
Õ 1500
1000
500
o
o
20
40
60
80
Flowing Time, Ius
May 7, 2001
1000
.¡¡¡
Q.
Ii'
l-
LL
..
500 ~
ö¡:::
o
III
ci
o
C)
o
100
reate I et
Ie In
.. ..
" I I
" )
ross Reserves ....
5
May 7,2001
-Construction egan J nuary 2001
-All n dra Construction Now Complete
- urrently rilli g irst evelopment ell
- n-Pad Constructio In Progress
- nticipate irst Production By ct. 1, 2001
6
May 7, 2001
-
I ieatio
.. ..
IS SSI S
- la S I ress
- Expand Kuparuk River U it
- Form Meltwater rticipating Area
-
-
7
pli 0 S
ill I el e
peratio s, a
e iI i
alia S fo
ploratio
ay 00
Develop e
May 7, 2001
8
Attachment NO.5
Proposed Kuparuk River
Unit Expansion and
Meltwater Participating Area
01030104AOO
May 7, 2001
hillips Alaska, Inc.
B Exploration (Alaska) I
Unocal
obil ( eritage)
Chevron
Total
eltwater Lease old
Parti pation Interests
55.380345%
39.343780%
.950600%
0.216676%
0.108600%
1 00.000000%
Agreed Among Owners
Lease Assignments Not Yet Complete
9
May 7, 2001
" aste a ote se 0
" I
" ate Reeove
" pa est Sak,
,
Slope ools
10
May 7, 2001
el
ate
11
5500 7300
8'
187'
9
,
May 7, 2001
001
Alaska, Inc.
A SubSldla.ry of PHILLIPS PETROLËUM COMPANY
Proposed Meltwater
Pool Area
01030104C01
12
May 7,2001
13
May 7, 2001
14
May 7, 2001
May 7, 2001
May 7, 2001
Tam Net Sand Map
May 7, 2001
el
a
4900.00
5000.00
5100.00
(.i
~
c:o::t
(.i
5200.00
00
5300.00
5400.00
2200
Subs ea Depth .vs. Fonnation res sure
Tam 3APres s ures
Tam 3AOil Gradient
Tam 4 Pres s ures
Tam 1 Pres sure
- Tam 4 Gradient(?)
" 2L-315 Pres sure
29
2L-315 Oil Gradient
Arete Gas Gradient
MWN 1
MWN 1 Gradient
MWN2A
MWN 2AGradient
2L rp Gas cap
at 5 1 4 1 f S s tvd
2250
2300
2350
2400
50
2500
Formation
s sure
May 7, 2001
19
Tam
Tam 4
. MWN
MWN2A
MWS
Sandstones are qnartz Poor (20%) bulk QM + QP + chert
Largely comprised of SRF, MRF, and VRF rock fragments
SRF's and MRF's are argillaceous (structural clay)
VRF's are largely pyroclastic glass shards altered to analcite
Analcite cement locally fills pores around the remnant shards
l
May 7, 2001
4
"
MWN2A
SRF's and MRF's are argillaceous (structural clay)
VRF's are largely pyroclastic glass shards altered to analcite
Analcite cement locally fills pores around
remnant shards
20
May 7, 2001
1000.000
1.000
100.000
10.000
0.100
---
Tarn
0 Tam4
MWN
MWN2A
MWS
0.001
0 5 10 15 20 25 30
Porosity (%)
21 May f, LVVl
I i
- M It water North Type Log
o Between 4958' (T 4.1) and 5297' (T2) sstvd
- Geographic imits
@ò Sections 1-36 of T8N,
Ie - iel a
I a e
- Kuparuk River ield
- Meltwater il
Ie
""
22
May 7,2001
I
la
ilia
pose
I
les
23
May 7, 2001
eltwater Sim
(Injection
ube Simulation Results
id is Kuparuk I)
100
>
0..
N 95
-
-
@9:
~O
(DO 90
>~
O~
u
(D
r.t:
85 MMP= psia
80
2050
2100
2150
2200
2300
2350
2400
2450
Slim Tube Operating Pressure (psia)
24
May 7, 2001
50.00
45.00
40.00
35.00
~ 30.00
~
"w 00
o
o 20.00
0..
Porosity as a of Pe rmeabmty
(Tarn Analog for Confined Flow Turbidite Facies)
1 00
1 00
5.00
0.00
o
. .
y = 18. 714xo.067
50
100
Permeability (md)
150
200
25
May 7, 2001
Water Saturation as a nction of Porosity
(Tarn Analog for Confined Flow Turbidite Facies)
100.00
90.00 . ---
80.00
-
~ 70.00
0
-
60.00 .,
:::s 50.00 --.---.
... .
co .
(I) 40.00
II..
Q) 30.00
...
~
20.00
10.00 y = (4290)(x)[(-0.0167)(X)-1
0.00
0.00 5.00 10.00 1 00 20.00 25.00 30.00 35.00
Porosity (%)
26 May 7,2001
Stochastic Permeability Distribution
(Confined Flow Turbidite Facies)
27
.
May 7, 2001
Pattern ode I Results for Confined low urbidite Facies
Recovery A unction Of HCPVI
60
55
50
45
40
35
~
0
- 30
~
CD
> 25·
0
U
~ 20
15
10
5
0
0
28
-
...
---....
.. .11II
.. .
Á NNVAG w/Water Chase (20% HCPVI MI)
. Waterflood
MI Flood w/Lean Gas Chase (20% HCPVI MI)
Lean Gas Flood
0.2
0.4
0.6
0.8
1
1.2
1.4
Total CPVI
May 7, 2001
--
iI!i
I
I
iI!i
I
I
- Stochastic Models
ully Compositional
ithofacies Dependent
omogeneous odels
lack Oil
Pattern Configuration pe dent
- Res Its
MWAG Recovery Provides Incremental 90/0 001
29
May 7, 2001
Iii I
iI!i
I
Recovery Benefits (-9% OOIP)
- KRU Impact
Gas Storag Benefit
No Appreciable Adverse Recovery Impact
I Availability
Infrastructure
Miscibility
- Infrastructure "Opportuni
down
30
May 7, 2001
10
Iii
2001 D lUng
Continuous Drilling of -1 Wells
Phased Drilling on a Regional Basis
Test Cairn Accumulation rly in rogram
Develop "Sweet Spots" & Test riphery
2002 D lUng
D II -9 Wells
Probable rilling reak du ng
loration Season
31
May 7, 2001
I
III
10
MWAG
Maintain Reservoir ressure to nsure Tertiary
Recovery nefits lized
Minim Injectors until Well Interaction better
Understood
Pursue A ressive Initial MI Injection Schedule for
Overall G Rate Be efit
Optimize Cumulative MI Slug S by Pattern based on
Performance
Gas
Recover NGLs
32
May 7, 2001
Itwater roduction recast
30000
0 25000
OJ 20000 Gross Production
-
s::: less Backout
0
...... 15000
......,
(J
:::s
"'C 10000
0
!I...
Q.. 5000
.....
......
0
0
2000 2005 0 2015 2020 2025
Year
33
May 7, 2001
III III
I I
io ( i
I
- Cumulative Slug S
I nrichment
II Spacing
o
ntal/High Angle
- Pattern Co guratio
- Well Location Refinement
34
IIiI
I
lis
e
ase )
May 7, 2001
ell 155 es
Artificial
Natural low
M I/Gas Lift
et u p ift
Possibl ressu Reduction
Seco dary rgets
Thin, Marginal Cairn
luate ability
Annular Isolation
35
May 7, 2001
Shallow Zon Well Completion Issues
36
May 7,2001
11II
rvlew
II Tests
- Gas Sam les
ressure Measure nts
- Surveillance logs
37
May 7, 2001
I P
ill
001
- Spaci g Units (Rule 3)
- Injection Well Completion (Rule 5)
- Reservoir ressu onitori g (Rule 8)
- GO Exemption (Rule 9)
- Timi g of Injection Start-Up (Rule 10)
- Reservoir Su ilia ce Reporting (Rule 11)
38
I s
May 7, 2001
Spacing nits
- Minimum of 10 Acres
- No Closer than 300' from Ownership Change
39
May 7, 2001
Inj ctio
ell 0 pi io s
- Injectors with ~ 200' between Top Perforated Interval &
Annular Isolation
ptions to 200' Rul whe ursuing Seco dary
Targets withi the Meltwater Pool
40
May 7, 2001
iI!i
eservol
- In I Press
5
III
I
urvey on Eac Well
inimum Annual Number of ressure Surveys Equal to the
Number of Produci g or Injecting Gove mental Sections
withi e Pool
- Reservoir ressure
m of 5400' Subsea
- Pressure Surveys
Stabilized Static Measurements, Falloffs, Build ps,
Multi-Rate Tests, Drill Stem Tests or Open Hole Tests
- Res Its Reported Quarterly
- Res Its from "Special Tests" Reported Quarterly
41
May 7, 2001
xe
pt from roduci g GOR mits
42 May 7, 2001
Initiate
43
11II
10
-
in 6 onths of Prod
o
May 7, 2001
I
ill
ill
I
- Reservoir Management Update
- Produced & I luids by Interval
- Reservoir ressure alysis
- Multi nterval roduction & Injection Logs
- Well location &
II Test
luatio
uture Development lans
44
May 7,2001
45
Typical 3-1/2"
Monobore Completion
FMC Prudhoe Gen V
9u5lS x 5% x 3%
2.875" CAMCO
OS nipple for
Possible K-Valve
7-5/8" Surface Casing
at 2,500' TVD
Cameo 3%" x 1"
side pocket GLM
6%" Hole
Baker CMU Sliding
Sleeve w/2.813" OS
Cameo profile
CAMCO 2.75"
OS nipple
5Y," Casing
Seal Receptacle
(CSR)
Crossed over to
3Y," tubing
at 5,000' TVD
3Y," Production Casing
at 5,200' TVD
Base of
permarrost
at 1,250' MD
Base of
West Sak
at 1,800' TVD
Typical 4-112"
Monobore Completion
FMC Prudhoe Gen V
9-5/8" 7 " 4%
12'/," Hole
9-5/8" Surf. Csg.
at 2,500' TVD
8%" Hole
7" Casing
Seal Receptacle
(CSR)
Crossed over to
4Y," casing
at 5,000' TVD
May 7, 2001
asing nd C me ing ces
- Conductor Set at Least 75' Below Ground Level
- Surface Casing at Least 500' low rmafrost for
Annular u ping
46
May 7,2001
TREE CAP
SWAB VALVE
4Y1s"-SØøø# API
TEE 4Y1a"x3Ys"
SØØØ¡¡ API
SURFACE SAFETY v.
4- Y1s" - Søøø# API
MASTER SURF ACE v"
4 Y16" Søøø# API
TUSING HD ADAPTER
n"-søøø# API
CASING HEAD
11"-5ØØØ# API
LANDING RING
CONDUCTOR
(16"Ø)
TREE ASSEMBLY
47
May 7, 2001
uto atic Sh ui e t
- Fail Safe Automatic u ce Safety Valves on All Wells
- S rface Safety Valves Tested ry 6-Months
48
May 7, 2001
ydroge 5 de .. la
. 0 I ge cy
MC .065
ata at e .. ents
. I
AAC 25.0 1 (a), (b )(1), and ( )(2)
49
May 7, 2001
- ravel oad a
ad (1
iles )*
ges
ctio
I
..
I e
"
-
"
ate I ectio
iscible I ectant
-8"
..
Ene
- ve e
owe i e
-1
liS
50
May 7, 2001
51
May 7, 2001
6 Miles
to DS 2M
@
tk~ ~O
1J $
1 «) Miles DS 2M to DS 2N
(0
..-
"Tarn OS's"
$) Miles DS 2N to DS 2P
52
;:
"Ñ
. -
*
$
.
l2f)T® .
~øø @)
"Meltwater"
"4-Corners"
Intersection
New Tarn Pipelines"
New Meltwater Pipelines
May 7, 2001
-Tru k a d Late I Well Manifolding
- Production
- Test
- Water Injection
- Miscible Injectant
-20' Wellhead Spacing
-Conventional Well Test Separator
-Remote Well Test Actuatio
-Remote Control II Cokes
- D Skid
- lectrical/Control Room
53
May 7,2001
54
".~'<II~"-'''I>
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? Alaska Anvil Inc.
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May 7, 2001
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lr ;.!EM l. r AlllJrl ~MU'SS
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Meltwater Pool Rules Hearing
S2P ~ad ty.ayout
- - - - - - -
! . ~ J : ;1 ~I !I !I !I ;1 !I 'I ~ .
. . ~
j~
Meltwater Pool Rules Hearing
· Conventional Vessel
. · Gas/Liquid Separation Only
· Metering Devices
- Total Liquid - Micro Motion Mass Flow Meter
- Liquid Water Cut - Phase Dynamics Meter
- Gas - Vortex Shedding Meters
.
55
May 7,2001
.
.
Meltwater Pool Rules Hearing
~
~
Common Production Facilities and Suñace Commingling
- Surface Commingling of Meltwater and Other Greater Kuparuk
Area Production
- Floating Allocation Allocation Factor Scheme for KPA and GKA
Satellites (Pending Agency Approval)
- Two Well Tests per Month
- Monthly Reports of Allocation and Test Data
56
May 7, 2001
Meltwater Pool Rules Hearing
~ (, ¡¡
dl
l :L~ ã (11
'~' ~ ,,?
.:~..' ;1
a
Cii'i>,,^f:i ':h':· ~'(\;,~J ;¡',::r 4¡i;o". ?'f~,,~J\i¡, ''''/"';.'' ,;1'I!'(1!\' "lit!
:;~,j"-j',': ':-;:.H,~;,.. ",;, ·:It YI".f)! ~~'I' ~~ r;qj~", a
" " "j, "~I ',1 >," ,", ", "'. '-'.;;:)
~,:';~;4 \'¥ ~,! !'¡: I\i;';~,:r. ~"¡'i,w $:¡;@'
KPA + All GKA Satellites Have Variable Alloc. Factors
. If Overall Alloc. Factor is Less than 1.02
· KPA and All Satellites Have Same Alloc. Factor
If Overall Alloc. Factor is 1.02 or Greater
· Alloc. Factor for All Satellites Set to 1.02
· All Residual Production is Allocated to KPA
.
*Change to Previous Allocation Factor of 1.0 for GKA Satellites
57
May 7, 2001
Meltwater Pool Rules Hearing
-
Rule 12 - Production Anomalies (Proration Events)
. - Attempt to Cut All Pools by Equal Percentage
- May Vary to Avoid Equipment Damage and/or
Increased Operating Costs
Rule 13 - Administrative Action
- Commission May Administratively Amend Pool Rules
.
58
May 7, 2001
Meltwater Pool Rules Hearing
I
- - -
Rule 1 Field and Poo Name
Rule 2 Pool Definition
Rule 3 Spacing Units
Rule 4 Casing and Cementing Practices
Rule 5 Injection Well Completion
Rule 6 Automatic Shut-In Equipment
Rule 7 Common Production Facilities and Surface Commingling
RuleS Reservoir Pressure Monitoring
Rule 9 GOR Exemption
Rule 10 Pressure Maintenance Project
Rule 11 Reservoir Surveillance Report (Annual)
Rule 12 Production Anomalies
Rule 13 Administrative Action
59 May 7, 2001
.
.
.
.
8
œ.
$-
r\;;,
Meltwater Area Injection Order Hearing
May 7, 2001
.
.
Meltwater Area Injection Order Hearing
Application Requirem nts
20 AAC 25.402{c)
15 Requirements
4 Covered During Pool Hearings
11 Covered with Additional Testimony
2
May 7, 2001
.
.
Meltwater Area Injection Order Hearing
Pool Rule Hearing Reference
Area Injection Order
Proposed Operation
Depth & Name of Affected Pool
Casing & Testing Methods for Injectors
Incremental Increase in Ultimate Recovery
3
May 7, 2001
Meltwater Area Injection Order Hearing
Discussi n pies
Area Injection Order
- Existing Penetrations within One-Quarter Mile
. - Operators & Surface Owners within One-Quarter Mile
- Affidavit of Notification
- Type Well Log (Injection Wells)
- Formation Proffered for Injection & Confining Zones
- Water Analysis
- Applicable Freshwater Exemption
. - Injection Fluid Data
- Estimated Pressures
- Evidence of Injection Confinement
4 - Mechanical Condition of Wells Penetrating Injection Zone
May 7, 2001
PHilliPS Alaska, Inc.
A Subsidie¡y of PHilLIPS PETROLEUM COMPANY
Proposed Meltwater
Injection Area
V IV.:IVIV,+I.JVI
5
May 7, 2001
.
.
Meltwater Area Injection Order Hearing
Notificati n
20 AAC 25.402 (c)(2)
Qperators and Suñace Owners within One Quarter Mile of Injection
Qperations
Operator:
Phillips Alaska, Inc.
Attention: Dan Kruse ATO-1220
P.O. Box 100360
Anchorage, AK 99510-0360
Surface Owner:
State of Alaska
Department of Natural Resources
Attention: Mike Kotowski
P.O. Box 107034
Anchorage, AK 99510
6
May 7, 2001
50
7
4958'sstvd
5187' sstvd
5297' sstV(
May 7,2001
I
RESISTIVITY
LWD.GRC 2
GAÞ!
c
~G;
øæ
ø
8
..J
~
W
...
æ
May 7, 2001
I
II
GAM M A RA Y
9
/~
\!
ill.)
-¡
J::
(J)
en
(J)
-
ill.)
I:
o
N
-
ill.)
I:
o
N
Well Log
4/98
May 7, 2001
Meltwater Area Injection Order Hearing
Formation Water Analyses
-No Water zones encountered at Meltwater by exploration
. wells
-Connate water obtained from core plugs using miscible
extraction process
-Chlorides measured by Ion Chromatography
. - Chloride content 20-40 Kppm TDS
-Range due to chlorides diffused by drilling mud filtrates
-Currently gathering a core with tracer data to pin down
water composition
10
May 7, 2001
AlpineAquifer
Exemption
Alpine Pool
Sections
11
N2
Proposed
Meltwater Pool
May 7, 2001
,
,
Meltwater Area Injection Order Hearing
Iculated Sh lIow S n alinity
Kalubik #1
Rmf= 1.19 Q-m 69°
Permafrost 1510'
Sand @ 1740'-90'
<I> = 36 Rt = 12 Qm
Rwa = 1.09 Qm
(5.3 Kppm)
SP = -35 mv (@ 35°)
RwSP = 0.38 Qm
(15 Kppm)
Hole badly washed
out. SP probably
more representative.
12
Colville River St 1
Rmf = 2.52 Q-m 68°
Permafrost 1360'
Sand @ 1510'-20'
<I> = 36 Rt = 2.1 Qm
Rwa = 0.24 Qm
(28 Kppm)
SP = -40 mv (@ 34°)
RwSP = 0.5 Qm
(20 Kp m)
Zone slightly shaly.
Salinities quite high.
Cirque 2
Rmf = 2.28 Q-m 85°
Permafrost 1170'
Sand @ 1440'-60'
<I> = 34 Rt = 26 Qm
Rwa = 2.1 Qm
(2.5 Kppm)
SP = -20 mv (@ 35°)
RwSP = 1.03 Qm
(5.4 Kppm)
Hydrates known .SP
more representative
though still too low.
2N-349
Rmf= 3.3 Q-m 63°
Permafrost @ 1310'
Sand @ 1905'-15'
<I> = 31 Rt = 10 Qm
Rwa = 0.8 Qm
(6.9 Kppm)
SP = -20 mv (@ 44°)
RwSP = 1.19 Qm
(4.5 K pm)
Hydrates below
Permafrost R wa
more representative.
May 7, 2001
:2
13
H
)
o
May 7, 2001
Cchn: V5 B-1
C02
C1
o
500
1000
:É
£ 1500
"
'"
o
2000
2500
3000
88888 °88
;2~¡¡¡Rð5 §8
~
uUL
uUL
14
G2
C3
iG4
oC5
iC5!nC5
IC5
C6
C1!C2+C3 IG4/nG4
oC4
nOOCS
o § § O.,..(\j(lt)VOd~"!
~ <-I
May 7,2001
Gas
Hydrates
1800
1600
1400
1200
1
U) 800
<t
C)
600
400
15
..305
D
and GAS SHOWS
110.0
o
o
100.0
500
1000 1500 2000 2500 3000 3500
ft)
~
C')
CD
"C
-
Q.
