Department of Commerce, Community, and Economic Development
Alaska Oil and Gas Conservation Commission
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HomeMy WebLinkAboutCO 341 DINDEX CONSERVATION ORDER NO. 341D
Prudhoe Oil Pool
Prudhoe Bay Field
1.
September 21, 2001
Letter from BPXA regarding Gas Cap Water Project
(portions held confidential)
2.
September 29 2001
Notice of Public Hearing, Affidavit of Publication,
mailings
3.
October 18, 2001
BSI GCWI Questions
4.
October 30, 2001
BPXA's pre -filed testimony, sign -in sheet
5.
October 30, 2001
Transcript
6.
November 1, 2001
BPXA's submittal of additional information from hearing
Testimony
7.
November 30, 2001
BPXA's letter of non -objection
8.
--------------------
PBU Annual Surveillance Reporting Requirements
9.
November 9, 2005
BPXA, CPAI, and Exxon Gas Cap Water Injection
Presentation (held confidential)
10.
April 29, 2009
BPXA's letter and results of the collected surveillance
data from the commingled production from Aurora Oil
Pool and PBU (oil tracers held confidential)
11.
May 24, 2011
Alaska Gasline Development Corp letter regarding Gas
Off -Take For Instate Gas Pipeline
12.
June 27, 2011
AOGCC letter regarding Gas Off -Take For Instate Gas
Pipeline
13.
September 30, 2013
BPXA letter regarding discovered lapse in reporting
requirements
14.
March 31, 2014
BPXA's report regarding commingled production for well
S-26
INDEX CONSERVATION ORDER NO. 341D
.
.
STATE OF ALASKA
ALASKA OIL AND GAS CONSERVATION COMMISSION
333 West 7th Avenue, Suite 100
Anchorage Alaska 99501
Re: THE APPLICATION OF BP
EXPLORATION (ALASKA) INC.
Prudhoe Oil Pool- Modification to
pool rules - Conservation Order
34lC, for injection of water into the
Prudhoe Bay Gas Cap
IT APPEARING THAT:
) Conservation Order 341D
)
) Prudhoe Oil Pool
) Prudhoe Bay Field
)
)
) November 30,2001
1. By letter dated September 21, 2001, BP Exploration (Alaska), Inc. ("BPXA") on
behalf of the Working Interest Owners ("WIOs") of the Initial Participating Areas of
the Prudhoe Bay Unit ("PBU") has applied for a modification of certain rules of
Conservation Order 341 C ("CO 341 C") in conjunction with a proposed project
named the Gas Cap Water Injection Project ("GCWI").
2. The Commission published notice of opportunity for public hearing in the Anchorage
Daily News on September 29,2001.
3. The Commission held a public hearing October 30,2001 at 9:00 am at the Alaska Oil
and Gas Conservation Commission at 333 West ih Avenue, Suite 100, Anchorage,
Alaska 99501.
4. The Commission received no protests to BPXA's application or to the public
testimony.
5. Pre-filed testimony of representatives of BP Exploration (Alaska), Inc., Phillips
Alaska, Inc. and ExxonMobil Production Company is included in the record (revised
October 30, 2001). All additional information requested by the Commission at the
hearing was received November 1,2001 and November 6,2001.
FINDINGS:
1. Authority 20 AAC 25.520. 20 AAC 25.540
Commission regulation 20 AAC 25.420 provides authority to issue orders prescribing
rules to govern the proposed development and operation of a pool. The commission
will, in its discretion, amend pool orders in accordance with procedures set forth in 20
AC 25.540.
CO 341D
November 30,2001
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Page 2
2. Gas Cap Water Injection Project - Overview
Currently, reservoir pressure is declining at 25 to 35 psi/year. The WIOs have studied
options to mitigate pressure decline and have annually reported the progress of these
studies to the Commission, based upon rulings in CO 290 (2/21/92), which were
incorporated into CO 341C, Rule 12(d). As a result of these studies, the WIOs
sanctioned the Gas Cap Water Injection project in June 2001. This project represents
a new element in the depletion strategy of the Prudhoe Bay Oil Pool with the dual
goals to mitigate reservoir pressure decline and improve recovery.
3. Proposed Modifications to Conservation Order 341C
The most current rules governing Prudhoe Bay Field, Prudhoe Oil Pool are contained
in CO 341C, dated June 12, 1997. CO 341C is a consolidation of all conservation
orders in effect for the Prudhoe Bay Field, Prudhoe Oil Pool at that point in time.
Specific to CO 341C, BPXA is requesting the following modifications:
a) Revoke paragraph (d) of Rule 12 that requires the Operator to continue to
investigate options to mitigate pressure decline and to provide an annual
report to the Commission. With the implementation of GCWI, BPXA claims
pressure decline will be mitigated.
b) Modification of Paragraph (c) in Rule 12 which currently provides that the
Operator maintain a pressure differential of at least 250 psi between the
minimum miscibility pressure of the miscible injectant and the prevailing
reservoir pressure. BPXA claims that as GCWI will mitigate pressure decline,
a more appropriate pressure differential of 100 psi is appropriate and will
allow BPXA to better optimize both the composition and volume of the
miscible injectant.
c) Modification of Rule 11, which describes the Prudhoe Oil Pool surveillance
report, to include the results of GCWI surveillance.
4. GCWI Project Overview
The project scope calls for ramping up to 650,000 barrels per day of seawater
injection into the eastern portion of the gas cap from a new injection site located at
the East Dock Staging Pad. Initial projected rates are 500,000 barrels per day. Water
injection will increase over time with increased availability of seawater and decreased
seawater demand in other projects, such as the Flow Station 2 and Point McIntyre
waterfloods and Grind and Inject. Water injection is anticipated to continue for
twenty years, with a final injected water volume of near four billion barrels.
Increased hydrocarbon recovery of 150-200 million barrels is projected by BPXA.
a) Facilities Requirements
Facility construction is planned for this winter, followed by start-up of injection in
mid 2002. To implement the Gas Cap Water Injection project, a new seawater
CO 341D
November 30, 2001
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Page 3
pipeline from Flow Station 2 to the East Dock Staging Pad will be constructed.
The new line will have a 32" diameter and a total length of approximately 18,000
feet. It will tie-in to the existing 32"seawater line running from the Eastern
Seawater Injection Plant to Flow Station 2. A heated pig receiver/manifold
module and well houses will be installed at the East Dock Staging Pad to
accommodate five to seven new injection wells.
b) GCWI Well Locations
Current plans for the GCWI include drilling of up to seven water injection wells
into the eastern portion of the PBU, Ivishak formation gas cap. BPXA indicates
the well locations were strategically chosen to allow for sufficient Ivishak pay at
the bottom hole locations of the injectors, while maintaining sufficient distance
from the gas injection and oil producing areas.
c) GCWI Well Completion
Each gas cap water injector will be completed with 13 3/8" surface casing
cemented to surface, 9 5/8" intermediate casing with cement brought to 1000'
above the shoe, and a fully cemented 7" injection liner. The tubing will be 7 5/8"
and will include a 7" subsurface safety valve and two 7" profiles. The tubing is
large to accommodate the high volume of water to be injected. The tubing will
also be plastic coated to help minimize the friction losses. Average surface
pressure for these new injection wells will be approximately 2700 psi. Maximum
injection pressure is expected to be approximately 3100 psi.
5. Project Benefits
a) Reservoir Pressure
Average reservoir pressure in the Prudhoe Bay field is declining at a rate of 25-35
psi/year. The declining pressure reduces efficiency of every recovery mechanism
operating in the field. The GCWI project is designed to arrest pressure decline
and maintain the reservoir pressure until water injection ends in 2022. Current
average reservoir pressure is approximately 3450 psi (@ 8800' ss datum).
b) Reservoir Simulation of Recovery
The GCWI incremental oil recovery was predicted using BPXA's Full Field
Compositional Reservoir Model, comprised of a sixty (60) acre areal grid of the
Prudhoe Bay field. It includes the oil that initially was in the gas cap and is
immobile. The recovery calculated by the full field model was validated using
mechanistic studies of GCWI using fully compositionallD, 2D, strip, and pattern
models. The increased pressure resulting from GCWI improves every recovery
mechanism operating in the field. The benefits are characterized for three regions
of the field; Gas Cap, Gravity Drainage, and WaterfloodlEOR.
The incremental net additional recovery from GCWI is approximately 200 MMB
in the full field model. The total reflects a reduction of 20 MMB in the Gas Cap
region with increases of 200 MMB in the Gravity Drainage region, and 20 MMB
in the waterfloodlEOR region.
CO 341D
November 30, 2001
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Page 4
(1) Gas Cap Area
In total, there is a net reserves reduction of about 20 MMB in the Gas Cap
region. In the original gas cap, not invaded by water, BPXA projects 30
MMB additional reserves from vaporization of residual oil and retrograde
condensate. In the water invaded area, some hydrocarbon liquids will be
trapped and remain immobile to injected water, preventing vaporization by
injected gas, which reduces liquid recovery by approximately 50 MMB.
(2) Gravity Drainage Area
BPXA projects improved vaporization and gravity drainage processes will
yield about 200 MMB of incremental recovery from the Gravity Drainage
region. Vaporization of residual oil and retrograde condensate by the
injected gas is more efficient at higher pressure. Higher reservoir pressure
reduces oil shrinkage and oil viscosity. Both of these effects increase oil
mobility and result in more efficient gravity drainage.
(3) Waterflood and EOR Area
The waterflood/EOR benefits are approximately 20 MMB. The projected
benefits result from: I) higher reservoir pressure increasing well
production capacity; 2) lowered oil shrinkage; and 3) the higher reservoir
pressure allowing leaner miscible injectant, thus greater supply, leading to
more EOR recovery.
6. Water Movement
The potential for water to interfere with the various recovery mechanisms has been
extensively studied by the WIOs. In particular, the potential for water to finger
through the gas cap, and interfere with the gravity drainage area was a prime concern.
WIO studies showed that because gas is 100 times more mobile than the water that
displaces it, a piston-like displacement is anticipated. Water saturations in simulation
of water displacing oil were compared to simulation of water displacing gas in a
reservoir containing a high permeability (5 Darcy) thief zone. In the case of water
displacing oil, water fingered through the high perm streak to the producer. In the
case of water displacing gas, a piston-like displacement occurred.
Areal water saturation maps from BPXA's full field model were presented, showing
the movement of water over time. The water is projected to move in a relatively
radial to oblong shaped front. At the end of GCWI injection in 2022, water is
projected to reach the waterflood area in the eastern part of the field, and the northern
oil producers in the gravity drainage area. However, the western portion of the gas
cap, and the major portion of the gravity drainage area are not expected to be invaded
with water. Shut-down of GCWI is expected in 2022. Review of model projections
through 2031 indicates little lateral movement of the water, again due to the low
mobility of the water to the gas in the area.