:::;)
:ä
May 7, 2001
,
,
Meltwater Area Injection Order Hearing
Aquife Exemption Summary
-No apparent fresh water zones in
Meltwater area suitable for human
consumption
-Applying for an Aquifer Exemption
for the Meltwater Pool
16
May 7,2001
,
,
Meltwater Area Injection Order Hearing
Injection Fluid Data
Injection Water Composition
Component
Concentration
Í!!!9ill
159
12
1,920
<0.15
20
35
18
137
13,131
<0.06
<10
12.6
0.74
1.2
<0.003
99
<0.5
60
20
8,800
6.7 May 7, 2001
17
Su Ifate
Sulfide
Bicarbonate
Aluminum
Ammonia
Barium
Boron
Calcium
Chloride
Chromium
Fluoride
Iodide
Iron
Lithium
Manganese
Magnesium
Phosphorus
Potassium
Silicon
Sodium
Strontium
Meltwater Area Injection Order Hearing -
Inj ction luid D
Lean Gas and MI Compositions
Component Lean Gas MI
, .(Mole % \ Mole %\
CO2 0.89 0.5
N2 0.27 0.3
C1 81.37 69.6
C2 8.79 6.7
C3 5.10 5.0
i-C4 0.92 2.2
n-C4 1.99 6.3
, i-C5 0.30 2.0
n-C5 0.28 2.5
C6 0.07 2.1
C7 0.01 1.8
C8+ 0.00 1.0
18
May 7, 2001
Meltwater Area Injection Order Hearing
Pre SlJre, Inj Confinement ondition of II
- Estimated Pressures
, Water Injection: 1600 - 2600 psi
MI/Gas Injection: 2600 - 3600 psi
- Evidence of Injection Confinement (wlWorst Case Modeling)
Mllnjection: No Appreciable Growth
Water Injection: Upward Growth of -10'
, Propped Fracture Height: Upward Growth of -200'
- Mechanical Condition of Wells Penetrating Injection Zone
P&A (20 AAC 25.112)
Casing Strings Cut 3' Below Ground (20 AAC 25.120)
19
May?,2001
#4
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(. ... kA .. . ...) "We Talk Safety First""
. to.. . ._n'_ prt¿¡~e.t~ð?~£t? nee
PhiUip'ii AIWika, I'nç, ß"¡~,':\k;:j '!\~1:role\.!l·n ('ontr':l\:I.~jr~;. lnt'. Almìku ,.t\nvi! 11\;;,
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FAX
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t~·ì ~ i .: EI V'Cl,
11 ' j I
Greater Kuparuk Area Projects MAR 2 2 2001
Phillips Alaska, Inc. . ... Con ,,_~
P.O. Box 100360 AIIIk8()1&Ga8 S.\NIJI....uI.
Andøage
Anchorage, AK 99510..0360
Facsimile · (90!> 263-4.035
Confirmation ·
Date:
.~ . -.'., ,- : .. -,- ".11.-'" ...._\... ~. ..
J:c"'ax:
. ." ··..·..1..· .."... ":;,.NT-·
_.- .. ... - ...- .-_. . -.
.To: .~.""fll
Company: AOnC(.-
~om: ~~~~ ~~-~
Phone:
Panes (includine cover) ~+ \
C.c: ,..-.
Sub.iect;
I I
o Urgent D For Review
D Please R~ply D Please copy & Distribute Locally
COMMENTS:
11t, liI/I.t ~ ~tA
14y,!"..¡f. . '.lH.
~ . _ t.,,, t,,-~
. ..J..r"~ 4)1aØW'i_~ hIVItM..",. h'l
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'í?1I1J1\_,-·_u .
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RECEIV'ED
MAR 2 2 2001
Alaska Oi' & Gas r.JVI~ \l\fttmHtðß
Anch -""'''W' JrJ
. orage .
1'1. No.. lease No. Exp. Date Legol D"crlp.1on [eœe A/:;œ$
. 142
roaN, R07E. UM Sec.
4: AJt Sec. 5: .AJl: Sec.
.AJJ1313H2 . I1lðOiYa 6: Aft Sec. ï: Aft Sec.
',8: All; See. 9: All: Sec.
16: All; Sec. 17: An;
Sec. '8: AIL
1.4.3 .4CL373111
roaN, R07E, :JM: Sec.
1 : At Sec. 2: Aft Sec.
n i3Cm 3: All; Sec. 1:J: All: Sec.
. ,11: All; Sec. 12: All;
Sec. 13: All; Sec. 14:
All; Sec. 15: All.
TeD '. ,ACl~aroæ
maN, R07E. UM: Sec.
t 9: All; Sec. 2G: AIt
: Sec. 21: AU: Sec. 28:
. C,/:! ','05 ; All; Sec. 29: All: Sec.
30: All; Sec. 31: All;
Sec. 32: Aft, Sec. 33:
,All.
. TBD : AJ:\.'IftOOfn
T08N, R07E. UM; Sec.
22: Ail; Sec. 23: AU:
Sec. 24: All; Sec. 25:
10131.'t)5 AJI; Sec. 26: Alt Sec.
27: All: Sec. 34: All;
Sec. 35: Aft Sec. 36:
All.
T*
._~, . - -
lease Jnfonnation for Meltwater Pool Rules and Areà Injedlon Order
5.[)!33
5.760
~607
5.760
11..343
LMIof
RoyafIV
12 rot.
, 2.5O'I.
12.5Iß;
12.~
Alaskø Net
ProftSftcr.
C.O'"
0,(1%
0.0%
0.0$
1.11'1I1
: r~ FA?
Yes
'r'ê$ 1\-0
ExporsJcn _ PQrtbl
. Exp::lI"ISion No
¡\Qleed WQ~ InlefèStl
Philips AJaska
BPX UNOCAL
Total
MOBil
CHEVRON
."
"2
1
.3
5!;.29Jl43
39.252256%
4.';00600% O.364ðO:»i.; O.l0ò60Q"J>
..
!
100.('(XX)(P;!l.
f'artia
.. --..
::-: - - -.!:-- :::' . _ :~;:;·i;: - . :"!:=:::f-:- _':'_':, "." 0'" ~~ ~-. - . < : ~:: ::= - ~.~ ~-: -: : - .: .~- ?:;.: .. .
f',,~j;~a~r:~f'fî!; >v,~·¡;,·~~'-Q~':.:~I~ "
. .
100.oonm '
. . 1
~
..c
ª :
.:9
\!?;;~r:·1~fE~~r.~~~;;~~~w;,:;~:,~~:
55.293744%
3'?.:282256% 4.9.::¡œoc,% G.Jé400:ni a.106lf.C'ì6 IOO.1XKX'm(,
~
:!
.§ '< ¡
~';~¡r;';~~"f{~;')~~~i';~R!t'6~,]J;Pf!
5S.-S07C24%
a9 ..43311tJ%
0..1 (J86OC)%.
K'G.IX~
4.950600%
o.o:o:oo~
'0
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D.DCJ.'IX.Q'%
O. 108iíJ{J'J.,
100.'.Xr~
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']9A~3776~
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INV. MUST BE IN TRIPLICATE SHOWING ADVERTISING ORDE~.. CERTIFIED
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ADVERTISEMENT MUST BE SUBMITrED WITH INVOICE
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R 333 W 7th Ave, Ste100
o Anchorage,AK 99501
STATE OF ALASKA
ADVERTISING
ORDER
M
~ Anchorage Daily News
POBox 149001
Anchorage, AK 99514
Type of Advertisement ~ Legal
REF TYPE
1 VEN
2 ARD
3
4
FIN AMOUNT
1
2
3
NUMBER
02910
Sy
01
4
RE~I°è!;PO}vfÁ
02-902 (Rev. 3/94)
ADVERT1SING ORDER NO.
AO-02114014
AGENCY CONTACT
DATE OF A.O.
Jody Colombie
PHONE
April 4, 2001
PCN
(907) 793 -1221
DATES ADVERTISEMENT REQUIRED:
April 5, 2001
THE MATERIAL BETWEEN THE DOUBLE LINES. MUST BE PRINTED IN ITS
ENTIRETY ON THE DATES SHOWN.
SPECIAL INSTRUCTIONS:
D Display
D Classified
DOther (Specify)~
SEE ATTACHED PUBLIC HEARING NOTICE
AOGCC, 333 W. 7th Ave., Suite 100
~chora~e,AJ(99501
AMOUNT DATE
CC
PGM
LC
TOTAL OF
PAGE 1 OF ALL PAGES$
. 2 PAGES
COMMENTS
ACCT
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NMR
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DIST un
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DIYISION APPROVAL:
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Publisher/Original Copies: Department Fiscal, Department, Receiving
AO.FRM
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AMENDED
Notice of Public Hearing
STATE OF ALASKA
Alaska Oil and Gas Conservation Commission
Re: Meltwater Oil Pool, KuparukRiver Field - Pool Rules and Area Injection Order
PHILLIPS Alaska, Inc. (PAl) by letter dated March 12, 2001, has applied for an
area injection order and pool rules under 20 AAC 25.460 and 20 AAC 25.520,
respectively, for development of the Meltwater Oil Pool, Kuparuk River Field, on the
North Slope of Alaska.
The Commission has set a public hearing on the Applications for the Area
Injection Order and Pool Rules on May 7, 2001 at 9:00 am at the Alaska Oil and Gas
Conservation Commission, 333 West ihA venue, Suite 100, Anchorage, Alaska 99501.
In addition, a person may submit a written protest or comments on· the applications prior
to May 7,2001 at 9:00 am
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 Jody Colombie at 793-1221
before May 1, 2001.
~~~
Camillé Oechsli Taylor
Commissioner
Published April 5,2001
ADN AO# 02114014
~) ~ )
Anchorage Daily News
Affidavit of Publication
1001 Northway Drive, Anchorage, AK 99508
PRICE OTHER OTHER GRAND
AD# DATE PO ACCOUNT PER DAY CHARGES CHARGES #2 TOTAL
822766 04/05/2001 02114014 STOF0330 $76.11 $0.00 $0.00 $76.11
$0.00 $0.00 $0.00
$76.11 $0.00 $0.00 $76.11
STATE OF ALASKA
THIRD JUDICIAL DISTRICT
Eva Alexie, being first duly sworn on oath deposes and says that she
is an advertising representative of the Anchorage Daily News, a
daily newspaper.
That said newspaper has been approved by the Third Judicial
Court, Anchorage, Alaska, and it now and has been published in
the English language continually as a daily newspaper in
Anchorage, Alaska, and it is now and dUrIng all saia time was
printed in an office maintained at the aforesaid :place of
publication of said newspaper. That the annexed is a copy of an
advertisement as it was published in regular issues (and not in
supplemental form) of said newspaper on the above dates and
that such newspaper was regularly distributed to its subscribers
during all of saId period. That the full amount of the fee charged
for the fore~oing publication is not in excess of the rate charged
private indIviduals.
'.,..A.·.·.;. M~~D~[) ,,"
~otic:e()f.·..i.
P.Ub.I.i.~·..I'I.e~ri.n,,!
STATE .OF AL.ASKA
Alaska Oil and Gas "
Conservation
;cómm ¡~~i~~"
1;·~~~~tlk~~!ì~:$Wi~.~g:I:\
. re~~:o~'t::~Je~nd Area In-I
I I
; PHILLIPS 'Alasko. Inc. '
'<PAl) bY letter dated I
I March 12,2001, has. ap- I
'plied for an area ¡niec-
'tion order and pool rules!
~~dÃ:~~0~~5~l,5'r~~paenc~ ¡
: tively, for development of !
I the Meltwoter Oil Pool, :
~~~a~u~ ~i~e~ r~~~' ~~ l
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f h~'C.)n'1rni..s;¿ rit;CI ~ \i~ti
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mlE'c'ic.n OrClE'r ana POOl
, FC\.I..':I (In Ma~ 7 200 I al !
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I
Signed ~ ~
Subscribed and sworn to me before this date:
tl¡ml_-4/l.ðôl
Notary Public in and for the State of Alaska.
Third Division. Anchorage, Alaska
MY COMMISSION EXPIRES: & R; ;kJ~ I-
t ~I:.
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and 'Ga¿C on se rvolion
Commission, 333 West 7th
I Avenue, Suite 100, An-
'I charage, Alaska 99S01. In
I additian, a person mÇlY
'I submit a written protest
or camments on the ap-
, pllcatlons prlar to May 7,
2001 at 9:00 am.
I .. Ifyou,are,aperson,with
a:diso,bl.llty who may
I ,~~~d.r~~~:i~~~Tg~I~~~t
. or to attend the public'
I 'he,arin9, please contact
JoðyColombie at 793~1221 :
befor,e M~y 1, 200~. '
Is/Camille' Oechsll Taylar
Commissloher ,'",
Pub;;' Å:ril'S, 20Q1
AO# 02114014
AO.FRM
PUBLISHER
02-901 (Rev. 3/94)
Page 2
Notary public for state of
My commission expires
19_,
day of
This
Subscribed and sworn to before me
excess of the rate charged private individuals.
, 1 9 I and that the rate charged thereon is not in
day of _
consecutive days, the last publication appearing on the
1 9_, and thereafter for
day of
the annexed is a true copy, was published in said publication on the_
and that the advertisement, of which
_and state of
in said division
Published at
of
says that he/she· is the
who, being first duly sworn, according to law,
INVOICE MUST BE IN TRIPLICATE AND MUST REFERENCE
THE ADVERTISING ORDER NUMBER.
A CERTIFIED COPY OF THIS AFFIDAVIT OF PUBLICATION
MUST BE SUBMITTED WITH THE INVOICE.
ATTACH PROOF OF PUBLICATION HERE.
Before me, the undersigned, a notary public this day personally appeared_
division.
ss
State of
AFFIDAVIT OF PUBLICATION
REMINDER
United states of America
SPECIAL INSTRUCTIONS:
THE MATERIAL BETWEEN THE DOUBLE LINES MUST BE PRINTED IN ITS
ENTIRETY ON THE DATES SHOWN.
DATE OF A.O.
AGENCY CONTACT
Jody Colombie
PHONE
(907) 793 -1221
DATES ADVERTISEMENT REQUIRED:
April 5, 2001
~ Anchorage, Daily News
POBox 149001
Anchorage, AK 99514
April 4. 2001
PCN
AOGCC
R 3001 Porcupine Drive
o Anchorage, AK 99501
M
F
.) NOTICE TO PUBLISHER I ) ADVERTISING ORDER NO.
II. MUST BE IN TRJPLlCATE SHOWING ADVERTISING ORDE~.. ŒRTlFIED 0
AFFIDAVIT OF PUBLICATION (PART2 OF THIS FORM) WITH ATTACHED COpy OF AO- 2114014
ADVERTISEMENT MUST BE SUBMITTED WITH INVOICE
STATE OF ALASKA
ADVERTISING
ORDER
, . seE B9TI<?~ :F~~ 1NV~,C~ 'ADDRESS:,
Page 1
ACE PETROLEUM COMPANY
AK JOURNAL OF COMMERCE OIL & INDUSTRY NEWS
ALASKA DEPT OF LAW
ALASKA OFC OF THE GOVERNOR
ALASKA OIL & GAS ASSOC
AL YESKA PIPELINE SERV CO
AL YESKA PIPELINE SERV CO LEGAL DEPT
AL YESKA PIPELINE SERV CO
AL YESKA PIPELINE SERVICE CO VALDEZ CORP AFFAIRS
AMERICA/CANADIAN STRATIGRPH CO
4/4/01
()
AddrConsOrd
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~)
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4/4/01
GEORGE G VAUGHT JR
SENATOR LOREN LEMAN
JOHN MILLER
RICHARD FINEBERG
FRED PRATT
RAY TYSON
C BURGLlN
RICK WAGNER
DIANE SUCHOMEL
JOHN A LEVORSEN
POBOX 13557
STATE CAPITOL RM 113
3445 FORDHAM DR
POBOX 416
POBOX 72981
2016 MAIN #1415
POBOX131
POBOX 60868
105070 W MAPLEWOOD DR
200 N 3RD ST #1202
PENNY V ADLA POBOX 467
JERRY HODGDEN GEOL 40818TH ST
DUSTY RHODES 229 WHITNEY RD
RON DOLCHOK POBOX 83
R E MCMILLEN CONSULT GEOL 202 E 16TH ST
DAVID CUSATO 600 W 76THAV #508
WATTY STRICKLAND 2803 SANCTUARY CV
L G POST O&G LAND MGMT CON 10510 Constitution Circle
ANTONIO MADRID POBOX 94625
H L WANGENHEIM 5430 SAWMILL RD SP 11
BAPI RAJU 335 PINYON LN
ROBERT G GRAVELY 7681 S KIT CARSON DR
JAMES GIBBS POBOX 1597
ALFRED JAMES III 107 N MARKET STE 1000
DAVID W. JOHNSTON 320 MARINER DR.
JAMES E EASON 8611 LEEPER CIRCLE
ARMAND SPIELMAN 651 HILANDER CIRCLE
NANCY LORD PO BOX 558
THOMAS R MARSHALL JR 1569 BIRCHWOOD ST
NICK STEPOVICH 543 2ND AVE
GORDON J. SEVERSON 3201 WESTMAR CIR
JAMES RODERICK PO BOX 770471
MARK ALEXANDER 7502 ALCOMITA
ARLEN EHM GEOL CONSL TNT 2420 FOXHALL DR
JACK 0 HAKKILA POBOX 190083
GERALD GANOPOLE CONSULT 2536 ARLINGTON
ANDREW C CLIFFORD PO BOX 79593
ROSE RAGSDALE 4220 B Street Ste #210
ROBERT E MINTZ ASST ATTY G 1031 W 4TH AV STE 200
JOHN KATZ STE 518 444 N CAPITOL NW
JUDY BRADY 121 W FIREWEED LN STE 207
PERRY A MARKLEY 1835 S BRAGAW - MS 575
1835 S BRAGAW
1835 S BRAGAW - MS 530B
POBOX 300 MS/701
4800 KUPREANOF
CHUCK O'DONNELL
SANDY MCCLINTOCK
RON BROCKWAY
Page 2
DENVER
JUNEAU
ANCHORAGE
ESTER
FAIRBANKS
HOUSTON
FAIRBANKS
FAIRBANKS
LITTLETON
BOISE
CO
AK
AK
AK
AK
TX
AK
AK
CO
10
NINILCHIK AK
GOLDEN CO
ANCHORAGE AK
KENAI AK
OWASSO OK
ANCHORAGE AK
KATY TX
EAGLE RIVER AK
PASADENA CA
PARADISE CA
,COPPELL TX
LITTLETON CO
SOLDOTNA AK
WICHITA KS
ANCHORAGE AK
ANCHORAGE AK
ANCHORAGE AK
HOMER AK
ANCHORAGE AK
FAIRBANKS AK
ANCHORAGE AK
EAGLE RIVER AK
HOUSTON ' TX
ANCHORAGE AK
ANCHORAGE AK
ANCHORAGE AK
HOUSTON TX
ANCHORAGE AK
ANCHORAGE AK
WASHINGTON DC
ANCHORAGE AK
ANCHORAGE AK
ANCHORAGE AK
ANCHORAGE AK
VALDEZ AK
ANCHORAGE AK
6,)
AddrConsOrd
()
4/4/01
AMOCO CORP 2002A
AMSINALLEE CO INC
ANADARKO
ANADRILL-SCHLUMBERGER
ANCHORAGE DAILY NEWS
ANCHORAGE TIMES
ARENT FOX KINTNER PLOTKIN KAHN
ASRC
ASRC
BABCOCK & BROWN ENERGY, INC.
BABSON & SHEPPARD
BAKER OIL TOOLS
BELOWICH
BONNER & MOORE
BP EXPLORATION (ALASKA) INC
BP EXPLORATION (ALASKA) INC
BP EXPLORATION (ALASKA) INC
BP EXPLORATION (ALASKA) INC
BP EXPLORATION (ALASKA), INC.
BRISTOL ENVIR SERVICES
C & R INDUSTRIES, INC.,
CHEVRON
CHEVRON CHEM CO
CHEVRON USA INC.