7. GCWI - Maior Gas sale Relationship
The WIOs addressed the interaction of the GCWI project with potential major gas
sales and how gas sales would impact the estimated benefits of the GCWI project and
CO 341D
November 30,2001
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Page 5
how gas cap water injection is expected to impact ultimate gas recovery.
a) Maior Gas Sale Effect on GCWI Recovery
A gas sale will reduce the incremental oil recovery from gas cap water injection.
While the rate and timing have not been determined for major gas sales, a case to
demonstrate the effect was shown. Assuming a 4 BCF /D gas sales rate beginning
in 2008, the incremental production derived from GCWI is reduced from about
200 MMB to about 135 MMB. The reduction in the recovery results from three
mechanisms:
· With a major gas sale the volume of gas available for injection is
reduced in order to meet the gas sale demand. This reduces
vaporization recovery for gas cap water injection;
. The ability of the injected gas to vaporize the oil it contacts diminishes
as reservoir pressure decreases.
. Gas sale will lower reservoir pressure, making the oil more viscous,
which decreases efficiency of oil production and reduces oil produced
by gravity drainage.
b) Effect of GCWI on Gas Recovery of Maior Gas Sales
The WIOs state that ultimate gas recovery should not be reduced by GCWI.
Major Gas Sales off-take will require a large water free area from which to
produce the gas. The simulation projections presented for the GCWI project
suggest that the water will be localized and a significant portion of the gas cap
will be free from water to allow blow-down of the gas reserves.
Without GCWI, gas recovery is expected to exceed 80% of the original gas cap
gas in place when the pressure is reduced from the original 4400 psi to about 850
psi. With GCWI, gas is expected to be trapped at a saturation of 25% within the
area of water injection. When reservoir pressure is subsequently reduced during
"blow down", the trapped gas expands and once again becomes mobile. In the
example shown by the WIOs, at a reservoir pressure of 1500 psi the gas recovery
was projected at 90% with GCWI, while by pressure depletion alone the pressure
has to be blown down to 500 psi to achieve the same recovery
8. Surveillance
BPXA presented plans to monitor injection well conformance, water movement and
reservoir pressure. The major components of the GCWI surveillance plan are:
· Injection wells will be monitored in a manner similar to other water injection
wells within the Prudhoe Bay pool.
· Pulsed Neutron Logs (PNLs) in existing wells will provide downhole and
regional data on the water movement.
· 4-D gravity will provide a general view of water movement.
· Reservoir pressure monitoring will be done according to current Prudhoe Bay
pool rules.
CO 341D
November 30,2001
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Page 6
a) Iniection Well Monitoring
Injection well monitoring will be conducted to ensure that the water injection is
contained in the desired reservoir interval. The injection wells will be monitored
with surface measured temperature, pressure and injection rate. These
measurements will be similar to other injection wells within the Prudhoe Bay
pool. With these measurements it is possible to monitor injection characteristics,
particularly changes in the injectivity indices. The injectivity indices provide
direct evidence of changes in well performance. Downhole measurements will
provide confirmation of the surface measurements and will also help describe
reservoir properties and hydraulic performance. Downhole temperature logs will
provide verification of injection conformance and confirm that fracture height
growth is confined within the Ivishak. Downhole pressure measurements will be
used to determine tubular pressure drops and hydraulic performance. Pressure
falloff tests will be undertaken to determine reservoir properties and wellbore
skin.
b) Water Movement Surveillance with Pulsed Neutron Logs:
The leading edge of the waterflood will be detected primarily with pulsed neutron
logs. BPXA identified more than nine wells surrounding the injection areas in
which pulsed neutron logs can be run to monitor the movement of water. These
wells are primarily Lisburne producing wells. BPXA indicated that there are no
known cement problems that would prevent confinement of injection to the
Ivishak. Pulsed neutron logs, specifically the RST logs, were chosen because
they can be run in Lisburne wells completed with 2 7/8 inch tubing. Also, they
can be run in two modes to collect data for discerning a major change in fluids
(sigma & Carbon/Oxygen). The RSTs will help locate the leading edge of the
waterflood, by detecting the change in saturation as water invades the Ivishak gas
cap interval at the wellbore. It will also provide data in determining the regional
waterflood coverage. BPXA indicated that the statistical variations seen in the
RST log measurements should not substantially affect the ability to detect
movement of water into the gas zones.
c) 4D Gravity Technique
The 4D Gravity technique utilizes very sensitive surface gravity measurements
taken periodically. The method measures small changes in gravity as the low-
density gas is replaced with the higher density water. Baseline measurements will
be taken prior to water injection. Subsequent measurements will be made at
discrete time intervals and compared to the baseline measurements. An increase in
the density of the fluids in the gas cap indicates the presence of water. BPXA
anticipates the 4D Gravity technique will allow them to map general water
movement, determine an average waterflood front, and provide a means to
perform a mass balance of the injected water. The major limitations of the 4D
gravity technique are that it cannot detect small horizontal or vertical flood fronts
and it cannot provide any downhole zonal information. Gravity measurements
coupled with material balance and PNL measurements can aid validation of
simulation predictions and fine tune history match calculations.
CO 341D
November 30, 2001
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Page 7
9. Proposed chan2e to Rule 12l c)
BPXA requested in the rules for GCWI that the requirements for mImmum
miscibility pressure stipulated in Rule 12( c) should be modified. Currently this rule
stipulated that the Operator maintain a pressure differential of at least 250 psi
between the minimum miscibility pressure of the miscible injectant and the prevailing
reservoir pressure. The 250 psi differential had been initially proposed by the WIOs
in testimony provided 10/9/91, and approved in CO 290 dated February 21, 1992.