CIRI
COOK INLET KEEPER
CROSS TIMBERS OIL COMPANY
CROSS TIMBERS OPERATIONS
D A PLATT & ASSOC
DEGOL YER & MACNAUGHTON
DEPT OF ENVIRON CONSERV SPAR
DEPT OF NATURAL RESOURCES
DEPT OF NATURAL RESOURCES
DEPT OF NATURAL RESOURCES
DEPT OF NATURAL RESOURCES
DEPT OF NATURAL RESOURCES
DEPT OF NATURAL RESOURCES
DEPT OF NATURAL RESOURCES
DEPT OF NATURAL RESOURCES
DEPT OF REVENUE
DEPT OF REVENUE
DEPT OF REVENUE
DEPT OF REVENUE
DEPT OF REVENUE
DNR
DOCUMENT SERVICE CO
DPC
LIBRARY/INFO CTR
EDITORIAL PG EDTR
LIBRARY
JULIE WEBER
ALASKA AREA MGR
LIBRARY H20
INFO RESOURCE CTR MB 3-2
LIBRARY & INFO CTR
ALASKA DIVISION
LAND DEPT
MIDCONTINENT DIVISION
DIV OF OIL & GAS
DIV OF OIL & GAS
PUBLIC INFORMATION CTR
DIV OF OIL & GAS
DIV OIL & GAS
DIV OF OIL & GAS
DIV OF LAND
DGGS
OIL & GAS AUDIT
OIL & GAS AUDIT
DIV OF OIL & GAS
Page 4
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AddrConsOrd
()
4/4/01
WILLIAM 0 VALLEE PRES
MARK HANLEY
MICHAEL CAREY
BERT TARRANT
WASHINGTON SQ BLDG
CONRAD BAGNE
BILL THOMAS
600 17TH STREET
JOHN F BERGQUIST
MICHAEL A BELOWICH
SUE MILLER
MR. DAVIS, ESQ
PETE ZSELECZKY LAND MGR
MARK BERLINGER MB 8-1
JIM MUNTER
KURT SALTSGAVER
PAUL WALKER
ATTN: CORRY WOOLlNGTON
BOB SHAVELSON
MARY JONES
SUSAN LILLY
ONE ENERGY SQ, STE 400
CHRIS PACE
JIM STOUFFER
TIM RYHERD
JULIE HOULE
WILLIAM VAN DYKE
BRUCE WEBB
REG MGR NORTHERN REGION
JOHN REEDER
DAN DICKINSON, DIRECTOR
CHUCK LOGSTON
DENISE HAWES
FRANK PARR
BEVERLY MARQUART
JAMES B HAYNES NATURAL RE
JOHN PARKER
DANIEL DONKEL
POBOX 87703 CHICAGO IL
PO BOX 243086 ANCHORAGE AK
3201 C STREET STE 603 ANCHORAGE AK
3940 ARCTIC BLVD #300 ANCHORAGE AK
POBOX 149001 ANCHORAGE AK
POBOX 100040 ANCHORAGE AK
1050 CONNECTICUT AV NW WASHINGTON DC
301 ARCTIC SLOPE AV STE 300 ANCHORAGE AK
POBOX 129 BARROW AK
STE. 2630 SOUTH TOWER DENVER CO
POBOX 8279 VIKING STN LONG BEACH CA
4710 BUS PK BLVD STE 36 ANCHORAGE AK
1125 SNOW HILL AVE WASILLA AK
2727 ALLEN PKWY STE 1200 HOUSTON TX
POBOX 196612 MIS LR2-3 ANCHORAGE AK
POBOX 196612 MB 13-5 ANCHORAGE AK
POBOX 196612 ANCHORAGE AK
POBOX 196612 ANCHORAGE AK
PO BOX 196612 ANCHORAGE AK
2000 W. INT'L AIRPORT RD #C-1 ANCHORAGE AK
7500 W MISSISSIPPI AVE STE C4 LAKEWOOD CO
1301 MCKINNEY RM 1750 HOUSTON TX
POBOX 2100 HOUSTON TX
POBOX 1635 HOUSTON TX
POBOX 93330 ANCHORAGE AK
POBOX~~ HOMER AK
810 HOUSTON ST STE 2000 FORT WORTH TX
210 PARK AVE STE 2350 OKLAHOMA CITY OK
9852 LITTLE DIOMEDE CIR EAGLE RIVER AK
4925 GREENVILLE AVE DALLAS TX
410 WILLOUGHBY AV STE 105 JUNEAU AK
550 W 7TH AVE, SUITE 800 ANCHORAGE AK
550 W 7th AVE STE 800 ANCHORAGE AK
550 W 7TH AVE, SUITE 800 ANCHORAGE AK
550 W 7TH AVE, SUITE 800 ANCHORAGE AK
550 W 7TH AVE, SUITE 800 ANCHORAGE AK
550 W 7TH AVE, SUITE 800 ANCHORAGE AK
3700 AIRPORT WAY FAIRBANKS AK
POBOX 772805 EAGLE RIVER AK
550 W 7TH AVE, SUITE 500 ANCHORAGE AK
550 W 7TH AVE, SUITE 500 ANCHORAGE AK
550 W 7TH AV STE 570 ANCHORAGE AK
550 W 7TH AVE STE 570 ANCHORAGE AK
550 W 7TH AV STE 570 ANCHORAGE AK
550 W 7TH AVE, SUITE 800 ANCHORAGE AK
POBOX 1468 KENAI AK
1420 NORTH ATLANTIC AVE, ST DAYTON BEACH FL
Page 5
&.,)
AddrConsOrd
()
4/4/01
ECONOMIC INSIGHT INC
ENERGY GRAPHICS
ENSTAR NATURAL GAS CO
EXXON EXPLOR CO
EXXON EXPLORATION CO.
EXXONMOBIL PRODUCTION COMPANY
EXXONMOBIL PRODUCTION COMPANY
EXXONMOBIL PRODUCTION COMPANY
FAIRBANKS DAILY NEWS-MINER
FAIRWEATHER E&P SERV INC
FINK ENVIRONMENTAL CONSULTING, I
FORCENERGY INC.
GAFFNEY, CLINE & ASSOC., INC.
GAFO
GUESS & RUDD
H J GRUY
HALLIBURTON ENERGY SERV
HDR ALASKA INC
ILLINOIS STATE GEOL SURV
INTL OIL SCOUTS
IOGCC
JWL ENGINEERING
K&K RECYCL INC
KENAI NATL WILDLIFE REFUGE
KENAI PENINSULA BOROUGH
LA PUBLIC LIBRARY
LIBRARY OF CONGRESS
LINDA HALL LIBRARY
MARATHON
MARATHON OIL CO
MARATHON OIL CO
MARATHON OIL CO
MARPLES BUSINESS NEWSLETTER
MUNGER OIL INFOR SERV INC
MURPHY E&P CO
N-I TUBULARS INC
NORTHERN CONSULTING GROUP
NRG ASSOC
NY PUBLIC LIBRARY DIV E
OIL & GAS JOURNAL
OIL & GAS JOURNAL
OPSTAD & ASSOC
ORO NEGRO, INC.
PACE
PENNZOIL E&P
PETRINFO
PETRAL CONSULTING CO
LAND/REGULATORY AFFAIRS RM 301
LIBRARY
GREENPEACE
LIBRARY
REFUGE MGR
ECONOMIC DEVEL DISTR
SERIALS DIV
STATE DOCUMENT SECTION
SERIALS DEPT
OPERATIONS SUPT
GRAND CENTRAL STATION
Page 7
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AddrConsOrd
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4/4/01
POBOX 683
1600 SMITH ST, STE 4900
POBOX 190288
POBOX 4778
POBOX 4778
POBOX 2180
POBOX 2180
PO BOX 196601
POBOX 70710
715 I ST #4
6359 COLGATE DR.
310 K STREET STE 700
16775 ADDISON RD, STE 400
125 CHRISTENSEN DR. #2
510 L ST, STE 700
1200 SMITH STREET STE 3040
6900 ARCTIC BLVD
2525 C ST STE 305
615 E PEABODY DR
POBOX 338
POBOX 53127
9921 MAIN TREE DR.
POBOX 58055
POBOX 2139
POBOX 3029
630 W 5TH ST
10 FIRST ST SE
5109 CHERRY ST
POBOX 3128, Ste 3915
POBOX 196168
BRAD PENN POBOX 196168
GEORGE ROTHSCHILD JR RM 25 POBOX 4813
MICHAEL J PARKS 117 W MERCER ST STE 200
POBOX 45738
POBOX 61780
3301 C Street Ste 209
2454 TELEQUANA DR.
POBOX 1655
POBOX 2221
1700 W LOOP SOUTH STE 1000
POBOX 1260
POBOX 190754
9321 MELVIN AVE
POBOX 2018
POBOX 2967
POBOX 1702
9800 RICHMOND STE 505
SAM VAN VACTOR
MARTY LINGNER
BARRETT HATCHES
T E ALFORD
GARY M ROBERTS RM 3039
J W KIKER ROOM 2086
MARK P EVANS
KATE RIPLEY
JESSE MOHRBACHER
THOMAS FINK, PHD
JIM ARLINGTON
PAMELA MILLER
GEORGE LYLE
ATTN: ROBERT RASOR
MARK WEDMAN
MARK DALTON
469 NATURAL RESOURCES BLD
MASON MAP SERV INC
JEFF LIPSCOMB
STAN STEADMAN
EXCH & GIFT DIV
Ms. Norma L. Calvert
ROBERT F SAWYER
-
ROBERT BRITCH, P.E.
RICHARD NEHRING
BOB WILLIAMS
LAURA BELL
ERIK A OPSTAD PROF GEOL
SHEILA DICKSON
WILL D MCCROCKLIN
DAVID PHILLIPS
DANIEL L LIPPE
Page 8
PORTLAND OR
HOUSTON TX
ANCHORAGE AK
HOUSTON TX
HOUSTON TX
HOUSTON TX
HOUSTON TX
ANCHORAGE AK
FAIRBANKS AK
ANCHORAGE AK
ANCHORAGE AK
ANCHORAGE AK
ADDISON TX
ANCHORAGE AK
ANCHORAGE AK
HOUSTON TX
ANCHORAGE AK
ANCHORAGE AK
CHAMPAIGN IL
AUSTIN TX
OKLAHOMA CITY OK
ANCHORAGE AK
FAIRBANKS AK
SOLDOTNA AK
KENAI AK
LOS ANGELES CA
WASHINGTON DC
KANSAS CITY MO
HOUSTON TX
ANCHORAGE AK
ANCHORAGE AK
HOUSTON TX
SEATTLE WA
LOS ANGELES CA
NEW ORLEANS LA
ANCHORAGE AK
ANCHORAGE AK
COLORADO SPRI CO
NEW YORK NY
HOUSTON TX
TULSA OK
ANCHORAGE AK
NORTHRIDGE CA
SOLDOTNA AK
HOUSTON TX
HOUSTON TX
HOUSTON TX
E~~JJ1J*~~';~'~:~ti;'-<;'CÞ'M,PAMY':i~ .:::·}:::::'f~:.::~:i"::~;'\~~H:;!:~;:~'&~.:.a;±:Z1~;t.iX~~:::!:;¡.~L:;',~~~,PÂB!.Ms~L~¡:~2)~t~~~
PETROLEUM INFO CORP
PHILLIPS ALASKA
PHILLIPS ALASKA
PHILLIPS ALASKA
PHILLIPS ALASKA
PHILLIPS ALASKA
PHILLIPS ALASKA
PHILLIPS ALASKA
PHILLIPS PETR
PHILLIPS PETR CO
PHILLIPS PETR CO
PHILLIPS PETR CO
PHILLIPS PETR CO
PHILLIPS PETROLEUM COMPANY
PINNACLE
PIRA ENERGY GROUP LIBRARY
PRESTON GATES ELLIS LLP LIBRARY
PURVIN & GERTZ INC LIBRARY
REGIONAL SUPRVISOR, FIELD OPERAT MMS
RUB ICON PETROLEUM, LLC
SD DEPT OF ENV & NATRL RESOURCES OIL & GAS PROGRAM
SHELL WESTERN E&P INC
SHIELDS LIBRARY
STANDARD AMERICAN OIL CO
STATE PIPELINE OFFICE
TAHOMA RESOURCES
TECHSYS CORP
TESORO PETR CORP
TEXACO INC
TEXACO INC
TRADING BAY ENERGY CORP
TRUSTEES FOR ALASKA
U S DEPT OF ENERGY
UNIV OF ALASKA FAIRBANKS
UNIV OF ALASKA FBX
UNIV OF ARKANSAS
UNIVERSITY OF ALASKA FBKS
UNOCAL
UNOCAL
UNOCAL
UOAl ANCHORAGE
US BLM AK DIST OFC
US BUREAU OF LAND MGMT
US BUREAU OF LAND MNGMNT
US BUREAU OF LAND MNGMNT
US DEPT OF ENERGY
US EPA REGION 10
Page 10
INST OF SOCIAL & ECON RESEARCH
RESOURCE EVAL GRP
OIL & GAS OPRNS (984)
ANCHORAGE DIST OFC
ANCHORAGE DIST OFC
ENERGY INFORMATION ADMINISTRATIO
REVENUE ACCOUNTING
PETR DEVEL LAB
PETR DEVEL LAB
SERIALS DEPT
PETR DEVEL LAB
Portfolio Team Manager
LIBRARY
GOVT DOCS DEPT
ALASKA OPERATIONS MANAGER
PARTNERSHIP OPRNS
LAND DEPT
LEGAL DEPT
KUP CENTRAL WELLS ST TSTNG
LIBRARY
4/4/01
()
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4/4/01
KRISTEN NELSON POBOX 102278 ANCHORAGE AK
JAMES WINEGARNER POBOX 10036 ANCHORAGE AK
MARK P WORCESTER POBOX 100360 ANCHORAGE AK
WELL ENG TECH NSK 69 POBOX 196105 ANCHORAGE AK
POBOX 100360 ANCHORAGE AK
STEVE BENZLER A TO 1404 POBOX 100360 ANCHORAGE AK
JOANN GRUBER ATO 712 POBOX 100360 ANCHORAGE AK
MARK MAJOR A TO 1968 POBOX 100360 ANCHORAGE AK
J W KONST P 0 DRAWER 66 KENAI AK
JIM JOHNSON 6330 W LOOP S RM 1132 BELLAIRE TX
JOE VOELKER 6330 W LP S RM 492 BELLAIRE TX
ERICH R. RAMP 6330 W LOOP SOUTH BELLAIRE TX
ALASKA LAND MGR POBOX 1967 HOUSTON TX
W ALLEN HUCKABAY PO BOX 1967 HOUSTON TX
STEVE TYLER 20231 REVERE CIRCLE EAGLE RIVER AK
3 PARK AVENUE (34th & PARK) NEW YORK NY
420 L ST STE 400 ANCHORAGE AK
2150 TEXAS COMMERCE TWR 600 TRAVIS ST HOUSTON TX
ALASKA OCS REGION 949 E 36TH A V STE 308 ANCHORAGE AK
BRUCEICLARDY SIX PINE ROAD COLORADO SPRI CO
2050 W MAIN STE #1 RAPID CITY SD
G.S. NADY POBOX 576 HOUSTON TX
UNIV OF CALIF DAVIS CA
AL GRIFFITH POBOX 370 GRAN BURY TX
KATE MUNSON 411 W 4TH AVE, STE 2 ANCHORAGE AK
GARY PLAYER 1671 WEST 546 S CEDER CITY UT
BRANDY KERNS PO BOX 8485 GATHERSBURG MD
LOIS DOWNS 300 CONCORD PLAZA DRIVE SAN ANTONIO TX
R W HILL POBOX 5197x Bakersfield CA
R Ewing Clemons PO BOX 430 BELLAIRE TX
PAUL CRAIG 5432 NORTHERN LIGHTS BLVD ANCHORAGE AK
1026 W. 4th Ave, Ste 201 ANCHORAGE AK
PHYLLIS MARTIN MS EI823 1000 INDEPENDENCE SW WASHINGTON DC
DR V AKAMATH 427 DUCKERING FAIRBANKS AK
SHIRISH PATIL 437 DICKERING FAIRBANKS AK
UNIV LIBRARIES FAYETTEVILLE AR
DR AKANNI LAWAL POBOX 755880 FAIRBANKS AK
POBOX 196247 ANCHORAGE AK
POBOX 4531 HOUSTON TX
KEVIN TABLER POBOX 196247 ANCHORAGE AK
TERESA HULL 3211 PROVIDENCE DR ANCHORAGE AK
ART BONET 6881 ABBOTT LOOP RD ANCHORAGE AK
J A DYGAS 222 W 7TH AV #13 ANCHORAGE AK
PETER J DITTON 6881 ABBOTT LOOP ROAD ANCHORAGE AK
DICK FOLAND 6881 ABBOTT LOOP RD ANCHORAGE AK
MIR YOUSUFUDDIN 1999 BRYAN STREET STE 1110 DALLAS TX
THOR CUTLER OW-137 1200 SIXTH AVE SEATTLE WA
Page 11
~)
AddrConsOrd
()
4/4/01
US GEOLOGICAL SURVEY
US GEOLOGICAL SURVEY
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US GEOLOGICAL SURVEY
US MIN MGMT SERV
US MIN MGMT SERV
US MIN MGMT SERV
US MIN MGMT SERV
US MIN MGMT SERV
US MIN MGMT SERV
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USGS - ALASKA SECTION
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VALDEZ VANGUARD
WORLD OIL
YUKON PACIFIC CORP
LIBRARY
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RESOURCE STUDIES AK OCS REGN
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EDITOR
Page 13
Page 14
BOX 25046 MS 914 DENVER CO
KEN BIRD 345 MIDDLEFIELD RD MS 999 MENLO PARK CA
2255 N GEMINI DR FLAGSTAFF AZ
NATIONAL CTR MS 950 RESTON VA
KIRK W SHERWOOD 949 E 36TH A V RM 603 ANCHORAGE AK
381 ELDEN ST MS 4022 HERNDON VA
FRANK MILLER 949 E 36TH A V STE 603 ANCHORAGE AK
949 E 36TH A V RM 603 ANCHORAGE AK
949 E 36TH AV RM 110 ANCHORAGE AK
RICHARD PRENTKI 949 E 36TH AV ANCHORAGE AK
JIM SCHERR 949 E 36TH A V RM 603 ANCHORAGE AK
4200 UNIVERSITY DR ANCHORAGE AK
POBOX 367 VALDEZ AK
POBOX 98 VALDEZ AK
DONNA WILLIAMS POBOX 2608 HOUSTON TX
JOHN HORN VICE CHM 1049 W 5TH AV ANCHORAGE AK
4/4/01
()
AddrConsOrd
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Notice of Public Hearing
STATE OF ALASKA
Alaska Oil and Gas Conservation Commission
Re: Meltwater Oil Pool, Kuparuk River Field - Pool Rules and Area Injection Order
PHILLIPS Alaska, Inc. by letter dated March 12, 2001, has applied for an area
injection order and pool rules under 20 AAC 25.460 and 20 AAC 25.520, respectively, to
enable development of the Meltwater Oil Pool, Kuparuk River Field, on the North Slope
of Alaska.
A person may submit a written protest or written comments on the requested
exemption prior to 4:00 PM on April 25, 2001 to the Alaska Oil and Gas Conservation
Commission, 3001 Porcupine Drive, Anchorage, Alaska 99501. In addition, the
Commission has tentatively set a public hearing for April 25, 2001 at the Alaska Oil and
Gas Conservation Commission, 333 W. 7th, Suite 100, Anchorage, Alaska. A person
may request that the tentatively scheduled hearing be held by filing a written request with
the Commission prior to 4:00 PM on April 12, 2001.
If a request for a hearing is not timely filed, the Commission will consider the
issuance of an order without a hearing. To learn if the Commission will hold the
tentative hearing, please call 793 -1221.
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 Jody Colombie at 793-1221
before April 18, 2001.
~4ùG ~W-. ~
Camil1é Oechsli Taylor
Commissioner
Published March 23, 2001
ADN AO# 02114013
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Anchorage Daily News$/291~OQ1
Affidavit of Publication
1001 Northway Drive, Anchorage, AK 99508
PRICE OTHER OTHER GRAND
AD# DATE PO ACCOUNT PER DAY CHARGES CHARGES #2 TOTAL
807914 03/23/2001 02114013 STOF0330 $94.17 $0.00 $0.00 $94.17
$0.00 $0.00 $0.00
$94.17 $0.00 $0.00 $94.17
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STATE OF ALASKA
, Alaska 011" and Gas·
,. Conservation Commission
Re: Meltwater Oil Pool,
Kuparuk River Field -
Pool Rule,s and Area In-
lectlon, .Order
PHILLIPS Alaska, Inc'"
by letter dated March 12,
, 2001-, has applied for an
area injection order and
, pool rules under 20 ÄAC
: 25.460 and' 2Q AAC 25.520,
, respectively, tp enable
~ de vel 0 P me n t . Of the
I Meltwater 011 Pool, Ku-
, paruk,R'iver,Fièll:l; on the
, North Slope of Alaska. '
I A person may submit a
, wrlttel1:protes,-or wrlt-
¡ten comm,'nts on the're-
I quested exemption, prior
, to 4:,OO.PM an,Aprll,25,
: 2001 to· the Alaska 0/1 'and
; Gas Conservation Com-
mission, 3001 Porcupine
, Drive, Anchorage, Alaska ,
: 99501. 'In addltlo,n, ,the
Commission has tenta-
tively set: a public 'hear-
Ing for April 25, 2001 at
the Alaska Oil and Gas
Conservation Commis-
sion, 333 W. 7th Avenue,
I Suite 100, Ancho·rage,
I Alaska. A person may 're-
, quest that the ,tentativelY,
scheduled'hearlng be held
I by fill n9 a written re-
quest with the Com mls-
: sian prior fa, 4:00 PM on,
April ,12; ~OOl. .
. If!c:ii:r::~~~·e~t:foÍ""a,:,.,eàr;..
,ing is.' nortimelyJUed,the
COT\r:nts(;lon,wHI con-
si(Ìerthe l~suaqClir of. an
orderw.ltho/./t,,, hearln,""
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793-'1221.': ' , ' '
STATE OF ALASKA
THIRD JUDICIAL DISTRICT
Eva Alexie, being first duly sworn on oath deposes and says that she
is an advertising representative of the Anchorage Daily News, a
daily newspaper.
That said newspaper has been approved by the Third Judicial
Court, Anchorage, Alaska, and it now and has been published in
the English language continually asa daily newspaEer in
Anchorage, Alaska, and it is now and during all saia time was
printed in an office maintained at the aforesaid place of
publication of said newspaper. That the annexed is a copy of an
advertisement as it was published in regular issues (and not in
supplemental form) of said newspaper on the above dates and
that such newspaper was regularly distributed to its subscribers
during all of saId period. That the full amount of the fee charged
for the fore~oing publication is not in excess of the rate charged
private indIviduals.
Signed 2uc,-----, Q~~
Subscribed and sworn to me before this date:
Notary Public in and for the State of Alaska.
Third Division. Anchorage, Alaska
MY COMMISSION EXPIRES: /é.6 S; ~ f
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......
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If YOU arl'a Dl'r<>on with
, á di'ilaDlllty who may
nE'E-d 0 sDl'clal modifica·
tionln order,to comm~nt
or to attend thep/./bllc
; hearing, 'please contact
; Jody Colombie at 793-1221
\ before April 18, 2001., ,
~ "Is/Camille Òechsll TOYlor
Commissioner ,. '. '.
/!2u1Ld)
AO-D21140,13 '
Pub.: March 23, 2001
-
PUBL\C --
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PHilliPS Alaska, Inc.
A Subsidiary of PHilLIPS PETROLEUM COMPANY
Post Office Box 100360
700 G Street
Anchorage, Alaska 99510
Telephone 907 265-6806
Ryan Stramp, Meltwater Coordinator
March 12, 2001
RECEIVED
MAR 1 2 2001
Alaska Oil & Gas C
ons Com .
AnChorag~ mission
Ms. Julie Heusser, Mr. Dan Seamount and Ms. Cammy Taylor
Alaska Oil and Gas Conservation Commission
333 West 7th Avenue
Anchorage, AK 99501
Re: Meltwater Area Injection Order
20 AAC 25.402
Dear Commissioners:
Phillips Alaska, Inc. (PAl) is pursing development of the Meltwater Reservoir through an
expansion of the Kuparuk River Unit. (Parallel efforts to expand the Kuparuk River Unit
and formulate pool rules to facilitate Meltwater Reservoir development are in progress.)
PAl briefed the Commission on Meltwater during a January 30, 2001 meeting. PAl in
its capacity as operator submits this letter as an application for Alaska Oil and Gas
Conservation Commission approval to conduct an enhanced recovery operation
involving MWAG (i.e., alternating water and miscible gas injection), consistent with 20
AAC 25.402 (a). Approval of this application would permit these operations to be
conducted in the Meltwater Pool within the initial area targeted for development.
The following attachments are submitted pursuant to 20 AAC 25.402 (c):
1. Plat with location of all existing wells that penetrate the injection zone within one-
quarter mile of the area covered by this application
2. List of operators and surface owners within one-quarter mile of the proposed
injection operations
3. Affidavit showing the operators and surface owners within one-quarter mile of the
area affected by the Meltwater Area Injection Order have been provided a copy of
this application
4. Full description of the proposed operation
5. Description, depth, and name of the pool to be affected
6. Description of the formation into which fluids are to be injected and the associated
confining zones
7. Type well log
8. Casing description and proposed method for testing injection well casing
9. Injection fluid data
10. Estimated pressures
11. Evidence and data to support a commission finding that injection wells will not
initiate or propagate fractures through the overlying strata
12. Analysis of the water within the formation
Phillips Alaska, Inc. is a subsidiary of Phillips Petroleum Company
)
)
"
13. Reference to applicable freshwater exemption issued under 20 AAC 25.440
14. Incremental increase in ultimate hydrocarbon recovery.
15. Mechanical condition of each well that has penetrated the proposed injection zone
within a one-quarter mile radius of the Meltwater Oil Pool.
I appreciate your work on this application and would be happy to answer any related
questions. I can be reached at 265-6268 or rstramp@ppco.com via email.
Sincerely,
~O-r, S~~
Ryan Stram p
Meltwater Coordinator
cc: Mike Kotowski
RECErVED
MAR 1 2 2001
Alaska Oil & Gas Cons. Commission
Anchorage
Meltwater Area Injection Order
Page 2/29
)
)
Meltwater Area Injection Order
Attachment 1
20 AAC 25.402 (c)(1)
Plat of Wells Penetrating Iniection Zone
The attached map (Attachment 1 A) shows all existing wells that penetrate the injection
zone in the proposed injection area. The map also shows Meltwater Reservoir seismic
anomalies and the proposed Kuparuk River Unit expansion area. Although the exact
acreage of the expansion has not yet been finalized, this map shows its largest
possible extent based on current expansion efforts. In addition, the map shows
Meltwater development wells (with their expected initial service) planned to be drilled
during 2001 and 2002 and Meltwater exploratory well penetrations. Initial well location
and service plans will likely change as net pay and well performance data are gathered.
The total number, type and locations of wells ultimately drilled into the Meltwater Pool
will also be a function of net pay and well performance data.
Since Meltwater Reservoir distribution is stratigraphically controlled and sand
accumulations are localized, sand continuity is expected to be difficult to predict.
Producer/Injector interactions will likely be difficult to predict in the absence of field
data. Development plans call for minimizing the number of injection wells until
producer/injector interactions are better understood. Producers will be converted to
injection service as necessary in order to provide pressure support and minimize
injectant cycling. Hence, to as large of an extent as possible, plans are to let reservoir
performance be a guide in optimizing pattern configurations.
Although initial development plans do not include a Class II disposal well, future needs
may eventually require one. The Ivishak Sandstone of the Sadlerochit Group has been
selected, if needed. This zone is expected to have at least 60 feet of sandstone with
porosities greater than 15% in the vicinity of the Meltwater Participating Area. The
Ivishak depth is expected to be approximately 8500 feet subsea. Several exploration
wells have been drilled to this horizon in the vicinity of the Meltwater Participating Area,
in particular, the Union Kookpuk, Union Itkillik River and Sinclair Colville wells. The
Ivishak Sandstone was wet in each of these wells and is therefore also expected to be
wet in the vicinity of the Meltwater Participating Area wells (see Sinclair Colville log
section, Attachment 11 c). The Ivishak Sandstone, as well as the overlying Shublik
Formation and Sag R. Sandstone, was wet in each of these wells. This zone is
therefore also expected to be wet in the vicinity of the Meltwater Participating Area.
The Ivishak Sandstone is separated from the overlying Kuparuk River Formation by
approximately 1800 feet of shales of the Kingak Formation, as well as approximately
400 feet of Shublik and Sag River Sandstone.
RE.CEiVED
MAR 1 2 2001
Alaska Oil & Gas Cons, Commission
Anchorage
Meltwater Area Injection Order
Page 3/29
)
)
Meltwater Area Injection Order
Attachment 2
20 AAC 25.402 (c)(2)
Operators and Surface Owners within One Quarter Mile of Iniection Operations
Operator:
Phillips Alaska, Inc.
Attention: Dan Kruse A TO-1220
P.O. Box 100360
Anchorage, AK 99510-0360
Surface Owner:
State of Alaska
Department of Natural Resources
Attention: Mike Kotowski
P.O. Box 107034
Anchorage, AK 99510
RECErv?ED
MAR 1 2 2001
,,A,laska Oil & Gas Cens, Commission
Anchorage
Meltwater Area Injection Order
Page 5/29
)
Meltwater Area Injection Order
Attachment 3
20 AAC 25.402 (c)(3)
Affidavit of Ryan L. Stramp Regarding Notice to Suñace Owners
Ryan L. Stramp, on oath, deposes and says:
1. I am the Meltwater Coordinator at Phillips Alaska, Inc., the designated operator of
the Kuparuk River Unit (which will include the Meltwater Pool).
2. On March 12, 2001, I caused copies of the Area Injection Order Application to be
provided to the surface owner and operator of all land within a quarter mile of the
unit as listed below:
State of Alaska
Department of Natural Resources
Attention: Mike Kotowski
P.O. Box 107034
Anchorage, AK 99510
Phillips Alaska, Inc.
Attention: Dan Kruse ATO-1220
P.O. Box 100360
Anchorage, AK 99510-0360
~t7n L__ 'S~~
I J kyan L. Str~
,
STATE OF ALASKA )
) ss.
THIRD JUDICIAL DISTRICT )
SUBSCRIBED AND SWORN to before me this 12th day of March, 2001.
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My Commission Expires: <6Í\ 6(-ZCo(
RECEiVED
MAR 1 2 2001
Alaska Oil & Gas Cons. Commission
Anchorage
Meltwater Area Injection Order
Page 6/29
}
}
RECEiVED
Meltwater Area Injection Order
MAR 1 2 2001
Attachment 4
20 AAC 25.402 (c)(4)
Alaska Oil & Gas Cons. Commission
Anchorage
Description of the Proposed Operation
The Meltwater Area Injection Order is needed to develop the Meltwater Reservoir. The
expected scope of the current development project involves drilling approximately 26
wells to develop 52 MMBO associated with an estimated 132 MMBO original oil in
place (001 P) seen by existing exploratory wells in the Bermuda Interval of the
Meltwater Reservoir. Although Attachment 1 A shows 41 penetrations, this is
considered an upside case.
Field Development
Development wells will be drilled from a single new drill site. Initial development drilling
operations are planned to start during the second quarter of this year. The drilling
program will initially focus on developing the main portion of the reservoir and testing
the periphery. Well performance data and improved seismic calibrations acquired from
the initial development wells will help guide the extent of the overall development drilling
program.
Exploratory drilling targeting other zones within the Meltwater Reservoir will be
conducted concurrently with development drilling operations. Successful exploratory
drilling results could alter existing plans by (1) changing the location and target interval
of the initial development wells and (2) expanding the scope of the project to include
additional wells. An expanded project scope would likely involve additional
development drilling phases and may require an areal expansion of the proffered
Meltwater Area Injection Order.
Recovery Mechanism
Initially employing an MW AG recovery process, which consists of alternating cycles of
water and MI, is a key aspect of the planned development. Following are the main
reasons for the
1. Numerical simulation indicates that MW AG provides higher recoveries than any
other competing recovery process (i.e., primary drainage, waterflood, miscible gas
flood, and lean gas flood). For example, simulation results suggest that an
MW AG process, with a 20% cumulative hydrocarbon pore volume slug of injected
miscible gas, would provide an incremental recovery of 9% 001 P compared to a
waterflood process.
2. Enriched natural gas used at Kuparuk is miscible with Meltwater fluids at reservoir
conditions. (Henceforth in this document, enriched natural gas will be referred to
as "MI" for Miscible Injectant.) This is supported by slim tube simulation results
and is consistent with actual slim tube experiments run on Tarn crude. (Given that
the composition of Meltwater and Tarn crudes are very similar, they should behave
in a similar fashion from a phase behavior and fluid displacement standpoint.)
Meltwater Area Injection Order
Page 7/29
)ì
}
3. Greater Kuparuk Area (GKA) MI is currently piped to offset Tarn Drill Site 2N and
is transportable to Meltwater for a relatively small premium.
4. Initially pursing MWAG is imperative if this EOR process is to be employed.
Meltwater's MI supply is dependent on existing west-end GKA infrastructure. The
MW AG floods in this part of the GKA are relatively mature. Delaying
implementation of MW AG at Meltwater would therefore jeopardize this project's
EOR reserves, as critical GKA infrastructure may not be available in the future to
transport MI. (Other potential uses of the GKA MI distribution system include de-
bottlenecking production/injection lines and providing high pressure lift gas).
After the cumulative target slug size of MI has been injected into the formation,
pressure support will be maintained with water injection. Current plans are to
eventually inject lean gas into the reservoir to help recover light liquid hydrocarbons
(used to manufacture MI) that will be trapped in the reservoir by the MWAG process.
Injectant Sources
The miscible injectant employed at Meltwater will initially be the same injectant as that
currently used at Tarn and the Kuparuk River Unit Large Scale EOR Project. This
injectant is manufactured at Kuparuk's CPF-1 and CPF-2 by blending lean gas from the
Kuparuk River Unit's production facilities with light hydrocarbon liquid streams from the
Prudhoe Bay Unit and Kuparuk River Unit. The light liquid hydrocarbons from the
Prudhoe Bay Unit are NGLs from the CGF. The light liquid hydrocarbons from the
Kuparuk River Unit consist of scrubber liquids from artificial lift gas compression
systems at CPF-1 and CPF-2, NGLs from CPF-1 and naphtha from the Topping Plant.
During the flood, there is a possibility that Meltwater produced gas may be blended with
Kuparuk River Unit MI to generate a lighter MI blend customized for the Meltwater
Reservoir pressure and oil properties. Slim tube simulation results and slim tube
experiments on similar (Tarn) crude indicate that Kuparuk MI is richer than needed to
achieve miscibility with Meltwater oil at reservoir pressure (2400 psig in the Meltwater
#1 well).
After the cumulative target slug size of MI has been injected into the formation,
pressure support will be maintained with water injection. Current plans are to
eventually inject lean gas into the reservoir to help recover light liquid hydrocarbons
(used to manufacture MI) that will be trapped in the reservoir by the MWAG process.
The source of the lean gas will be Kuparuk River Unit's CPF-2. Potential gas
accumulations in the area will also be considered as possible supplemental sources.
Rl::CEi\lED
MAR 1 2 2001
Alaska Oil & Gas COilS, Comrnissiol~
.A.nchorage
Meltwater Area Injection Order
Page 8/29
~
)
Fluid and Cost Allocation
Meltwater production will be commingled with Tarn and Kuparuk production in surface
facilities prior to final processing and ultimate custody transfer in accordance with the
Meltwater Pool Rules (currently being developed). The Greater Kuparuk Area
Alignment Agreement, which set new tract ownership and facility sharing terms in the
Meltwater area, will help govern business issues associated with sharing infrastructure.
A portion of the Meltwater accumulation extends outside the existing GKA onto a
PAI/BP lease (see Attachment 4A). All GKA owners, except Exxon-Mobil (with a
.3648% GKA working interest), have agreed to buy interest in the lease. Mobil heritage
interest was proportionately split between Phillips and BP based on an estimate that
400/0 of total Meltwater reserves are located of this lease. No future production interest
adjustments will be made. The resulting Meltwater production interests, pending
approval of the Supplemental Provisions, are as follows:
Phillips Alaska, Inc.
BP
Unocal
Mobil
Chevron
0.55957929
0.39754111
0.03960480
0.00218880
0.00108600
1.00000000
Total
RECEfVED
MAR 1 2 2001
Alaska Oil & Gas Cons Comm' .
, ISSlon
,';nchorage
Meltwater Area Injection Order
Page 9/29
Attachment 4A
Meltwater Accumulation Outside Existing GKA
Meltwater Area
Order
1 0/29
)
)
Meltwater Area Injection Order
Attachment 5
20 AAC 25.402 (c)(5)
Description and Depth of Pool to be Affected
The Meltwater Reservoir is the sequence of reservoir sandstones and associated
mudstones found in the interval between 4958' and 5368' tvd subsea in the Meltwater
North #2A well, and in its lateral equivalents. The Meltwater Reservoir is late
Cretaceous in age and stratigraphically within the Seabee Formation. The reservoir is
approximately 400' thick and is composed of two intervals. The initial Meltwater Oil
Pool includes the entire Meltwater Reservoir, however, the pool definition may change
as additional information from development and exploratory activities becomes
available.
Both Meltwater and Cairn Reservoir intervals are shown in the wireline log from the
Meltwater North #2A well (see Attachment 7). Brief summaries of these intervals are
given below in descending order.
. The 'T4.1', or Cairn Interval, was encountered between 4958' and 5187' tvd subsea
in the Meltwater North #2A well. The boundaries are correlatable markers T 4.1 and
T3, respectively. Reservoir quality sands were not encountered at this location, but
may be present laterally.
. The Bermuda Interval was encountered between 5187' and 5297' tvd subsea in the
Meltwater North #2A well. The boundaries are correlatable markers T3 and T2,
respectively. Hydrocarbon-bearing sands in this interval were encountered in the
Meltwater North #2A and in two offset wells.
Two Meltwater Reservoir intervals, the Bermuda Interval and Cairn Interval, are
sufficiently understood to be included in development plans. Initial injection will be
restricted to these two intervals. An expansion of injection operations (both vertically
and areally) may be sought in the future depending on results from upcoming drilling
activities.
RECEi\/ED
MAR 1 2 2001
Alaska Oil & Gas Cons. Commission
.A.nchorage
Meltwater Area Injection Order
Page 11/29
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)
Meltwater Area Injection Order
Attachment 6
20 AAC 25.402 (c )(6)
Description of the Formation
The proposed injection zone includes the Cairn Interval and the Bermuda Interval within
the Meltwater Oil Pool. This zone lies between 4958' and 5368' tvd subsea in the
Meltwater North #2A well (Attachment 7). The Cairn Interval lies between reservoir
markers T3 and T 4.1 while the Bermuda Interval lies between reservoir markers T2 and
T3.
The Meltwater Pool sands are fine- to very fine-grained and have common shale
laminations and interbeds. Sands are compositionally heterogeneous: the major
components include quartz, heterolithic rock fragments, plagioclase and zeolite. Shale
laminations are common.
Reservoir sands, which are locally developed within each interval, are lobate to linear in
form, and are separated from adjacent reservoirs by mudstones and shales. The top of
the Meltwater Reservoir is separated from the Tabasco Sandstone equivalent, the first
overlying potential reservoir zone, by a confining layer of approximately 3000' of
impermeable shale (Attachment 11 A). The base of the Meltwater Reservoir is
separated from the underlying Kuparuk River Formation by approximately 500' of shale.
RECEf\J!E:]
MAR 1 2 ?001
Alaska Oil & Gas Cons. Commission
Anchorage
Meltwater Area Injection Order
Page 12/29
Meltwater Area Injection Order
Attachment 7
20 MC 25.402 (c)(7)
LOQ of Meltwater Tvpe Well
MELTWATER NORTH 2A
Meltwater Area Injection Order
Page 13/29
')
)
Meltwater Area Injection Order
F~E:CEjvrED
Attachment 8
MAR 1 2 2001
20 AAC 25.402 (c)(8)
/~Iaska Oil & Gas Cons. Commission
Anchorage
Casing Description and Proposed Method for Testing Casing
The proposed casing programs for a typical Meltwater well resembles the casing
programs employed in the Kuparuk River Unit (KRU). Although the standard program
incorporates maintaining a tubing annulus with isolation and pressure integrity within
200' of the initial producing interval, exceptions to this design criterion will be required
to optimize recovery from potentially productive secondary targets.