This differential was based upon the assumption that the reservoir pressure will
decline 100-150 psi during the time in which a cycle of MI is in the reservoir. A
safety factor of 100 psi in addition was added to this. With GCWI pressure will be
maintained in the injection patterns. As such 100 psi differential is sufficient until
such time that the reservoir pressure is stabilized. This change will allow some
additional flexibility of the Operator to increase overall MI volumes, and disperse MI
to other areas of the field, leading to better optimization of MI throughout the field.
This will not have a negative impact upon overall recovery.
10. Miti2ation of Risks
Studies indicate that not implementing or further delaying GCWI will result in less
recovery over the remaining life of the field. The studies and analysis appear
thorough and technically sound. Though outweighed by the expected benefits to
overall hydrocarbon recovery, there remain some risks that must be managed through
ongoing surveillance. Oil reserves are potentially at risk if the injected water moves
too far, too fast and enters the sensitive Gravity Drainage area of the field. Numerous
reservoir simulation and studies show a likely tendency for the injected water to be
concentrated in the eastern portion of the gas cap where it is more likely to improve
oil recovery from up dip oil zone waterfloods already in progress or planned. In
addition, model studies have consistently shown that water will move in a piston-like
way through the gas cap, regardless of heterogeneities. Therefore, sweep efficiency
of the process will be high and the water should move downdip slowly. GCWI is a
recovery technique, which, though well studied, is untried at Prudhoe Bay. Despite
the lack of precedents, risks to hydrocarbon reserves can be controlled. The WIOs
have designed a process and outlined overall surveillance plans that should minimize
losses and ensure greater ultimate hydrocarbon recovery.
11. Blowout Prevention Equipment and Practice
The provisions of Rule 4 of CO 341 C are obsolete and inconsistent with current
Commission regulations as stated in 20AAC 25 and current North Slope operator
practice.
CO 341D
November 30,2001
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Page 8
CONCLUSIONS:
1. The application requirements of20 AAC 25.520 have been met.
2. The GCWI project is expected to significantly increase overall hydrocarbon recovery
from the Prudhoe Bay Oil Pool.
3. The GCWI project will mitigate pressure decline within the Prudhoe Bay Oil Pool.
4. With the planned implementation of GCWI, further investigation of options to
mitigate pressure decline and annual report of these investigations is no longer
necessary.
5. Further implementation of paragraph (d) of Rule 12, is unnecessary so long as the
GCWI project is in operation.
6. Decreasing the minimum pressure differential requirement of Paragraph (c) of Rule
12 from 250 psi between the minimum miscibility pressure and the average reservoir
pressure in the EOR injection areas will allow the Operator flexibility to provide
more MI volume, and will not negatively impact recovery. Potential for increased
rate and recovery exists through optimization of the MI injectant.
7. Adequate surveillance of the GCWI project is required to determine that water
movement within the reservoir is confined as intended and does not negatively impact
overall hydrocarbon recovery, and to determine if the project is successful in
stabilizing reservoir pressure.
8. The Commission needs to be apprised of surveillance plans and results on a yearly
basis.
9. The conclusions in CO 341 C and the amendments thereto are incorporated herein to
the extent not inconsistent with this order.
10. Rule 4 of CO 341C is no longer current and has been superseded by 20 AAC 25.035,
25.036,25.037,25.285,25.286,25.287, and 25.288.
CO 341D
November 30,2001
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Page 9
NOW, THEREFORE, IT IS ORDERED THAT
(1) Conservation Order 341D supersedes Conservation Order 341C dated June 12, 1997;
(2) Rule 4 of Conservation Order No. 341C is revoked, Rules 11,12, and 16 are amended,
and new Rule 17 is added; and
(3) In addition to statewide requirements under 20AAC 25 (to the extent not superseding
these rules), the following rules now apply to the Prudhoe Oil Pool within the
following described area (referred to in this order as the affected area):
UMIAT MERIDIAN
Township Range
T. ION., R. 12E.,
Section
1,2,3,4,10,11,12
T. ION., R. BE.,
1,2,3,4,5,6, 7,8,9, 10, 11, 12, 13, 14, 15, 16,24
T. ION., R. 14E.,
1, 2, 3, 4, 5, 6, 7, 8, 9, 10, 11, 12, 13, 14, 15, 16, 17,
18,19,20,21,22,23,24,25,26,27,28,36
T. ION., R. 15E.,
T. ION., R. 16E.,
T. llN., R. lIE.,
T. IIN., R. 12E.,
T. llN., R. BE.,
T. llN., R. 14E.,
T. llN., R. 15E.,
T. IIN., R. 16E.,
T. 12N., R. 10E.,
T. 12N., R. lIE.,
all
5,6,7,8,17,18,19,20,29,30,31
1,2,3,4,9, 10, 11, 12, 13, 14, 15,24,25
all
all
all
all
17, 18, 19,30,31,32
13,24,
15, 16, 17, 18, 19, 20, 21, 22, 25, 26, 27, 28, 29, 30,
32,33,34,35,36
T. 12N., R. 12E.,
23,24,25,26,27,28,29,30,31,32,33,34,35,36
T. 12N., R. BE.,
19,20,21,22,23,26,27,28,29,30,31,32,33,34,
35,36
T. 12N., R. 14E.,
25,26,27,28,29,31,32,33,34,35,36
CO 341D
November 30, 2001
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Page 10
T. 12N., R. 15E.,
25,26,27,28,29,30,31,32,33,34,35,36
(Source: C. O. 145, page 7, expansions/contractions of initial participating area based on
November 20, 1987 letter, Wade and Nelson to Eason, Re: Prudhoe Bay Unit Exhibits,
Exhibit C, Part I Oil Rim Participating Area and Part II Gas Cap Participating Area.)
Rule 1 Pool Defmition and Chan2Ïn2 the Affected Area (ref. C.O. 145)
(a) The Prudhoe Oil Pool is defined as the accumulations of oil that are common to and
which correlate with the accumulations found in the Atlantic Richfield - Humble
Prudhoe Bay State No.1 well between the depths of 8, 11 0 feet and 8,680 feet.
(Source: C.O. 145, Rule 1)
(b) The Commission may adjust the description of the affected area to conform to future
changes in the initial participating area by administrative approvaL
(Source: C. O. 145, Rule 12)
Rule 2 Well Spacin2 (ref. C.O. 145, 174)
There shall be no restrictions as to well spacing except that no pay shall be opened in a
well closer than 500 feet to the boundary of the affected area.
(Source: C.O. 174, Rule 2)
Rule 3 Casin2 and Cementin2 Reauirements (ref. C.O. 145,238)
(a) Conductor casing shall be set at least 75 feet below the surface and sufficient cement
shall be used to fill the annulus behind the pipe to the surface. Rigid high-density
polyurethane foam may be used as an alternate to cement, upon approval by the
Commission. The Commission may also administratively approve other sealing
materials upon application and presentation of data which show the alternate is
appropriate based on accepted engineering principles. (Source: C.O. 238, Rule 3a)
(b) Surface casing to provide proper anchorage for equipment, to prevent uncontrolled
flow, to withstand anticipated internal pressure, and to protect the well from the
effects of permafrost thaw-subsidence or freeze-back loading shall be set at least 500
feet, measured depth, below the base of the permafrost but not below 5000 feet true
vertical depth. Sufficient cement shall be used to fill the annulus behind the casing
to the surface. The surface casing shall have minimum axial strain properties of
0.5% in tension and 0.7% in compression.
(Source: C.O. 238, Rule 3b)
(c) Alternate casing programs may be administratively approved by the Commission
upon application and presentation of data, which show the alternatives, are
appropriate, based upon accepted engineering principles.
(Source: C.O. 238, Rule 3c)
CO 34ID
November 30, 2001
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Page 11
Rule 4 Blowout Prevention Eauipment and Practice (revoked c.o. 341D).
Rule 5 Automatic Shut-in Eauipment (ref. C.O. 145,333,363)
(a) Each well shall be equipped with a Commission approved fail-safe automatic surface
safety valve system (SVS) capable of preventing uncontrolled flow by shutting off
flow at the wellhead and shutting down any artificial lift system where an over
pressure of equipment may occur.
(b) The safety valve system (SVS) shall not be deactivated except during repairs, while
engaged in active well work, or if the pad is manned. If the SVS cannot be returned
to service within 24 hours, the well must be shut in at the well head and at the
manifold building.
1. Wells with a deactivated SVS shall be identified by a sign on the wellhead
stating that the SVS has been deactivated and the date it was deactivated.
2. A list of wells with the SVS deactivated, the dates and reasons for
deactivating, and the estimated re-activation dates must be maintained current
and available for Commission inspection on request.
(c) A representative of the Commission will witness operation and performance tests at
intervals and times as prescribed by the Commission to confirm that the SVS is in
proper working condition.
(d) The SVS must be maintained in working condition at all times unless the well is shut
in and secured, or the well is being operated in conformance with other sections of
this rule.
( e) Upon proper application or its own motion, the Commission may administratively
waive or amend the requirements of this rule as long as the change does not promote
waste, jeopardize correlative rights or compromise ultimate recovery, and is based
on sound engineering principles.
(t) Nothing in this rule precludes the installation of a SSSV in wells designated by the
operator. If a SSSV is installed, it must be maintained in working order and is
subject to performance testing as part ofthe SVS.
Rule 6 Pressure Surveys (ref. C.O. 145, 165, 192,208,213,220, AA 220.1, 341B)
(a) Prior to regular production, a static bottom hole or transient pressure survey shall be
taken on at least one in three wells drilled from a common drilling site.
(Source: C.O. 220, Rule 1, C.O. 341B)
CO 341D
November 30,2001
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Page 12
(b) An annual pressure surveillance plan shall be submitted to the Commission in
conjunction with the Annual Prudhoe Pool Reservoir Surveillance Report by April 1,
each year. The plan will contain the number of pressure surveys anticipated for the
next calendar year and be subject to approval by the Commission by May 1. These
surveys are needed to effectively monitor reservoir pressure in the Prudhoe Oil Pool.
The surveys required in (a) of this rule may be used to fulfill the minimum
requirements.
(Source: C.O. 220, Rule 6, C.O. 341B)
(c) Data from the surveys required in (a) and (b) ofthis rule shall be submitted with the
Annual Prudhoe Oil Pool Reservoir Surveillance Report by April 1 each year. Data
submitted shall include rate, pressure, time depths, temperature, and any well
condition necessary for the complete analysis of each survey. The datum for the
pressure surveys is 8800 feet subsea. Transient pressure surveys obtained by a shut
in buildup test, an injection well pressure fall-off test, a multi rate test or an
interference test are acceptable. Other quantitative methods may be administratively
approved by the Commission. (Source: C.O. 220, Rule 7, C. O. 341C.001)
(d) Results and data from any special reservoir pressure monitoring techniques, tests, or
surveys shall also be submitted as prescribed in (c) of this rule.