Standard Casing Program
As in KRU wells, conductor casing will be set below 75 feet to provide anchorage and
support for the rig diverter assembly. The surface casing size may be 9-5/8 or 7-5/8
inch, depending on casing setting depth and production tubing size. Surface casing will
be set below the base of the West Sak interval, effectively casing off the permafrost,
Ugnu, and West Sak formations.
Meltwater wells utilize a tapered casing string tied back to surface, that serves as the
combination production casing / tubing string installation. The casing adjacent from the
producing interval is the same size as the tubing is at the surface (monobore). The
casing across the production interval is then tied back to surface with a string of 3Y2 or
4112 inch tubing inserted into a seal bore or polished bore receptacle (positioned above
the top pay zone perforation.) This provides a tubing annulus with isolation and
pressure integrity (see diagrams shown in Attachment 8A).
There are three casing programs proposed for the Meltwater development:
Case 1) 3Y2 inch Slim hole Monobore completions. This casing program utilizes a
7-5/8 inch (L-80, 29.7 pound) surface casing string with a production string of
5Y2 inch (L-80, 15.5 pound) casing crossed over to 3Y2 inch (L-80, 9.3 pound)
casing across the Meltwater interval. These monobore wells will be
completed with 3112 inch (L-80, 9.3 pound) production tubing.
Case 2) 4Y2 inch Monobore completions. This casing program employs 9-5/8 inch
(L -80, 40 pound) surface casing with 7 inch (L -80 or J-55, 26 pound)
production casing crossed over to 4112 inch (L-80, 12.6 pound) production
casing.
Case 3) 3Y2 and 4Y2 inch Conventional completions. This casing program employs
a string of 9-5/8 inch (L-80, 40.0 pound) casing and an intermediate 7 inch (L-
80 or J-55, 26 pound) intermediate casing string set above the Meltwater
formation top. A 3112 inch (L-80, 9.3 pound) or 4112 inch (L-80, 12.6 pound)
liner would then be set across the Meltwater formation and tied back to
surface with either 3112 inch (L-80, 9.3 pound) or 4112 inch (L-80, 12.6 pound)
production tubing.
Meltwater Area Injection Order
Page 14/29
)
)
Each of these three well types may be completed for either production or injection
service. The service of the well will be determined after logging operations. Drilling
and completion plans for future Meltwater wells may vary with time as experience and
knowledge are gained.
The proposed method casing testing method for Meltwater injectors is to follow the
requirements of 20 AAC 25.412 (c). Sufficient notice of pressure tests will be given so
that a Commission representative may witness the test.
Secondary Targets
The Bermuda Interval will be the primary target of initial development efforts. Current
plans are to focus initial development efforts on that portion of the interval most likely
have good reservoir characteristics. As previously shown on Attachment 7, potentially
productive secondary targets in the Cairn Interval may be encountered during these
development efforts. Secondary targets in the Cairn Interval are expected to generally
be within 400' tvd of the Bermuda Interval. These thin, potentially productive zones
contain insufficient reserves to merit separate wells or extensive completion design
modifications. Although fracture stimulations are planned for Bermuda Interval
producers, fracture modeling indicates these stimulations will only grow approximately
100' upwards. Potentially productive secondary pay zones can therefore only be
developed if they can be inexpensively commingled with Bermuda production.
Given the initial uncertainty of producer/injector interactions, most producers will be
candidates for conversion to injection service. In order to maintain conversion
flexibility, there are no casing design differences between production and injection
wells. (Casing connections will be designed for gas or liquid service.) The flexibility to
convert wells to injection service on an as needed basis is an integral part of the
Meltwater development strategy. This complicates secondary target development as
these targets can only be pursued if they are not isolated by more than one casing
string.
Pursing secondary targets may result in exceeding the AOGCC guideline that injectors
provide annular isolation within 200' measured depth of the highest perforated interval.
Plans are to provide annular isolation within 200' measured depth of the perforated
lone, unless secondary targets are encountered with a pay thickness approaching or
exceeding 10' tvd. Based on current drilling and facility hook-up plans, the productive
nature of these secondary targets can not be fully ascertained during initial drilling
operations. If future evaluations indicate that developing secondary targets can not be
justified, there is the potential of having either current or future injectors with annular
isolation located more than 200' measured depth above the perforated zone. Meltwater
Oil Pool Rules are written to help ensure that well service flexibility is not sacrificed by
attempting to pursue thin secondary targets.
,- - ~E;·'I lfr;;c-\
RElJ ì"V t:U
MAR 1 2 2001
Alaska Oil & Gas Cons. Commission
Anchorage
Meltwater Area Injection Order
Page 15/29
')
)
Meltwater Area Injection Order
Attachment 9
20 AAC 25.402 (c)(9)
Injection Fluid Analysis
The vast majority of the MI initially employed at Meltwater will originate from Kuparuk
River Unit's CPF-2. During 2001, both MI and water will be employed to provide
pressure support and maximize sweep. After completing the MW AG recovery process,
plans are to eventually inject lean gas into the Meltwater Oil Pool to maximize recovery
of the light hydrocarbon liquids that were injected into the reservoir as part of the
miscible injectant stream.
The source of the lean gas will likely be Kuparuk River Unit's CPF-2. However, other
potential gas sources will also be considered. The initial water injection source will be
CPF-2 produced water. Local separation and reinjection of water at Meltwater may be
considered in the future. Fresh water collected in well cellars from snowmelt may also
be injected for short time periods to minimize road traffic during the caribou calving
season.
The average MI and lean gas composition produced at the Kuparuk CPF-2 facility
during 2000 is presented below. Also shown below is a CPF-2 produced water analysis
from February 2000.
Maximum MI/lean gas and water injection rates into the Meltwater Oil Pool are
estimated at 80 MMSCFPD and 65 MBWPD, respectively.
There is no evidence from laboratory core flood experiments or compositional studies
that indicate the fluids proffered for long-term injection would pose any appreciable
compatibility problems for either the Meltwater Formation or its confining zones. Short
periods of fresh water injection are also not expected to cause any appreciable
compatibility problems. If injectors do incur damage from fresh water injection,
remedial treatments (e.g., acid stimulations, high pressure breakdowns, etc.) can be
employed.
RECEiVED
MAR 1 2 2001
.6,18s)(a Oil & Gas Cons. Commission
Anchorage
Meltwater Area Injection Order
Page 16/29
)
)
Miscible Injectant & Lean Gas Composition Supplied by
the Kuparuk River Unit's CPF-2
Component MI Lean Gas
(Mole 0/0) (Mole 0/0)
CO2 0.89 0.5
N2 0.27 0.3
C1 81.37 69.6
C2 8.79 6.7
C3 5.10 5.0
i-C4 0.92 2.2
n-C4 1.99 6.3
i-C5 0.30 2.0
n-C5 0.28 2.5
C6 0.07 2.1
C7 0.01 1.8
C8+ 0.00 1.0
CPF-2 Produced Water Analysis
Component
Concentration
(m all)
159
12
1,920
<0.15
20
35
18
137
13,131
<0.06
<10
12.6
0.74
1.2
<0.003
99
<0.5
60
20
8,800
6.7
Sulfate
Sulfide
Bicarbonate
Aluminum
Ammonia
Barium
Boron
Calcium
Chloride
Chromium
FI uoride
Iodide
Iron
Lithium
Manganese
Magnesium
Phosphorus
Potassium
Silicon
Sodium
Stronti um
Meltwater Area Injection Order
RECEI\/ED
M/4R 1 2 2001
Alaska Oil & Gas Cons. Commission
Anchorage
Page 17/29
')
)
Meltwater Area Injection Order
Attachment 10
20 AAC 25.402 (c)(10)
Estimated Pressures
The maximum MI and water injection pressures available at the plant will be 4,400 psi
and 3000 psi, respectively. Due to pressure losses in the distribution system, actual
maximum wellhead pressures will vary. Injection wells may also be choked to avoid
exceeding injection targets. MI and water wellhead injection pressures are expected to
range from 2,600 - 3,600 psi and 1600 - 2600 psi, respectively.
RECEì\li:D
MAR 1 2 2001
Alaska Oil & Gas Cons. Commission
Anchorage
Meltwater Area Injection Order
Page 18/29
)
J
Meltwater Area Injection Order
Attachment 11
20 AAC 25.402 (c)(11)
Fracture Information
Injection into the Meltwater Formation will not breach the reservoir's confining zones.
Neither injection nor formation fluids will be able to enter any freshwater strata.
Although bottom-hole pressures may exceed the formation parting pressure during
enhanced recovery operations (i.e., water and MI injection), the Meltwater producing
sands are separated by over 2000' of confining shales and mudstones which act as an
impermeable barrier (see Attachment 11 A). These confining layers provide a
substantially greater barrier than necessary to contain fractures within the Meltwater
interval. Fracture modeling using Stimplan (i.e., Nolte/Smith's quasi 3-D model)
confirms this as predicted fracture heights are entirely contained within the perforated
interval. For example, injecting water at a rate of 10,000 BWPD at a surface pressure
of 2200 psi would result in upward fracture growth of only 10'. Injecting MI at an
injection rate 15 MMSCFPD at a surface pressure of 3500 psi would cause no
appreciable height growth.
The above-mentioned fracture modeling is based on single, planar, vertical fractures
that result from relatively short duration injection. Since these modeling captures
neither dentritic fractures nor disaggregation (i.e., destruction of the rock matrix), model
predicted fracture growth associated with long term injection is too large.
Hydraulically propped fracture stimulations are planned for Meltwater producers. The
1500' of confining shales and mudstones also provide a substantially greater barrier
than necessary to contain these fracture stimulations. Fracture modeling using
Stimplan suggests that typical fracture stimulations will grow upward approximately
100'. Model runs with worst case assumptions (which cause the most upward growth)
suggest the stimulations will not exceed 300' of upward growth. For example, a
fracture stimulation with 200,000 pounds of proppant with only 70' of gross interval is
forecasted to result in a maximum upward fracture height of approximately 200' (see
Attachment 11 B).
As previously mentioned, no disposal injection is initially planned in the Meltwater
Participating Area. However, the Ivishak sandstone is being permitted for Class II
disposal to address potential future needs. Approximately 2000' tvd of confining rock
separate this zone from Meltwater Reservoir strata. In addition, there are no potential
fresh water strata within several thousand feet of the zone (see Attachment 11 C). If the
Ivishak is used for disposal injection in the future, modeling will be conducted at that
time using the best available tools to help ensure that the planned disposal volumes
pose no risk to either potential freshwater strata or hydrocarbon recoveries.
R E~-" t'-~ E' f\ I;: ¡<U~'
\,J I V L-"
MAR 1 2 2001
Meltwater Area Injection Order
Alaska Oil & Gas COilS, Commission
Anchorage
Page 19/29
Attachment 11 A
Meltwater North #2A Confining Intervals
MELTWATER NORTH #2A
GAMNA RAY í RESISTIVITY
~
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1..Y.tJo_.a~
, I
D WI 111II
~AelTWATE.~
POOL
Meltwater Area Injection Order
Page 20/29
.
.
MAR 1 2 2001
Atta c h me nt 11 B ,;iéJSKa 8. Cèas Cons. Commission
Anchoraqe
Stimplan Results-Worst Case Height Growth -
· .
· .
· .
· .
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· .
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... ..........
.... .................
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5800
Max Width 0.93 in
phillips Alaska Inc.
Meltwater Frac 2
At Closure
20
Meltwater Area Injection Order
·
·
·
·
·
·
·
... . ... ... . ...
...................-..
· . ... . . .
· . ... . . .
·
·
·
·
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.......................................................
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· . . . .
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..................................................
· . . . .
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· . . .
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· . . . .
· . . . .
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· . . . .
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........ø.........~........~.........~........~...····.
· . . . .
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5200
--
·
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5400
·
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................
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Area :
·
·
· .
....................
· .
·
·
·
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·
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o
5500
·
·
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· . . . . .
....~..·~·..t·..t..1'·· 5700
· . .. . . .
-0.E-0.4-0.;'0.0 0.2 OA 0.6
200 300 400
Fracture Penetration (ft)
500
100
.
.
· Io . . . . . . . .
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. . . . . . . . . .
· . . . . . . . . .
· . . . . . . . . .
.. . . . . . . . . .
· . . . . . . . . .
· .. . . . . . . . .
· . . . . .. . . . .
........~..........~.......--.......#.............................,...........~.......~.......~..........
· . . . . . . . . .
· . . . . . . . . ..
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· . . . . . . . . .
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........~..........~.......~.........................................................~...................
· . . .. . . . . . ..
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· . . . . . . . . .
· . . . . . . . . .
5.0
20
50 100
Time (min)
200
500
1000
2000
10
Page 21/29
Attachment 11 C
Sinclair Colville #1 Confining Intervals
Meltwater Area
Order
lØ
¡en
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Sinclair
Colville #1
I
~
Page 22/29
.
.
Meltwater Area Injection Order
Attachment 12
AAC 25.402 (c)(12)
Formation Fluid
No oil-water or gas-water contacts within the Meltwater formation have been
encountered.
In the Bermuda interval at Tarn, average salinity estimates from immobile connate
water were estimated from low invasion cores. Connate water was obtained from core
plugs using a miscible (CHCI3 / CH30H) extraction process. Subsequent water
volumes were estimated using Karl Fisher analysis and chlorides were measured using
ion chromatography. The resultant estimated connate water NaCI concentration was
30 Kppm.
Anomalous lab results on Meltwater cores indicate a chloride content in the Bermuda
Interval at Meltwater North of 20 Kppm NaC!. Due to uncertain lab procedures, Core
Labs has little confidence in this value and estimates the actual value (based upon
anion calculations) to be in the 35-40 Kppm NaCI range. Further testing on subsequent
cored wells at Meltwater is planned.
c
MAR 1 2 200î
Alaska Gas Cons,
Meltwater Area Injection Order Page 23/29
.
.
RECE¡\lED
Meltwater Area Injection Order
Attachment 13
MAR 1 2 2DOí
20 AAC 25.402 (c)(13)
Alaska Oil & Gas Cons. Commission
Anchorage
Aquifer Exemption
The proposed Meltwater pool lies just south of the current Kuparuk River Unit (KRU)
exemption area established by the EPA on May 11, 1984 (see Attachment 13A). An
aquifer exemption is being sought for the Meltwater Pool, as there are no potential fresh
water sands in the area suitable for human consumption.
No porosity logs were acquired in the surface portion (above approximately 1900' tvd
subsea) of the Meltwater North wells.
As part of the permitting process for the exploration season, three wells with shallow
logs were analyzed for water salinity (see below). Two of the wells (Kalubik #1 and
Colville River St. 1) are outside the existing KRU and Alpine Aquifer Exemption Areas.
The third well (Cirque 2) is located within the KRU Aquifer Exemption Area.
The following table is a list of salinity calculations for the sand underneath the
permafrost. Calculated fluid resistivities are corrected to 75° F and salinity numbers are
in NaCI equivalent, or total dissolved solids (TDS).
Rt = 2.1 Qm
Rwa = 2.1 em
(2.5 Kppm)
SP = -20 mv (@ 35°)
RwSP = 1.03 em
(5.4 Kppm)
a cu atlons are Inva I
due to the presence of
hydrates. Actual
salinities are higher.
SP more representative
than Rwa, though still
too low.
In the Kalubik and Cirque wells, average resistivities drop dramatically below these
sands, indicating much saltier waters. In the Colville well, the high salinities begin at
the base of permafrost.
Kalubik
Water salinities below permafrost are estimated to be in the 10-12 Kppm range (TDS),
increasing to 25 Kppm below 1950'. An analysis of a water sample from Albian aged
sands (5050-5250') in this well tested 24.3 KPPM TDS.
Meltwater Area Injection Order
Page 24/29
.
.
Colville River St. 1
Salinities below permafrost are approximately 25 Kppm TOS.
Cirque 2
Under permafrost, salinities are 6+ Kppm increasing to 21 Kppm below 2200'. The
sand immediately below the permafrost is believed to contain gas hydrates. This
causes log based salinity calculation results to be too low.
Tarn 2N-349
In addition to the three wells above, Tarn Well 2N-349 was also analyzed for shallow
water salinities. This well was logged across the shallow portion of the hole as part of a
USGS study on gas hydrates. This well is located within the existing KRU Aquifer
Exemption Area.
The base of permafrost is 1310' at this location. Sands immediately below permafrost
are affected by gas hydrates. This is supported by gas sampling done by USGS in
Tarn Well 2N-305 (see Attachment 138). Calculated salinities below 1900' increase to
10 Kppm.
R CEIVE[)
MAR 1 2 2001
Aiaska Oii & Gas Cons. Commission
Anchorage
Meltwater Area Injection Order
Page 25/29
AlpineAquifer
Exemption
hment 13A
ional Aquifer Exemption Map
Kuukpik
Kalubik 1
It
North S:ar
Milne Point
Kuparuk River
Prudhoe Bay
Alpine Pool
Sections
2N-349
It
Greater Kuparuk
Aquifer Exemption
2
N2
Proposed
Meltwater Pool
Meltwater Area Injection Order
Page 26/29
Attachment 138
rn 2N...305 Shallow Cuttings Samples
ARN 2N 305 SH LLOW CD
INGS GAS SAMP ES
Gas
Hydrates
Area Injection Order
Page 27/29
)
)
Meltwater Area Injection Order
Attachment 14
20 AAC 25.402 (c)(14)
Incremental Hvdrocarbon Recovery
The Meltwater Sand was tested in the Meltwater #1 exploration well. Fluids recovered
from the test indicated the interval contains 36° API gravity crude with a solution GOR of
approximately 620 SCF/B. There is no evidence that this zone is in contact with either
an aquifer or gas cap to provide pressure support.
Simulation results indicate that an MW AG process with a cumulative 20% hydrocarbon
pore volume slug of MI would provide an overall recovery factor of approximately 380/0
OOIP. This recovery factor is approximately 9% OOIP higher than that obtained from
waterflood and more than 20% OOIP higher than that obtained from primary depletion.
R t: ~~ E-' ~ \ / ;k: ~'-"~.~
\...J. ~ v C J,~J
MAR 1 2 200î
Alaska Oil & Gas Cons. Commission
Anchorage
Meltwater Area Injection Order
Page 28/29
')
)
Meltwater Area Injection Order
Attachment 15
20 AAC 25.402 (c)(15)
Mechanical Condition of Existing Penetrations
There are no active wells within a one-quarter mile radius of the Meltwater Oil Pool.
However, two exploratory wells and a sidetrack were drilled to evaluate the area.
These penetrations have been plugged and abandoned as per AOGCC regulations (20
AAC 25.112). All casing strings were cut three feet below the original ground level with
well abandonment markers installed as per 20 AAC 25.120. The well cellars were
removed and the remaining holes back filled to ground level with gravel.
RECE~\/EC)
MAR 1 2 In,! î¡
Alaska Oil & Gas COilS. Commission
Anchorage
Meltwater Area Injection Order
Page 29/29
)
)
KUPARUK RIVER UNIT
TESTIMONY FOR MELTWATER OIL
POOL RULES
, March 12, 2001
h ~ ~
PHILLIPS · PHilliPS Alaska, Inc.
"lTlt A Subsidiary of PHILLIPS PETROLEUM COMPANY
~
. . ' ~..- I¡'"'"""'-'
RECE\\¡ cU
MAR 1 2 ZOOí
0'\ & Gas Cons, CommiSSion
,~\aska I
Anchorage
)
')
TABLE OF CONTENTS
Paae
I. Introduction 1
II. Geology 3
III. Reservoir Description 6
IV. Reservoir Development 9
V. Facilities 15
VI. Drilling & Well Design 18
VII. Reservoir Surveillance 24
VIII. Summary of Testimony 27
IX. Proposed Meltwater Oil Pool Rules 29
X. Proposed Findings & Conclusions 32
XI. List of Exhibits 34
V \.,.,- ?"-.~
RECE\' t.v
Mp..R 1 2 2001
,... cornmission
. Oil & Gas 'vons,
,fl,\as\\a P"nchorage
Meltwater Oil Pool Rule.... )estimOny
)
March 12, 2001
I. Introduction
This hearing has been scheduled in accordance with 20 MC 25.540 with a
public notice period started on March 12. The purpose of this hearing is to
present testimony to support classification of the Meltwater Reservoir in and
around the Meltwater Participating Area as an oil pool and establish pool rules
for development of said oil pool pursuant to 20 MC 25.520. Phillips Alaska, Inc.