(Source: C.O. 220, Rule 8)
(e) By administrative approval the Commission may grant time extensions and waive
requirements of this rule, and by administrative order the Commission may require
additional pressure surveys in (b) of this rule. (Source: C.O. 220, Rule 5)
Rule 7 Gas-Oil Contact Monitorini! (ref. C.O. 145, 165, 192,208,213, AA 213.39)
(a) Prior to initial sustained production, a cased or open hole neutron log shall be run in
each well. (Source: C.O. 165, Rule 9a) This requirement is waived for
waterfloodlEOR areas encompassed by the expanded Prudhoe Bay Miscible Gas
Project outlined in C.O. 290, and for those areas not expected to have significant
GOC movement or gas encroachment from the gravity drainage area defined by the
Commission through Administrative Approval.
(Source: AA 213.39, excerpts from paragraph 1)
(b) A minimum of 40 repeat cased hole neutron log surveys shall be run annually.
(Source: C.O. 208, Rule 4)
(c) The neutron logs run on any well and those required in (a) and (b) of this rule shall
be filed with the Commission by the last day of the month following the month in
which the logs were run. (Source: C.O. 165, Rule 9d)
(d) By administrative approval, the Commission may delay, modify or waive the
logging requirements of this rule or may require additional wells to be logged.
(Source: C.O. 213, Rule 3)
CO 341D
November 30, 2001
.
.
Page 13
Rule 8 Productivity ProfIles (ref. C.O. 145, 165, 192,208,213, AA 213.40)
(a) A spinner flow meter or tracer survey shall be run in each well during the first six
months the well is on production. (Source: C.O. 165, Rule lla) This requirement is
waived for wells completed with a single perforated interval, or with perforations in
a single reservoir zone including highly deviated (greater than 65 degrees) and
horizontal wells.
(Source: AA 213.40 paragraph 3)
(b) Follow-up surveys shall be performed on a rotating basis so that a new production
profile is obtained on each well periodically. Nonscheduled surveys shall be run in
wells which experience an abrupt change in water cut, gas-oil ratio, or productivity.
(Source: e.O. 165, Rule lIb)
(c) The complete spinner flow meter or tracer data and results shall be recorded and
filed with the Commission by the last day of the month following the month in
which each survey is taken. (Source: C.O. 165, Rule llc)
(d) The Commission may administratively approve alternate methods and time periods
in the enforcement of this rule provided that the data obtained is appropriate for
monitoring the Prudhoe Oil Pool or may waive the requirements of (a), (b) and (c).
By administrative order the Commission may specify additional surveys other than
the surveys submitted under (a), (b) and (c) ofthis rule. (Sources: C.O. 208, Rule 8
and c.o. 213, Rule 2)
Rule 9 Pool Off-Take Rates (ref. c.o. 145,214)
The maximum annual average oil offtake rate is 1.5 million barrels per day plus
condensate production. The maximum annual average gas offtake rate is 2.7 billion
standard cubic feet per day, which contemplates an annual average gas pipeline delivery
sales rate of 2.0 billion standard cubic feet per day of pipeline quality gas when treating
and transportation facilities are available. Daily offtake rates in excess of these amounts
are permitted only as required to sustain these annual average rates. The annual average
offtake rates as specified shall not be exceeded without the prior written approval of the
Commission.
Annual average offtake rates mean the daily average rate calculated by dividing the total
volume produced in a calendar year by the number of days in the year. However, in the
first calendar year that large gas offtake rates are initiated, following the completion of a
large gas sales pipeline, the annual average offtake rate for gas shall be determined by
dividing the total volume of gas produced in the calendar year by the number of days
remaining in the year following initial delivery to the large gas sales pipeline.
Rule 10 Facilitv Gas Flarin2 revoked (ref. C. O. 34lC)
CO 341D
November 30,2001
.
.
Page 14
Rule 11 Annual Surveillance Reportinf! (ref. C.O. 165, 186, 195, 208, 223, 224, 279,
AA 279.1)
(a) An annual Prudhoe Oil Pool surveillance report will be required by April 1 of each
year. The report shall include but is not limited to the following:
1. Progress of enhanced recovery project(s) implementation and reservoir
management summary including engineering and geotechnical parameters.
2. Voidage balance by month of produced fluids, oil, water and gas, and injected
fluids, gas, water, low molecular weight hydrocarbons, and any other injected
substances (which can be filed in lieu of monthly Forms 10-413 for each EOR
project). (Source C.O. 279, Rule 7 and AA 279.1 excerpt from paragraph 3)
3. Analysis of reservoir pressure surveys within the field.
4. Results and where appropriate, analysis of production logging surveys, tracer
surveys and observation well surveys.
5. Results of gas movement and gas-oil contact surveillance efforts including a
summary of wells surveyed and analysis of gas movement within the reservoir.
The analysis shall include map(s) and/or tables showing the locations of various
documented gas movement mechanisms as appropriate.
(Source: C.O. 279, Rule 7)
6. Progress of the Gas Cap Water Injection project with surveillance observations
including;
(a) volume of water injected,
(b) reservoir pressure results, maps, and analysis (in conjunction with (a) 3 of
this rule),
(c) water movement and zonal conformance maps derived from surveillance
(such as Pulsed Neutron Logs and 4-D gravity surveys)
(d) results of reservoir evaluations of performance (such as material balance
and reservoir simulation studies),
( e) surveillance plans for the upcoming year, and
(f) any plans for change in project operation.
(b) Upon its own motion or upon written request, the Commission may administratively
amend this rule so long as the change does not promote waste nor jeopardize
correlative rights and is based on sound engineering principles.
(Source: C.O. 279, Rule 8)
Rule 12 Prudhoe Bay Miscible Gas Proiect lPBMGP) (ref. C.O. 195,290)
(a) Expansion of the PBMGP and infill expansion of miscible gas injection in the
NWFB is approved for the 59,740 acre portion of the Prudhoe Oil Pool defmed in
CO 341D
November 30, 2001
.
.
Page 15
the record. (Source: C.O. 290, Rule 1, AA 290.1)
(b) An annual report must be submitted to the Commission detailing performance of the
PBMGP and outlining compositional information for the current miscible injectant
(MI) necessary to maintain miscibility under anticipated reservoir conditions.
(Source: C.O. 290, Rule 2)
(c) The minimum miscibility pressure (MMP) of the Miscible Injectant must be
maintained at least 100 psi below the average reservoir pressure in the Prudhoe Bay
Miscible Project area. When the Operator demonstrates that the reservoir pressure is
no longer declining within the Prudhoe Bay Miscible Project Area (as evidenced by
reservoir pressure measurements), the MMP may be maintained at or below the
average reservoir pressure in the Prudhoe Bay Miscible Project area. (Source: C.O.
290, Rule 4; amended C.O. 341D)
(d) Revoked (e.O. 341D).
( e) Upon its own motion or upon written request, the Commission may amend this rule
by administrative action if the change does not promote waste, violate correlative
rights, nor jeopardize ultimate recovery, and is based on sound engineering
principles.
(Source: e.O. 290, Rule 6)
Rule 13 Waiver of GOR Limitation (ref. 8/22/86 letter)
The Commission waives the requirements of 20 AAC 25.240(b) for all oil wells in the
Prudhoe Oil Pool of the Prudhoe Bay Field so long as the gas from the wells is being
returned to the pool, or so long as the additional recovery project is in operation.
(Source: Letter 8/22/86, L. Smith to HeinzelNelson, paragraph 3)
Rule 14 Waiver of "Application for Sundry Approval" Reauirement for Workover
Operations (ref. C.O. 258)
The requirements of 20 AAC 25.280(a) are waived for development wells in the Prudhoe
Oil Pool of the Prudhoe Bay Field. (Source: C.O.258)
Rule 15 Waterfloodine: (ref. 3/20/81 letter Hamilton to NelsonINorgaard)
The commission approves the December 1980 additional recovery application for water-
flooding in the Prudhoe Oil Pool subject to the requirements listed in Rule 11 above.
Any proposed changes must be submitted to the Commission for approval.
(Source: Letter 3/20/81, Hamilton to NelsonINorgaard)
CO 341D
November 30, 2001
.
.
Page 16
Rule 16 Orders Revoked
The following Conservation Orders and associated Administrative Approvals and
letter approvals are hereby revoked. Conservation orders 78, 83B, 85, 87, 88, 96, 97,
98B, 117, 117 A, 118, 130, 137, 138, 139, 140, 141, 143, 145, 145A, 148, 155, 160,
164, 165, 166, 167, 169, 174, 178, 180, 181, 183, 184, 185, 186, 188, 189, 192, 194,
195, 195.1, 195.2, 195.4, 197, 199,200,204,208,213,214,219,220,223,224,238,
258, 259, 279, 290 and 333, 341, 341A, 341B, 341C, and March 20, 1981 and
August 22, 1986 letter approvals.
The hearing records of these orders are made part of the record for this order.
Rule 17 Gas Cap Water Iniections
The Gas Cap Water Injection Project as described in the operator's application and
testimony is approved. Ongoing reservoir surveillance is required to determine that water
movement within the reservoir is confined as intended and does not negatively impact
overall hydrocarbon recovery, and to determine that the project has resulted in
stabilization of reservoir pressure.
DONE at Anchorage, Alaska and dated November 30, 2001.
{þ. ~..J~
Cammy ~i Taylor, Chair
Alaska Oil and Gas Conservation Commission
an e . Se nt, Jr., Commissioner
Alaska OiLand Gas Conservation Commission
~M,~
... ..... .,.~..
Julie M. Heusser, Commissioner
Alaska Oil and Gas Conservation Commission
AS 31.05.080 provides that within 20 days after receipt of written notice of the entry of an order, a person affected by it
may file with the Commission an application for rehearing. A request for rehearing must be received by 4:30 PM on
the 23rd day following the date of the order, or next working day if a holiday or weekend, to be timely filed. The
Commission shall grant or refuse the application in whole or in part within 10 days. The Commission can refuse an
application by not acting on it within the 10-day period. An affected person has 30 days from the date the Commission
refuses the application or mails (or otherwise distributes) an order upon rehearing, both being the final order of the
Commission, to appeal the decision to Superior Court. Where a request for rehearing is denied by nonaction of the
Commission, the 30-day period for appeal to Superior Court runs from the date on which the request is deemed denied
(i.e., lOth day after the application for rehearing was filed).
Well Work Operations and Sundry Notice/Reporting Requirements for Pools Subject to Sundry Waiver Rules
July 29, 2005
DEVELOPMENT [PRODUCTION] WELLS
No Forms Re uired 1 Form Required 2 Forms Required
-10-403 Not Required
-10-404 Not Required
-10-403 Not Required
-10-404 / 407 or other form Required
-10-403 Required
-10-404 / 407 or other form Required
Thru-tubing Operations (D)
Thru-tubing Operations (D)
Thru-tubing Operations (D)
• Fill tag
• Permanent cement or mechanical plugs that
• Perforate anew pool (D)
• Set & pull retrievable plugs
do not completely abandon a zone. (D)
• Change GLV's
• Cutting off tailpipes. (D)
• Dummy & gauge ring runs
• Perforate new intervals within a pool (D)
• Pull &rerun SSSV's
• )
( Patches D
SPECIAL (D)
• Pressure surveys — unless required by
On a case -by -case basis, a 10-403 will be
some specific approval
required for a particular well or operation
• Temperature surveys —unless required by
if the Commission requests it.
some specific approval
• Caliper surveys
If a well is operating under a sundry
• Reperforating existing intervals
approval, a 10-403 may be required to
• Bottom hole samples
perform work. The operator should
• Spinner surveys
consult with the AOGCC to determine if
• Logs — CNL, TDT, CO, CCL, CBL and
a 10-403 is needed.