(PAl) is presenting testimony on behalf of the Meltwater Working Interest Owners
(WIOs). The scope of this testimony includes a discussion of geological and
reservoir properties, as they are currently understood, and PAl's plans for
reservoir development and surveillance, well planning, facilities installation and
project scheduling.
This testimony will enable the Commission to establish rules that allow
economical development of resources within the Meltwater Oil Pool. Confidential
data and interpretation concerning the Meltwater formation will be furnished to
the Commission as additional support testimony. Development drilling and
facility installation are scheduled to commence during the second quarter of
2001 with initial production beginning by year-end.
The proposed Meltwater Oil Pool includes all potential hydrocarbon-bearing
zones within the Meltwater Reservoir. The areal extent of the pool is limited to
areas that have been targeted for either development or possible exploratory
activities. The WIOs recognize a need for a consistent development strategy for
the Meltwater Reservoir. Pool rules for the entire reservoir will help maintain this
consistency. As additional information and understanding of the Meltwater
Reservoir is acquired, PAl will work with the Commission to ensure the Meltwater
Oil Pool definition continues to make sense.
Kuparuk River Unit (KRU) facilities will be employed to process production and
supply injectant. The Meltwater Participating Area will be operated in
accordance with special supplemental provisions to the Kuparuk River Unit
Operating Agreement (i.e., the Meltwater Special Supplemental Provisions).
The properties to be developed (i.e., the Meltwater Oil Pool) are leased from the
State of Alaska. A portion of the Meltwater Oil Pool is located within the present
boundaries of the Kuparuk River Unit. PAl, on behalf of the Meltwater Oil Pool
WIOs, will be filing an application ("Unit Expansion Application") with the
Commissioner of the Department of Natural Resources to expand the Kuparuk
River Unit area to include the remainder of the Meltwater Oil Pool. The Unit
Expansion Application will also request Department of Natural Resources
approval of a Meltwater Participating Area, which will include the Meltwater Oil
Pool. PAl intends to file this application no later than May 1, 2001. The Unit
Expansion Application will also include plans of development and operations for
1
Meltwater Oil Pool Ru )-estimony
')
,I
March 12, 2001
the Meltwater Participating Area, including the Meltwater Oil Pool. PAl will file a
copy of the Unit Expansion Application with the Commission.
The interests of the Meltwater WIOs will be integrated within the Meltwater
Participating Area of the Kuparuk River Unit. Costs and production will be
allocated in accordance with the Meltwater Special Supplemental Provisions.
Ownership assignments have been filed with the Alaska Department of Natural
Resources. The Meltwater Participating Area working interests are shown
below.
Phillips Alaska, Inc.
BP
Unocal
Mobil
Chevron
0.55957929
0.39754111
0.03960480
0.00218880
0.00108600
Total
1.00000000
2
Meltwater Oil Pool R, )Testimony
')
March 12, 2001
II. Geology
Introduction
This portion of the testimony provides geologic data to the Commission in
support of PAl's proposed Meltwater Oil Pool.
Stratigraphic Nomenclature
The Meltwater Reservoir is the sequence of reservoir sandstones and associated
mudstones found in the interval between 4958' and 5368' tvd subsea in the
Meltwater North #2A well, and in its lateral equivalents. The Meltwater Reservoir
is late Cretaceous in age and stratigraphically within the Seabee Formation. The
reservoir is approximately 400' thick and is composed of two intervals. The initial
Meltwater Oil Pool includes the entire Meltwater Reservoir, however, the pool
definition may change as additional information from development and
exploratory activities becomes avai,!e:,ble.
Both Meltwater Reservoir intervals are shown in the wireline log from the
Meltwater North #2A well (Exhibit 1). Brief summaries of these intervals are
given below in descending order.
. The 'T4.1' or Cairn Interval was encountered between 4958' and 5187' tvd
subsea in the Meltwater North #2A well. The boundaries are correlatable
markers T4.1 and T3, respectively. Reservoir quality sands were not
developed at this location, but may be present laterally.
. The Bermuda Interval was encountered between 5187' and 5297' tvd subsea
in the Meltwater North #2A well. The boundaries are correlatable markers T3
and T2, respectively. Hydrocarbon-bearing sands in this interval were
encountered in the Meltwater North #2A and in two offset wells.
Stratigraphic Description
The Meltwater Sands comprise a sequence of oil-bearing, very fine- to fine-
grained marine sandstones and interbedded mudstones. Initial injection
operations will initially be restricted to these two intervals. As information is
gained about the Cairn Interval, the Meltwater Oil Pool definition may be
modified.
The Bermuda interval is bounded by the T3 and T2 surfaces. The T2 surface
appears to be erosional; the nature of the T3 surface is uncertain at this time.
3
Meltwater Oil Pool R~ )Testimony
')
March 12,2001
Sand profiles vary from well to well. Sandbodies in the Bermuda interval consist
of Channel fill and lobate deposits.
The Cairn interval is bounded by the T3 and T4.1 surfaces. The T4.1 surface
may be a conformable contact. The Cairn sandbody is linear in form.
The areal distribution of Meltwater sandbodies is shown in Exhibit 2.
Sandbodies are distributed in an overlapping geometry within the proposed
Meltwater Oil Pool area.
A{:Ie of Sediments
Based upon Phillips in-house micropaleontologic and palynologic data, the
Meltwater Sands sequence is late Cretaceous (Cenomanian-Turonian) in age.
Proposed Pool Name
The primary reservoir covered by this application was first encountered in 2000
in the Meltwater North #2 well. The use of II Meltwater" as the reservoir and pool
names was based on the names of the confirmation wells (i.e., Meltwater North
#1 and Meltwater North #2A). The zone was first flow tested during 2000 in the
Meltwater North #1 well, where rates of approximately 4000 BOPD of 36 degree
API oil were obtained.
Proposed Vertical Pool Boundaries
The Meltwater Oil Pool is the hydrocarbon accumulations in the sequence of oil-
bearing, very fine- to fine-grained sandstones and mudstones between 4958'
and 5368' tvd subsea in the Meltwater North #2A well and its lateral equivalents.
This zone is bounded below by the T 4.1 log marker and above by the C35 log
marker. C35 is recognized on Meltwater North #2A logs and its lateral
equivalents as the low resistivity spike at 5368' tvd subsea representing the top
of the Albian age shales underlying the Meltwater reservoir. T 4.1 is recognized
by the high gamma-ray log reading above a blocky silty sand at 4958' tvd subsea
in the Meltwater North #2A well and its lateral equivalents.
Structure
The Meltwater Oil Pool has been mapped using 3D seismic data. Structural dip
is generally to the east. The T3 surface, the top of the Bermuda Interval, dips to
the east-southeast; dipping approximately 2-3 degrees near the Meltwater North
4
Meltwater Oil Pool R,- )Testimony
)
March 12, 2001
#1 well (Exhibit 3). Complex faulting is seen along the west (updip) edge of the
Meltwater Oil Pool. Channel complexes positioned to the north, south and east
of the Meltwater Oil Pool cut through the T3 reservoir and act as lateral
boundaries. No faults are mapped within the main reservoir trends. Bermuda
Interval depths range from approximately 4700' subsea in the west to 5500'
subsea in the east.
The Cairn Interval stratigraphically overlies the Bermuda Interval, and is offset to
the east of the Bermuda Interval. The T4.1 surface, the top of the Cairn Interval,
is shown in Exhibit 4. Faulting is similar to the pattern on T3. Structural depth of
the Cairn Interval ranges from 4800' to 5500' subsea. Because of structural dip,
the Cairn Interval is generally structurally level with or deeper than the Bermuda
Interval
Con trois on Oil Distribution
Trapr>ing in the Bermuda and Cairn Intervals is stratigraphic, and hydrocarbon
dis1ribution is controlled by sand distribution. No water or gas cap has been
encountered within the Bermuda Interval. Both the Bermuda and the Cairn
Intervals dip east with updip stratigraphic seals to the west.
5
Meltwater Oil Pool R ) Testimony
')
March 12, 2001
III. RESERVOIR DESCRIPTION
Introduction
This section summarizes reservoir properties. Core data provides the foundation
for much of the rock property information presented in this section. Whole cores
were collected from the Meltwater North #1 and Meltwater North #2. In addition,
rotary side-wall cores were obtained from the Meltwater North #2A and the
Meltwater North #1 well (in a section where whole core was not obtained). A
cased hole test of the Meltwater #1 provides the basis for the fluid information.
Porosity, Permeability and Water Saturation
The Meltwater Oil Pool sands are fine to very fine-grained and have common
shale laminations and interbeds. Sands are compositionally heterogeneous.
The major components are quartz, heterolithic rock fragments, plagioclase and
zeolite. The heterolithic component consists of sedimentary, igneous and
metamorphic rock fragments. Zeolites result from diagenetic alteration of
volcanic glass. Dominant clays are chlorite, and Illite, with lesser amounts of
kaolinite and 'stable-phasel mixed layer Illite/Smectite. While XRD analyses
show clay content in the range of 15 to 25%, clay minerals are dominantly in the
heterolithic grains rather than in the matrix.
Core measured porosities range from 17% to 25% and average 20%).
Corresponding air permeabilities range from 1 md to 80 md and average
approximately 10 md. The average core based water saturation (after correcting
for invasion) was measured at 40%.
Net Pay Determination
Petrographic observations were combined with laboratory analyses to determine
the appropriate log model for the Meltwater Reservoir. A key observation is that
the clay component within these rocks is dominantly located in framework grains,
not the matrix. It was concluded that, despite the superficial appearance of the
rocks, a shaley-sand log model was not appropriate. Instead, core porosity,
which is total porosity, was matched with porosity logs, and then saturation was
calculated using the standard Archie approach with laboratory-measured "m"
and II n" values. Net pay is then determined by application of cut-offs on
calculated total porosity and water saturation curves. The porosity cut-off is
170/0, based on a cross-plot of core porosity and permeability where 17%
porosity equates to 1 millidarcy rock. A water saturation cut-off of 60% is used.
6
Meltwater Oil Pool RL ~h-estimony
)
March 12, 2001
This value was determined by matching calculated net pay with pay counted
from whole core.
Reservoir Fluids and PVT Properties
Reservoir fluid properties are estimated from fluids recovered during a cased-
hole test of the Meltwater North #1 well. The well was on production for a total of
92 hours. At the end of the test, the well was éNeragi;¡g 3700 BOPD (of 36° API
gravity crude) and 730 SCF/STB at a flowing tubing pressure of 380 psig.
Original reservoir pressure of at the Meltwater #1 well was calculated at
approximately 2400 psig from a pressure build-up test immediately following the
flow test.
Separator gas and separator liquid were physically in a high-pressure cell at
reservoir temperature (135° F). After establishing thermal equilibrium, the
contents were subjected to a constant mass expansion. Following the
expansion, the contents were repressured and a differential vaporization was
performed. Formation volume factor and viscosity values above bubble point
were derived from the constant mass expansion whereas all other fluid
properties were based on the differential vaporization. Results are summarized
below.
Pressure Bo Rs uo
(psig) (Rvb/STB) (SCF/BO) ~
3500 1.32 618 0.85
2500 1.33 618 0.76
2067 1.34 618 0.73
1800 1.31 550 0.75
1600 1.29 501 0.79
1400 1.27 452 0.86
1200 1.25 403 0.96
A corresponding compositional analysis is shown in Exhibit 5.
7
Meltwater Oil Pool ¡ '}s Testimony
)
March 12,2001
Original Oil-in-Place
Original oil-in-place (OOIP) is determined using volumetrics with expected
reservoir parameters. Porosity and water saturation values are calculated from
the Meltwater log model. The formation volume factor is based on results from
the recombined fluid analysis performed on produced fluids from the Meltwater
North #1 well test. Net pay and areal extent estimates are prepared from
seismic maps (in which various seismic attributes are calibrated to the calculated
net pay values for the existing penetrations). OOIP estimates were then chance
weighted to account for gas and water fluid. The resultant Meltwater Sand OOIP
estimates range from 50 to 200 MMBO, with an expected value of 125 MMBO.
The chance-weighted OOIP estimate for the Cairn Sand in the vicinity of the
Meltwater accumulation is 7 MMBO.
8
Meltwater Oil Pool R ) Testimony
')
March 12. 2001
IV. Reservoir Development
Introduction
This portion of the testimony includes a discussion the recovery process
selection and the development and management strategies that are planned to
address uncertainties associated with the Meltwater Reservoir. Discussion is
also presented 011 expected well performance.
Recovery Process Selection
One of the most critical aspects to the Meltwater development plan is the
recovery process. Screening analysis resulted in a decision to initially pursue a
recovery process involving altemating cycles of water and miscible gas (MWAG).
Following are the main reasons for this selection:
1. Numerical simulation indicates that MWAG provides higher recoveries than any
other competing recovery process (Le., primary drainage, waterflood, miscible gas
flood, and lean gas flood). For example, simulation results suggest that an MWAG
process, with a 200/0 cumulative hydrocarbon pore volume slug of injected miscible
gas, would provide an incremental recovery of 9% OOIP compared to a waterflood
process. This modeling work used stochastic reservoir descriptions
(generated from geostatistical techniques) using Tarn analog data.
2. Enriched natural gas used at Kuparuk is miscible with Meltwater fluids at reservoir
conditions. (Henceforth in this document, enriched natural gas will be referred to as
"MI" for Miscible Injectant.) This is supported by slim tube simulation results (Exhibit
6) and is consistent with actual slim tube experiments run on Tam crude. (Given
that the composition of Meltwater and Tam crudes are very similar, they should
behave in a similar fashion from a phase behavior and fluid displacement
standpoint. )
3. GKA MI is currently piped to offset Tam Drill Site 2N and is transportable to
Meltwater for a relatively small premium.
4. Initially pursing MWAG is imperative if this EOR process is to be employed.
Meltwater's MI supply is dependent on existing west-end GKA infrastructure. The
MWAG floods in this part of the GKA are relatively mature. Delaying
implementation of MWAG at Meltwater would therefore jeopardize this project's
EOR reserves, as critical GKA infrastructure may not be available in the future to
transport MI. (Other potential uses of the GKA MI distribution system include de-
bottlenecking productionlinjection lines and providing high pressure lift gas).
9
ì
Meltwater Oil Pool R ) Testimony
)
March 12, 2001
After the cumulative target slug size of MI has been injected into the formation,
pressure support will be maintained with water injection. Current plans are to
eventually inject lean gas into the reservoir to help recover light liquid
hydrocarbons (used to manufacture MI) that will be trapped in the reservoir by
the MWAG process.
Recovery Mechanisms
Initially employing an MWAG recovery process is integral to successfully
developing the Meltwater Reservoir. HO~Never, given that the reservoir
distribution is stratigraphically controlled with localized sand accumulations,
some isolated areas may experience primary depletion. Although remedial
measures (Le., additional drilling and well conversions) will be considered to help
ensure pressure support is maintained, maintaining pressure support may not be
justified in all situations.
Development Approach
The scope of the Meltwater development project involves drilling approximately
26 wells to develop 52 MMBO associated with the 132 MMBO OOIP estimate for
the Bermuda Interval. (Reserve estimates include 2 MMBO from returned MI
solvent and 3 MMBO from chance weighted exploratory targets.) The wells will
be drilled from a single new drill site. Production would be initiated by yearend.
Initial injection support would commence no later than six months after first
production.
Current plans are to develop the Meltwater accumulation primarily through a
continuous development drilling approach (as opposed to phased development).
However, in an effort to reduce risk, a phased drilling approach will be employed
on a regional basis. Specifically, areas with questionable reservoir quality (e.g.,
poor continuity, low permeability, thin pay etc.) will be tested prior to initiating
extensive offset development drilling activities. Well performance data and
improved seismic calibrations acquired from the initial development wells would
guide subsequent drilling plans.
Exploratory drilling targeting the Cairn Interval will be conducted concurrently
with Meltwater development drilling operations. Successful exploratory drilling
results could alter existing plans by (1) changing the location and target interval
of the initial development wells and (2) expanding the scope of the project to
include additional wells. An expanded project scope may involve additional
development drilling phases. An expanded project scope may also involve an
areal and/or vertical expansion of the Meltwater Oil Pool definition.
10
"
Meltwater Oil Pool Rl )Testimony
)
March 12, 2001
Horizontal and/or high angle wells are planned in areas where a facies change is
suspected. The purpose of these wells is to help ensure that adequate injection
and withdrawal points are available. This will help optimize recovery in areas of
potentially poor lateral continuity.
Given the localized sand deposits associated with the Meltwater accumulation, a
relatively high number of wells will likely be sidetracked compared with most
other North Slope fields. The drilling order of the wells will therefore be
optimized to test seismic anomalies along the periphery of the accumulation
while maintaining safer "fallback" locations in the heart of the accumulation.
Prior to spudding a well, sidetrack locations will be identified and included in the
drilling application to help ensure that permitting issues do not interrupt drilling
operations. Ongoing seismic interpretation will be a critical aspect when
delineating the periphery. Relatively low risk well locations will be drilled near
existing penetrations to provide time, when needed, for seismic reinterpretation.
Optimization
Optimizing field development will be an ongoing process requiring addi~ional field
data and reservoir modeling. Work efforts currently planned to optimize total
cumulative MI slug size and MI enrichment.
For screening purposes, a cumulative MI slug size equal to 20% of the
hydrocarbon pore volume (HCPV) was assumed. Optimizing slug size will
require additional simulation work and integrating Kuparuk Large Scale EaR
plans. Further work is also needed to determine the optimum enrichment level.
Slim tube simulation results indicate that Kuparuk MI is richer than needed to
achieve a miscible flood in the Meltwater Oil Pool. (A similar situation exists for
the Tarn Oil Pool.) There remains a possibility that a specialized MI blend for the
Meltwater Oil Pool may be employed (by adding produced gas to the Kuparuk MI
stream).
Plans are to develop the reservoir on nominally a 1 DO-acre well spacing. This
spacing guideline was developed from an economic analysis, which took into
consideration oil rate, cost and recovery impacts associated with various well
spacings. Some portions of the reservoir, however, may require a relatively
dense spacing to address permeability barriers (e.g., faults, mud drapes and
calcite cement) or poorer than expected well (productivity/injectivity)
performance. A 10-acre well spacing is therefore requested to allow a flexible
well placement strategy that will maximize recovery.
Unless optimization studies prove otherwise, plans are to are to inject
approximately 20% HCPVI (46 BCF based on 132 MMBO) of Kuparuk MI.
Reservoir pressure will be maintained to ensure that EaR reserves are not
11
Meltwater Oil Pooll\'~ T estímony
March 12, 2001
compromised during the MWAG process. Well spacing will average close to 100
acres, although some areas may require a much closer spacing to optimize
recovery.
Well Conversion Strategy
Since Meltwater Reservoir distribution is stratigraphically controlled and sand
accumulations are. localized, sand continuity is expected to be difficult to predict.
Producer/Injector interactions will therefore be difficult to predict in the absence
of field data. De\lelopment plans call for minimizing the number of injection wells
until producer/injector interactions are better understood. Producers will be
converted to injection service as necessary in order to provide pressure support
and minimize injection fluid cycling. Hence, to as large of an extent as possible,
plans are to let reservoir performance be a guide in optimizing pattern
configurations.
Simulation work and Tarn analog data suggest that voidage can be maintained
with MWAG at a producer/injector ratio of approximately two. Development
plans are to therefore initially employ a producer/injector ratio of approximately
two and adjust it as needed. As the flood matures (and more producers are
converted to injection service), the producer/injector ratio is expected to decline
to approximately one.
Stimulation Plans
The relatively tight nature of the Meltwater Reservoir coupled with vertical flow
barriers makes producer propped hydraulic fracture stimulations desirable.
Wellbore trajectories, cement and tubulars will be designed to accommodate
hydraulic fracture stimulation techniques.
Plans are to not initially stimulate injection wells. However, if injectivities are
poor or if injection logs indicate significant portions of the reservoir are not
accepting injectant, injectors will be stimulated with high-pressure breakdowns.
An attempt will be made to minimize propped hydraulic fracture stimulations on
injectors as this would complicate future profile modification efforts. Of course,
injectors that were previously produced would have existing propped fractures in
place.
Secondary Targets
The Bermuda Interval will be the primary target of initial development efforts.
Current plans are to focus initial development efforts on that portion of the
interval most likely have good reservoir characteristics. As previously shown on
12
Meltwater Oil Pool RL ITestimony
)
March 12, 2001
Exhibit 1, potentially productive secondary targets in the Cairn Interval may be
encountered during these development efforts. Secondary targets in the Cairn
Interval are expected to generally be within 400' tvd of the Bermuda Interval.
These thin, potentially productive zones contain insufficient reserves to merit
separate wells or extensive completion design modifications. Although fracture
stimulations are planned for Bermuda Interval producers, fracture modeling
indicates these stimulations will only grow approximately 200' upwards.
Potentially productive secondary pay zones can therefore only be developed if
they can be inexpensively commingl~d with Bermuda production.
Given the initial uncertainty of producer/injector interactions, most producers will
be candidates for conversion to injection service. In order to maintain conversion
flexibility, there are no casing design differences between production and
injection wells. (Casing connections will be designed for gas or liquid service.)
The flexibility to convert wells to injection service on an as needed basis is an
integral part of the Meltwater development strategy. This complicates secondary
target development as these targets can only be pursued if they are not isolated
by more than one casing string.
Pursing secondary targets may result in exceeding the AOGCC guideline that
injectors provide annular isolation within 200' measured depth of the highest
perforated interval. Plans are to provide annular isolation within 200' measured
depth of the perforated zone, unless secondary targets are encountered with a
pay thickness approaching or exceeding 10' tvd. Based on current drilling and
facility hook-up plans, the productive nature of these secondary targets can not
be fully ascertained during initial drilling operations. If future evaluations indicate
that developing secondary targets can not be justified, there is the potential of
having either initial or future injectors with annular isolation located more than
200 feet measured depth above the perforated zone. Help from the Commission
is therefore needed to ensure that well service conversion flexibility is not
sacrificed by attempting to pursue thin secondary targets.
Well Peñormance
There is considerable uncertainty in well performance projections. Similar to
Tarn, large variations are expected in well productivities and injectivities.
Meltwater development plans therefore require flexibility to address uncertainties
and performance variations. Typically, Meltwater producers are expected to
have initial average production rates in 2500 BOPO range. The average rate is
expected to gradually decline during the first year of production before stabilizing
at approximately 1500 SOPO/producer.
13
Meltwater Oil Pool R )Testimony
)
March 12, 2001
Artificial Lift
Most Meltwater producers not expected to initially require artificial lift due to a
variety of factors; namely, the absence of produced water, relatively high initial
GaRs (700 - 1500 SCF/B), light oil (360 API gravity crude), pressure support
and the associated insitu gas lift resulting from MI breakthrough. Nevertheless,
nodal calculations and Tarn analog data suggest that artificial lift will be needed
on selective wells; specially, those that are located in low permeability areas or
areas with tortuous injector-to-producer flow paths. Artificial lift will also be
needed after water breakthrough occurs and water cuts begin to rise.
Meltwater completions will include downhole jewelry that will allow the use of
artificial lift, such as hydraulic jet pump, hydraulic piston pumps, lift gas, or
plunger lift systems to be installed as needed. The completion design would
allow hydraulic artificial lift systems to inject power fluid either down the tubing-
casing annulus (with returned fluids flowing up the tubing) or vice-vers~a. Current
hydraulic artificial lift plans are to inject power fluid down the annulus. Lean gas
will not be initially available at Meltwater for lift purposes. Wells will 1)0 unloaded
using either trucked nitrogen or locally available MI for lift gas.
Wells requiring initial artificial lift will either use gas lift (with MI as lift gas) or jet
pumps (with GKA injection water as power fluid). Artificial lift selection will be a
well-by-well decision based on individual well properties and facility optimization.
Low rate wells with paraffin deposition problems will likely involve jet pump lift as
the warm injection water (-120° F) used for power fluid will prevent wellbore
paraffin deposition. However, jet pump lift is not desirable for high rate wells.
This is because high power fluid injection rates cause tubing hydraulic
restrictions. (Typical power fluid/produced fluid ratios for Meltwater producers
will be approximately two.)
As Meltwater matures, gas lift will likely become the dominant artificial lift
mechanism. After target MI slug volumes have been injected, the MI injection
line will be available to carry lift gas from the GKA. The availability of a lean lift
gas source will lower the opportunity cost associated with gas lift. (Using MI as a
lift gas source has a relatively high opportunity cost as the light liquid
hydrocarbons used to enrich the MI could otherwise be sold as oil.) As high rate
wells experience water breakthrough and water cuts subsequently increase,
artificial lift will be required on an increasing number of relatively high rate wells.
As previously mentioned, gas lift is preferable to jet pump lift when lifting high
rate wells due to tubing hydraulics. Other forms of artificial lift, such as electric
submersible pumps, will also be considered as water production rates begin to
rise.
14
Meltwater Oil Pool F\) Testimony
)
March 12, 2001
v. Facilities
Introduction
This portion of the testimony summarizes the injectant sources that will initially
be used at Meltwater. Discussion of the pads, roads, drill site facilities and other
infrastructure is presented below.
General Overview
Meltwater production will be commingled with Tarn and Kuparuk production in
surface facilities prior to final processing and ultimate custody transfer. Sharing
existing production facilities is possible due to existing spare liquid capacity at
Kuparuk's CPF-2 (central processing facility). Economical development is
contingent upon utilization of these facilities. Meltwater will make maximum use
of the existing Kuparuk River Unit (KRU) infrastructure. This maximizes reserves
and minimiz.es the environmental impacts. The Meltwater Special Supplemental
Provisions will govern the corresponding allocation of costs and production to the
working interest owners.
The miscible injectant employed at Meltwater will initially be the same injectant
as that currently used in the Tarn and KRU Large Scale EOR Project. This
injectant is manufactured at Kuparuk's CPF-1 and CPF-2 by blending lean gas
from the KRU's production facilities with solvent (i.e., light hydrocarbon liquid
streams) from the Prudhoe Bay Unit (PBU) and KRU. The light liquid
hydrocarbons from the PBU are NGLs from the Central Gas Facility (CGF). The
light liquid hydrocarbons from the KRU consist of scrubber liquids from artificial
lift gas compression systems at CPF-1 and CPF-2, NGLs from CPF-1 and
naphtha from the Topping Plant.
After completing the MWAG recovery process, plans are to eventually inject lean
gas into the Meltwater Oil Pool to maximize recovery of the light hydrocarbon
liquids that were injected into the reservoir as part of the miscible injectant
stream. The source of the lean gas will likely be Kuparuk River Unit's CPF-2.
However, other potential gas sources will also be considered. (The average
composition of CPF-2 MI and lean gas during 2000 is shown in Exhibit 7.)
KRU CPF-2 oil processing is currently constrained by gas handling limits. The
addition of Meltwater production will exacerbate existing facility limits. Efforts are
currently planned to de-bottleneck CPF-2's gas handling constraints to help
ensure Meltwater production has a minimal impact on KRU production.
15
Meltwater Oil Pool R )Testimony
)
March 12,2001
Pads and Roads
Meltwater development involves the addition of one new drill site to the Greater
Kuparuk Area (GKA), Drill Site 2P, along with required ancillary and support
facilities. Drill Site 2P will be just over ten miles south of existing Tarn Drill Site
2N. The drill site is designed to accommodate a total of 51 wells on 20-foot
centers.
A road connecting the new dlill site to the existing road system is routed from
Drill Site 2N to Drill Site 2P. Four bridges are required along the roadway to
cross small streams.
Pipelines
Cross-country pipelines include a 24-inch common line from Drill Site 2P to KRU
4-Corners, where it ties into the existing common line to CPF-2. The 24-inch line
will also tie into 2N to help debottleneck Tarn surface line hydraulics. A new 12-
inch water injection line will run from: KRU 4-Corners to 2P. The line will run
through and be connected into Tarn Drill Sites 2L and 2N. Finally, an a-inch MI
injection line will run from Drill Site 2N to Drill Site 2P. Pipelines are generally to
be offset from g ravel roads by at least 450 feet. Related construction activities
will be done from an ice road during winter 2000/2001.
Powerlines
Electrical power will be transmitted from Drill Site 2N to Drill Site 2P over new
34.5 kV power lines. The new transmission lines will be installed overhead.
Drill Site Facilities
The design premise for Meltwater facilities is for daily operations to require
minimal operator presence. All data gathering and routine operations are to be
accomplished remotely from CPF 2 and/or a Meltwater drill site control room.
Data gathering is based on Moore Multi-Drop technology, which offers two wire
control for all field instruments.
Facilities to be installed initially at the drill site include:
· Production, test, water injection and MI injection lateral piping and
headers
· Test separator for well testing
· Test loop production heater
· Instrumentation, control, and communication equipment.
16
Meltwater Oil Pool R ) Testimony
)
March 12, 2001
Remote operations include:
· Well testing using a conventional test separator
· Emergency shutdown
· Production choke control
· Injection fluid metering and control
· Gas lift and power fluid control
· Production pressure metering
· Annular pressure monitoring.
Remote well control and testing functions will be performed using the Moore
control system. Well production rate will be controlled using an automated choke
valve. Testing can take place remotely through a divert valve system, which
redirects the flow from the production header to the test.
Emergency Shutdown
Emergency shutdown systems meet API-RP-14C requireFl~nts and PAl
specifications for safety systems. All production, test and water injection piping
is designed to ANSI 1500 psi and will contain the wellhead shut-in pressure up to
the pad emergency shut down (ESD) valves. The MI injection piping will be
designed to ANSI 2500 psi in order to accommodate the injection pressures
needed. (At an expected flowing tubing pressure of 1000 F, ANSI 1500 psi and
ANSI 2500 psi provide working pressure ratings of approximately 3750 psi and
6250 psi, respectively.)
Both production and injection wells can be shut in from over- and under-pressure
through pressure switch signals which close the surface safety valves (SSVs).
Individual wells can also be shut in remotely through the control system. The
entire drill site can be shut in using the pad ESD valves.
17
Meltwater Oil Pool R ) Testimony
)
March 12, 2001
VI. Drilling & Well Design
Introduction
The Testimony below discusses activities related to drilling and completing
Meltwater Oil Pool wells. Discussion is also presented on safety systems, initial
logging plans and completion design advantages.
Ca=sfng & Cementing
Casing and cementing plans for Meltwater wells are consistent with AOGCC
Regulation 20 ACC 25.030. As in KRU wells, conductor casing will be set below
75 feet to provide anchorage and support for the rig diverter assembly. Surface
casing size may be 9-5/8" or 7-5/8", depending on casing setting depth and
produGtion tubing size. Surface casing will be set below the base of the West
Sak interval, effectively casing off the permafrost, Ugnu, and West Sak
formations.
Meltwater wells utilize a tapered casing string tied back to surface, that serves as
the combination production casing / tubing string installation. The casing
adjacent from the producing interval is the same size as the tubing is at the
surface (monobore). The casing across the production interval is then tied back
to surface with a string of 3~" or 4~" tubing inserted into a seal bore or polished
bore receptacle (positioned above the top pay zone perforation.) This provides a
tubing annulus with isolation and pressure integrity (Exhibit 8).
There are three casing programs proposed for the Meltwater development:
Case 1) 31f2 inch Slim hole Monobore completions. This casing program
utilizes a 7-5/8 inch (L-80, 29.7 pound) surface casing string with a
production string of 5~ inch (L-80, 15.5 pound) casing crossed over to
3~ inch (L-80, 9.3 pound) casing across the Meltwater interval. These
monobore wells will be completed with 3~ inch (L-80, 9.3 pound)
production tubing.
Case 2) 41f2 inch Monobore completions. This casing program employs 9-
5/8 inch (L-80, 40 pound) surface casing with 7 inch (L-80 or J-55, 26
pound) production casing crossed over to 4~ inch (L-80, 12.6 pound)
production casing.
18
Meltwater Oil Pool R .) Testimony
)
March 12,2001
Case 3) 3Y2 and 4Y2 inch Conventional completions. This casing program
employs a string of 9-5/8 inch (L-80, 40.0 pound) casing and an
intermediate 7 inch (L-80 or J-55, 26 pound) intermediate casing string
set above the Meltwater formation top. A 3% inch (L-80, 9.3 pound) or
4 % inch (L-80, 12.6 pound) liner would then be set across the
Meltwater formation and tied back to surface with either 3% inch (L-80,
9.3 pound) or 4% inch (L-80, 12.6 pound) production tubing.
Each of these three well types may be completed for either production or
injection service. The service of the well will be determined after logging
operations. Drilling and cornpletion plans for future Meltwater wells may vary
with time as experience and knowledge are gained.
PAl proposes that the Meltwater casing and cementing rules be written as
specified in 20 ACC 25.030 and in accordance with the current Kuparuk River
Field rules as summarized below.
1) For proper anchorage and t:> divert an uncontrolled flow, a conductor casing
shall be set at least 75 feet below the surface and sufficient cement will be
pumped to fill the annulus behind the casing to surface.
2) For proper anchorage, to prevent an uncontrolled flow, and to protect the well
from the effects of permafrost thaw-subsidence and freeze-back, a string of
surface casing will be set at least 500 feet measured depth below the base of
the permafrost section. Sufficient cement shall be pumped to fill the annulus
behind the casing to surface (across the permafrost interval.) If the cement
level in the annulus falls down-hole after the completion of the job, a top job
will be performed.
3) The casing will be designed to withstand the maximum stresses imposed on
it during the life of the well. Casing designs will employ the safety factors
outlined below.
Approved Casing Grades & Connections
Tension design factor = 1.4 or higher
Burst design factor = 1.0 or higher
Collapse design factor = 1.0 or higher
To prevent well failure due to permafrost action, the operator shall install
surface casing including connections, with sufficient strength and flexibility to
prevent failure. The surface casing, including connections, will have
minimum post-yield strain properties of 0.90/0 in tension and 1.26% in
compression.
To be approved for use as surface casing, the Commission shall require
evidence that the proposed casing and connections meet the above
requirement. Several types and grades of casing, with connections, have
been shown to meet the strain properties mentioned above, and have
19
Meltwater Oil Pool F ) Testimony
)
March 12, 2001
previously been approved for use by the Commission (see partial list below).
Other means for maintaining the integrity of the well from the effects of
permafrost thaw-subsidence and freeze-back, based on sound engineering
principles, may be approved by the Commission upon application.
Approved Casing Grades & Connections
7 -5/B" 29.7 ppf LBO BTC
9-5/8" 36 ppf K55 BTC
9-5/B" 40 ppf K55 BTC
9-5/B" 47 ppf LBO BTe
4) Intermediate casing may not be required and that proposed Meltwater well
designs Case 1 and Case 2 (utilizing conductor, surface and production
casing) be allowed. However, intermediate casing may be used (Case 3)
where either dictated by hole problems or in preparation to drill an over-
pressured zone.
5) In addition to conventional cased and perforated completions, the following
alternative completion methods:
a) Open hole completions provided that the casing is $et not more than 200
feet above the uppermost oil bearing zone
b) Slotted liners, wire-wrapped screen liners, or combination thereof, landed
inside of cased or open hole -
c) Horizontal completion with liners, slotted liners, wire-wrapped screens, or
combination thereof, landed inside the horizontal extension or open hole
d) Multi-lateral type completions in which more than one well bore
penetration is completed in a single well, with production gathered and
routed back to a central well bore.
6) The Commission may approve other completion methods upon application
and presentation of data showing the alternatives are based on sound
engineering principles.
Although the standard program incorporates maintaining a tubing annulus with
isolation and pressure integrity within 200' of the initial producing interval, as
previously discussed, exceptions to this design criterion will be required to
optimize recovery from potentially productive secondary targets.
Blowout Prevention
PAl proposes that the rule for blowout prevention in the Meltwater Oil Pool be
written identically to the provisions established in Regulation 20 ACC 25.035
20
Meltwater Oil Pool R ) Testimony
}
March 12,2001
(Secondary Well Control: Blowout Prevention Equipment Requirements) of the
AOGCC regulations. Except as modified by the AOGCC regulations, blowout
prevention equipment and its use will be in accordance with API Recommended
Practice 53 for blowout prevention systems.
Drilling Fluids
The drilling fluid program for Meltwater Wells will be prepared and implemented
in full compliance with 20 AAC 25.033 in the AOGCC regulations. Good.
engineering practices, offset well data and continuous monitoring of the mud
system will be utilized to ensure well control during drilling operations. Formatiop
pressure data for the strata to be penetrated is known and documented based
on the three Meltwater reservoir penetrations during the exploration phase.
Annular Disposal of DrillinQ Wastes
Meltwater development will utilize the practice of annulus pumping of fluids
incidental to well drilling activities. Fluids will be pumped down an adjacent
annulus. Cuttings will either be ground and injected with the fluid, or separated
and transported to a permitted disposal facility. Annulus pumping will be
performed in accordance with 20 AAC 25.080.
Fluids permitted for disposal include, but are not limited to:
· Waste drilling fluids
· Drill cuttings ground into slurry form
· Excess rig washdown water
· Excess cement returns from casing and cementing operations
· Cement rinseate fluids generated from cementing operations incidental to
drilling the wells
· Cement contaminated drilling fluids
· Completion fluids
· Formation fluids
· Reserve pit fluids
· Drill rig domestic waste water
· Other substances that the Commission determines are wastes associated
with the drilling of a well.
Disposal of such wastes in existing I or future, permitted North Slope Class II
injection wells is also a possibility, and will be employed at operator discretion.
21
Meltwater Oil Pool F ) Testimony
')
March 12, 2001
Wellhead and Production Tree Design
Meltwater wellhead and production tree designs will be similar to those employed
at Kuparuk. All wellhead and production tree equipment carries the API
monogram and meets or exceeds API RP 14C.
Directional Drilling
MWD surveys will be used for directional drilling operations. Continuous MWD
surveys have proven to be as reliable and accurate as gyro surveys on the North
Slope and will be used as the definitive survey.
TubinQ I Casing Annulus Mechanical Integrity
Both proposed Meltwater injector and producing wells will have an annulus and
seal bore I polished bore receptacle as part of their design, PAl will have the
capability to pressure test the tubing I casing annulus to periodically verify the
well's mechanical integrity. The casing testing method for Meltwater wells will
comply with the requirements of 20 AAC 25.412 (c). Sufficient notice of pressure
tests will be given so that a Commission representative may witness the test.
Subsurface Safety Valves
Consistent with statewide AOGCC regulations (20 MC 25.265) and current KRU
Field Practice (as modified by Conservation Order 348), there is no apparent
need for surface controlled sub-surface safety valves (SSSVs) in Meltwater
wells. In keeping with Kuparuk guidelines, velocity sensitive subsurface valves
(e.g., "K Valves") may be set wells with very high potential production rates.
Surface Safety Valves
Surface safety valves (SSVs) are included in the wellhead equipment. As
previously mentioned, these devices can be activated by high and low pressure
sensing equipment and are designed to isolate well fluids upstream of the SSV
should pressure limits be exceeded. Testing of SSVs will be similar to the
practice in Kuparuk formation producing wells.
22
Meltwater Oil Pool Rl )Testimony
)
March 12,2001
Logging Operations
The minimum log suite planned for Meltwater includes gamma ray and resistivity
measurements obtained from the surface casing shoe to well TO. In addition,
density and neutron logs may be utilized across this interval in selected wells.
These logs will be obtained from MWO/LWO tools positioned in the drilling
bottom-hole assembly.
Well Design
Profile modification and control of thief zones will be primarily managed by
controlling fluid injection in offset injection wells. Profile modification in this
reservoir management scenario is greatly facilitated by the monobore injector
designs that allow mechanical patches to be run on wireline and selectively
placed across discrete perforation sets.
23
Meltwater Oil Pool R ')Testimony
)
March 12,2001
VII. Reservoir Surveillance
Introduction
This section provides testimony regarding reservoir surveillance and operations
during production anomalies.
Reservoir Pressure Measurements
Pressures will be reported at a common datum of 5400' true vertical depth
subsea. An initial pressure survey will be acquired for each well prior to
establishing regular production or injection. On an annual basis, the minimum
number of bottom-hole pressure measurements will be equal to the number of
governmental sections included in the pool. PAl asks the Commission to giv(~
the operator more flexibility to collect pressure data in areas of special interest,
as opposed to specified geographical areas based on governmental section.
Allowable pressure survey techniques should include wireline RFT
measurements, pressure buildups with bottom-hole pressure measurement,
injector surface pressure falloffs, static bottom-hole pressure surveys following
extended shut in periods, or bottom-hole pressures calculated from well head
pressure and fluid level in the tubing of an injector which has been shut in a
minimum of 48 hours. Pressure survey data would be reported to the
Commission quarterly.
Surveillance Logs
Hydraulic propped fracture stimulations will limit the usefulness of production and
injection logs. Surveillance logging will be used to monitor injection in wells that
have not previously stimulated with hydraulic propped fracture stimulations. In
addition, surveillance logs may also be employed when more than one zone is
open in a single wellbore (e.g., wells with secondary targets).
Fluid Samplinq
Gas and/or liquid sampling will be periodically conducted during well tests during
the miscible injection period of the flood. Compositional analyses will be
performed on the samples to help gauge the effectiveness of the miscible flood.
24
Meltwater Oil Pool R ) Testimony
)
March 12,2001
GOR Determination
Gas-oil ratios (GaRs) will be routinely measured during well test operations.
Despite concurrent production and injection, the relatively tight nature of the
Meltwater reservoir coupled with a high solution gas content will cause primary
depletion effects to increase initial gas production. This may cause GaRs to
exceed limits set forth in 20 MC 25.240(b). Moreover, gas breakthrough from
MI and/or lean gas injection will also cause GaR measurements to exceed these
limits. An exception to 20 MC 25.240(b) is therefore requested.
Production Allocation and Well Testing
Reservoir management and surveillance requires accurate production data. A
conventional test separator will be employed to help ensure these requirements
are met.
Liquid mass flow will be measured using a Micro Motion meter, water cut will be
measured using a Phase Dynamics meter, and gas flow will be measured using
orifice meters. The conventional test separator and associated meters are
essentially the same test equipment employed at Kuparuk. One key difference,
however, is that level controls will be placed on the liquid and gas legs of the
Meltwater test separator. Test system pressure drop will ranges from 5 to 23 psi,
with most wells closer to the 5 psi value. With a low back-pressure imposed by
the metering equipment and a small flush volume (approximately 20 barrels), the
time required to displace the previous well's fluids is short, minimizing
stabilization time. Since low flow rate variance is anticipated, relatively short well
tests should be operationally practical and accurate. Meltwater test equipment
will also include a heater upstream of the separator to help ensure paraffin
deposition does not interfere with well test accuracy.
A test frequency of at least two well tests per month for each Meltwater producer
is planned. Variance analyses techniques will be employed to identify wells that
may benefit from a more frequent testing schedule. Additional testing will be
conducted as needed to ensure that well tests accurately represent production
rates. Hence, Meltwater producers will generally be tested more frequently than
Kuparuk producers (which are required to be tested at least once per month).
Although Meltwater well tests will occur more frequently than those at Kuparuk,
the Meltwater tests will be included with Kuparuk wells tests and other satellites
to determine overall allocation factors used for revenue and accounting
purposes. However, the Satellite Produced Oil Allocation Factor, which will be
applied to Meltwater, reverts to 1.00000 if the calculated GKA Produced Oil
Allocation Factor exceeds 1.02000. Allocation factor calculations are detailed in
Exhibit 9.
25
Meltwater Oil Pool R )Testimony
)
March 12,2001
Production Anomalies
Production prorations at or from Kuparuk facilities will affect all commingled
reservoirs produced through the facilities by an equivalent percentage of oil
production, unless this will result in either surface or subsurface equipment
damage, or increased operating costs. One potential operating cost concern
particular to Meltwater is paraffin deposition. A severe reduction in production
through the Meltwater flow line could cause paraffin deposition if ambient
temperatures are low.
26
Meltwater Oil Pool R )Testimony
)
March 12,2001
VIII. Summary of Testimony
The Meltwater working interest owners are first and foremost committed to a safe
and environmentally sound operation. The proposed drilling program meets or
exceeds all requirements specified in the Commission's rules and regulations.
Meltwater facilities are designed to operate safely and efficiently. All well and
facility designs meet or exceed the standards specified by state or national
codes, the recommended practices of the relevant advisory organizations, and/or
the time-proven practices of prudent operators. Plans are to make rnaximum
use of the existing KRU infrastructure, thus minimizing environmental impacts
while maximizing reserves for the Greater Kuparuk Area.
Developing the Meltwater Oil Pool presents many challenges. The reservoir is
relatively tight and injector/producer interactions are expected to be impeded by
tortuous flow paths. The localized nature of the sand accumulations coupled
with multiple Meltwater Reservoir horizons will complicate development efforts.
Develop plans, which include ongoing seismic reinterpretation, 5idetrack
planning, regionally phased development and minimizing the initial number of
injectors until well interactions are better understood, should help addrE:ss these
challenges. A key element of the development plan is initially employing a
tertiary recovery process. Reservoir studies support using an MWAG process to
maximize recovery. Delaying the tertiary recovery process would jeopardize
Meltwater reserves as critical GKA MI distribution infrastructure may not be
available in the future. The flood will be operated with the intent of exercising the
majority of flood control at the injectors.
To facilitate Meltwater Oil Pool development, exceptions to state wide
regulations are requested for well spacing (MC 25.055{a}) and GaR production
limits (MC 25.240{b}). Initial development plans call for 100 acre well spacing,
however, 10 acre well spacing is requested to allow for flexibility in adjusting for
reservoir heterogeneities (i.e., sand discontinuities, permeability barriers, etc.).
No GaR production limits are requested because of plans to initially employ an
MWAG recovery process.
Maximizing recovery from the Meltwater Reservoir will require a collaborative
effort between the Commission and the working interest owners. Pursuing
potentially productive secondary pay zones within the reservoir may result in
some injectors having annular isolation more than 200' above the top
perforation.
An ongoing reservoir surveillance program coupled with development drilling
results and additional reservoir modeling studies will be used to help optimize the
flood. As additional information is gained, fully developing this resource may
involve an areal and/or vertical expansion of the Meltwater Oil Pool definition.
27
Meltwater Oil Pool R )TestimOny
)
March 12,2001
Special emphasis has been placed on well testing because Meltwater production
will be commingled with KRU production in surface facilities prior to final
processing. A test system that operates as close to producing conditions as
possible will be employed to ensure accurate well tests. A minimum of two well
tests per month will be obtained. All volumes and tests will be summarized and
reported to the Commission on a monthly basis.
The development of the Meltwater resource is made possible through the
sharing of the sxisting KRU infrastructure.
PAl looks forward to working through the challenges of developing the Meltwater
Oil Pool. Successfully developing this accumulation will provide additional
infrastructure and insight that will be of value to other potential satellite
development opportunities.
Thank you for tt,e opportunity to present this testimony.
28
Meltwater Oil Pool RL}restimony
)
March 12, 2001
IX. Proposed Meltwater Field Rules
Rule 1. Field and Pool Name
The field is the Kuparuk River Field and the pool is the Meltwater Oil Pool.
Rule 2. Pool Definition
The Meltwater Oil Pool is defined as the accumulation of hydrocarbons common
to and correlating with the interval between 5187' and 5297' tvd subsea in the
Meltwater North #2A well
Rule 3. Spacing Units
Nominal spacing units within the pool wm be 10 acres. The pool shall not be
opened in any well closer to 300 feet to an external boundary where ownership
changes.
Rule 4. Casing and Cementing Practices
(a) Conductor casing will be set at least 75 feet below ground level and
cemented to surface.
(b) Where required for annular disposal, surface casing will be set at least 500
feet below the permafrost and be cemented to surface.
Rule 5. Injection Well Completion
(a) Wells may be employed for injection service provided a sealbore, packer, or
other isolation device is positioned not over 200 feet above the top
perforated interval.
(b) Exceptions to Rule 5(a) will be permitted in cases where the distance
between annular isolation and the top perforated zone exceeds 200 feet
measured depth due to pursuit of secondary targets within the Meltwater
Reservoir.
29
Meltwater Oil Pool RLJrestimony
)
March 12, 2001
Rule 6. Automatic Shut-in Equipment
(a) All wells capable of unassisted flow of hydrocarbons will be equipped with
a fail-safe automatic surface safety valve.
(b) Injection wells will be equipped with a fail-safe automatic surface safety
valve.
(c) Surface safety valves will be tested at six-month intervals.
Rule 7. Common Production Facilities and Surface Commingling
(a) Production from the Meltwater Oil Pool may be commingled with
production from the Kuparuk River Oil Pool and/or other oil pools in the
KRU in surface facilities prior to custody transfer.
(b) The allocation factor for the Meltwater Oil Pool will be equal to the Kuparuk
allocation factor, except in cases where the Kuparuk oil all·)cation factor
exceeds 1.05. Under these circumstances the Meltwater oil allocation
factor will limited to 1.05.
(c) Each producing Meltwater well will be tested a minimum of two times per
month during the first year of regular production.
(d) The operator shall submit monthly file(s) containing daily allocation data
and daily test data for agency surveillance and evaluation. '
Rule 8. Reservoir Pressure MonitorinR
(a) An initial pressure survey shall be taken in each well prior to establishing
regular production or injection.
(b) The minimum total number of bottom-hole pressure surveys measured
annually will be equal to the number of producing or injecting governmental
sections within the pool. Bottom-hole surveys as outlined in Rule 8(a) may
fulfill the minimum requirement.
(c) The reservoir pressure datum will be 5400' subsea.
(d) Pressure surveys may consist of stabilized static pressure measurements
at bottom-hole or extrapolated from surface, pressure fall-off, pressure
buildup, multi-rate tests, drill stem tests, and open-hole formation tests.
(e) Data and results from pressure surveys shall be reported quarterly on
Form 10-412, Reservoir Pressure Report.
(f) Results and data from special reservoir pressure monitoring tests shall
also be submitted in accordance with part (e) of this rule.
30
Meltwater Oil Pool F ) Testimony
)
March 12, 2001
Rule 9. Gas-Oil Ratio Exemption
Wells producing from the Meltwater Oil Pool are exempt from the gas-oil ratio
limit set forth in 20 MC 25.240(b).
Rule 10. Pressure Maintenance Project
Injection for pressure maintenance and enhanced oil recovery will commence
within six months after the start of regular production from the Meltwater Oil Pool.
Rule 11. Reservoir Surveillance Report
A surveillance report will be required after one year of regular production and
annually thereafter. The report shall include but is not limited to the following:
(a) Progress of enhanced recovery project(s) implementation and reservoir
maqagement summary including engineering and geotechnical
parameters.
(b) Summary of produced and injected fluids by producing interval.
(c) Summary of reservoir pressure analyses within the pool.
(d) Results from any productionlinjection logs when more than one interval is
commingled within a single wellbore.
(e) Results of any special monitoring.
(f) Future development plans.
Rule 12. Production Anomalies
In the event of oil production capacity proration at or from the Kuparuk facilities,
all commingled reservoirs produced through the Kuparuk facilities will be
prorated by an equivalent percentage of oil production, unless this will result in
either surface or subsurface equipment damage, or increased operating costs.
Rule 13. Administrative Action
Upon proper application, the Commission may administratively waive the
requirements of any rule stated above or administratively amend the order as
long as the change does not promote waste, jeopardize correlative rights, and is
based on sound engineering principles.
31
Meltwater Oil Pool Rl )restimony
)
March 12,2001
x. Proposed Findings & Conclusions
Phillips Alaska, Inc., as the Meltwater Oil Pool operator, respectfully proposes
that the Commission make the following findings.
1. Initial development plans include approximately 26 wells, with
approximately three fourth of the wells being drilled during 2001 and the
remaining wells being drilled during 2002.
2. The total number of wells included in the project for full development will be
better understood after initial development drilling and production/injection
data help address some of the uncertainties associated with reservoir
extent and sand continuity.
3. Pursuit of thin, potentially prodL:ctive secondary targets within the Meltwater
Oil Pool may result in annular isolation occurring more than 200' measured
depth above the top of the pertÖrated interval.
4. Injection into the Meltwater Oil Pool is scheduled to commence during late
2001 as facilities and wells associated with the project are brought on-line.
5. Meltwater development is dependent on GKA infrastructure.
6. Initially pursing an MWAG recovery mechanism at Meltwater helps ensure
reserves are maximized. Delaying the implementation of this process
jeopardizes EaR reserves, as critical GKA infrastructure may not be
available in the future to transport MI to Meltwater.
Recommended Conclusions
Phillips Alaska, Inc., as the Meltwater Oil Pool operator, respectfully requests
that the Commission make the following conclusions.
1. The Meltwater Development plan, which initially employs an MWAG
process, involves the application of a tertiary enhanced oil recovery method
in accordance with sound engineering principles.
2. The use of an MWAG process is reasonably expected to result in more than
an insignificant increase in the amount of crude oil that ultimately will be
recovered.
32
Meltwater Oil Pool Rl )Testimony
)
March 12,2001
Requested Decisions
Phillips Alaska, Inc., as the Meltwater Oil Pool operator, respectfully requests
that the Commission endorse an initial MWAG process for field development.
33
')
Meltwater Oil Pool R )Testimony
Exhibit 1
Exhibit 2
Exhibit 3
Exhibit 4
Exhibit 5
Exhibit 6
Exhibit 7
Exhibit 8
Exhibit 9
March 12, 2001
LIST OF EXHIBITS
Type Section of the Meltwater Reservoir
Meltwater Pool Area and Interval Trends
Top of Bermuda (T3) Structure Map
Top of Cairn (T4) Structure Map
Crude Composition Analysis
Meltwater Slim Tube Simulation Results
Composition of CPF-2 MI & Lean Gas
Meltwater Completion Designs
Satellite Allocation Technique
34
EXHIBIT 1
Type Section of the Meltwater Reservoir
MELTWATER NORTH 2A
EXHIBIT 2
Meltwater Pool Area and Interval Trends
EXHIBIT 3
Top of Bermuda (T3) Structure Map
- -
MELTWATER NORTH TOP BERMUDA (T3)
DEPTH STRUCTURE MAP
EXHIBIT 4
Top of Cairn (T4) Structure Map
.
.
EXHIBIT 5
Crude Composition Analysis
Sample:
Primary Stage Separator Liquid from Meltwater North #1 Test
Sampling Conditions: 150 psig & 85° F
Analysis Method:
Low Temperature Distillation / Programmed-Temperature, Capillary
Chromatography
ComDonent
Hydrogen Sulfide
Carbon Dioxide
Nitrogen
Methane
Ethane
Propane
Iso-Butane
n-Butane
iso-Pentane
n-Pentane
Hexanes
Heptanes
Octanes
Nonanes
Decanes
Undecanes
Dodecanes
Tridecanes
Tetradecanes
Pentadecanes
Hexadecanes
Heptadecanes
Octadecanes
Nonadecanes
Eicosanes
Heneicosanes
Docosanes
Tricosanes
T etracosanes
Pentacosanes
Hexacosanes
Heptacosanes
Octacosanes
Nonacosanes
Triacontanes
Hentriacontanes
Dotriacontanes
Tritriacontanes
T etratriacontanes
Pentatriacontanes
Hexatriacontanes plus
Mole %
0.00
0.02
0.00
3.65
2.10
5.77
1.68
5.29
2.12
3.88
8.52
5.81
9.17
6.22
5.34
4.17
3.57
3.59
3.01
2.77
2.10
1.94
1.93
1.66
1.41
1.22
1.17
1.06
0.97
0.93
0.80
0.69
0.66
0.63
0.57
0.52
0.42
0.43
0.37
0.30
3.54
Weiaht %
0.00
0.01
0.00
0.34
0.37
1.48
0.57
1.78
0.89
1.62
4.15
3.23
5.69
4.36
4.15
3.55
3.33
3.64
3.32
3.31
2.70
2.67
2.81
2.53
2.25
2.06
2.07
1.95
1.86
1.86
1.67
1.50
1.49
1.47
1.38
1.30
1.08
1.14
1.01
0.85
18.56
EXHIBIT 6
Meltwater Slim Tube Simulation Results
:::- 95
c..
l-
e"!
.....
@ 90
>-
...
(¡
>
0
(J
(¡ 85
c:
Õ
Meltwater Slim Tube Simulation Results
(Injection Fluid is Kuparuk MI - run at 1
100
n u ~
..
u
..
4Þ
80
2050 2100 2150 2200 2250 2300 2350 2400 2450
Slim Tube Operating Pressure
.
.
EXHIBIT 7
Composition of Miscible Injectant &
Lean Gas Supplied by
the Kuparuk River Unit's CPF-2
Component MI Lean Gas
(Mole %) (Mole %)
CO2 0.89 0.5
N2 0.27 0.3
Cl 81.37 69.6
C2 8.79 6.7
C3 5.10 5.0
i-C4 0.92 2.2
n-C4 1.99 6.3
i-CS 0.30 2.0
n-Cs 0.28 2.5
C6 0.07 2.1
C7 0.01 1.8
CS+ 0.00 1.0
.
.
EXHIBIT 8
Meltwater Completions Designs
FMC Prudhoe Gen V
9-518 x 5% x 3%
2.875" CAMCO
OS nipple for
Possible K-Valve
9-7/8" Hole
7-518" Surface Casing
at 2,500' TVD
63,.(¡"Hole
Baker CMU Sliding
Sleeve wl2.813" OS
Cameo profile
Cameo 3W' x 1"
side pocket GLM
5V2" Casing
Sea] Receptacle
(CSR)
Crossed over to
3'1i' tubing
at 5.000' TVD
3-112" Stirnhole Monobore
Completion
3·1/2" or 4·112"
Monobore Completion
FMC Prudhoe Gen V
9-518 x 7 x 4%
Base of
pennafrost
at 1,250' MD
1214" Hole
Base of
West Sak
at 1,800' TVD
9·5/8" Surf. Csg.
at 2,500' TVD
JI/2" tubing
31/i' or 41/2"
81f2"Hole
CAMCO 2.75"
OS nipple
7" Casing
Seal Receptacle
(CSR)
Crossed over to
4Vz" c"$ing
at 5.000' TVD
Production Casing
at 5.200' TVD
·
,
EXHIBIT 9
Satellite Allocation Technique
General Allocation Factor = Actual Volume
Theoretical Volume
Produced Oil Allocation
GKA Oil Allocation Factor
= [CT Vol + KRUTP Diesel Vol- Load Diesel Vol- Exploration Vol + Delta Divert Tank Vol]
[Kuparuk Well Test Oil Vol + Satellite Well Test Oil Vol]
If GKA Produced Oil Allocation Factor < 1.02000,
GKA Produced Oil Allocation Factor - = Satellite Produced Oil Allocation Factor
= Kuparuk Produced Oil Allocation Factor
If GKA Produced Oil Allocation Factor> 1.02000,
Satellite Oil Allocation Factor = 1.00000
Kuparuk Produced Oil Allocation Factor
= [CT Vol + KRUTP Diesel Vol - LoadDiesel Vol - Exploration Vol + Delta Divert Tank Vol
- Satellite Well Test Oil Vol] + [Kuparuk Well Test Oil Vol]
Produced Water Allocation
GKA Produced Water Allocation Factor = Satellite Produced Water Allocation Factor
= Kuparuk Produced Water Allocation Factor
= GKA Injected Water Vol - Seawater Injected Vol
(Kuparuk Well Test Water Vol + Satellite Well Test Water Vol)
Produced Gas Allocation
GKA Produced Gas Allocation Factor = Satellite Produced Gas Allocation Factor
= Kuparuk Produced Gas Allocation Factor
= GKA Injected Gas Vol + Kuparuk NGLs + Fuel + Flare
(Kuparuk Well Test Gas Vol + Satellite Well Test Water Vol
achment 1 A
Net Pay Map with Planned Wells
Meltw t r Bermu
Interv I et Pay a
F'L AN N ED
PROOJCffi
IIIIJEt.'f(JR
INTERV AL '.'JELLS
PRC!)I.JCffi
IIIIJEC:1CR
I NTE 11\1 AL WE LLS
Meltwater Area
Order
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