Other Types — Unless required by some
specific approval
• Pump changes.
• Packoff GLM (POGLM)
Attachment
Incorporated by reference into Conservation Orders 261 A, 297 A, 341 D Rule 14, 347 A, 351 A and 556
Page I of 5
Well Work Operations and Sundry Notice/Reporting Requirements for Pools Subject to Sundry Waiver Rules
July 29, 2005
DEVELOPMENT [PRODUCTION] WELLS
Nn Fnrmq Reauired 1 Form Reauired 2 Forms Required
-10-403 Not Required
-10-403 Not Required
-10-403 Required
-10-404 Not Required
-10-404 / 407 or other form Required
-10-404 / 407 or other form Required
Pumping Operations, including using coil.(D)
Pumping Operations, including using coil.
Pumping Operations, including using coil
• Tubing scale removal
• Stimulations (frac or acid) (D)
• Remedial cementing operations
• Sludge removal
• Remedial cementing operations
(including but not limited to)
• Freeze protection
o Conductor Fill (D)
o Casing shoes (outer annulus) (D)
• Ice plug removal
• Squeezes/plugs to control fluid
• Repair casing
• Inhibitor squeezes
movement in zone (D)
(including but not limited to)
• Hot Oil
o mechanical repairs (D)
• Tubing acid jobs
o "pumping" repairs (cement or
gel squeezes) (D)
• Fill clean out
Other Operations (D)
Other Operations
Other Operations
• Xmas tree & valve replacement
• Seal welding on bradenheads (D)
• Convert producer (D) to injector
• Diagnostic & pressure testing — unless
• Major welding repairs on wellheads
required by some specific approval
(D)
• Conductor "cutaways" and surface
casing welding repairs (D)
• Annular disposal (D)
(Reported on form 10-423)
Rig/Coil Operations
Rig/Coil Operations
• Alteration of mechanical completion
• Repair Casing
(including but not limited to)
(including but not limited to)
o Pulling tubing, milling packers (D)
o Mechanical repairs (D)
o Install velocity strings (D)
(scab liners, tiebacks, etc)
Attachment
Incorporated by reference into Conservation Orders 261 A, 297 A, 341 D Rule 14, 347 A, 351 A and 556
Page 2 of 5
Well Work Operations and Sundry Notice/Reporting Requirements for Pools Subject to Sundry Waiver Rules
July 29, 2005
SERVICE [INJECTION] WELLS
N F R d 1 Form Re uired 2 Forms Required
0 orms a uire
-10-403 Not Required
-10-404 Not Required
-10-403 Not Required
-10-404 / 407 or other form Required
-10-403 Required
-10-404 / 407 or other form Required
Thru-tubing Operations (S)
Thru-tubing Operations (S)
Thru-tubing Operations (S)
• Fill tag
• Perforate new interval within a pool (S)
• Perforate a new pool. (S)
• Set & pull retrievable plugs
• Permanent cement or mechanical
• Change GLV's
plugs that do not completely abandon
• Dummy & gauge ring runs
a zone (S)
• Pull & rerun SSSV's
• Patches (S)
• Pressure surveys — unless required by
• Cutting off tailpipes. (S)
some specific approval
• Temperature surveys — unless required by
SPECIAL {S)
some specific approval
• Caliper surveys
On a case -by -case basis, a 10-403 will be
• Reperforating existing intervals
required for a particular well or operation
• Bottom hole samples
if the Commission requests it.
• Spinner surveys
• Logs — CNL, TDT, CO, CCL, CBL and
If a well is operating under a sundry
Other Types — Unless required by some
approval, a 10-403 may be required to
specific approval
perform work. The operator should
consult with the AOGCC to determine if
a 10-403 is needed.
If operations in this column are planned on a
A 10-403 should be submitted for any
Please note that authorization from EPA
disposal well, the operator should contact the
perforating (new or reperf) operations on a
Region 10 may be necessary to perform an
AOGCC to determine if a 10-403 is needed.
Class II disposal well.
work on a Class I disposal well.
Attachment
Incorporated by reference into Conservation Orders 261 A, 297 A, 341 D Rule 14, 347 A, 351 A and 556
Page 3 of 5
Well Work Operations and Sundry Notice/Reporting Requirements for Pools Subject to Sundry Waiver Rules
July 29, 2005
No Forms Required
-10-403 Not Required
-10-404 Not Required
Pumping Operations, including using coil.(S)
• Tubing scale removal
• Sludge removal
• Freeze protection
• Ice plug removal
• High pressure breakdown or inhibitor
squeezes, excluding frac or acid jobs
• Hot Oil
• Tubing acid jobs
• Fill clean out
Other Operations (S)
• Xmas tree & valve replacement
• Diagnostic & pressure testing — unless
required by some specific approval
SERVICE [INJECTION] WELLS
1 Form Required
-10-403 Not Required
-10-404 / 407 or other form Require
Pumping Operations, including using coil.
• Remedial cementing operations
o Conductor Fill (S)
• Squeezes/plugs to control fluid
movement in zone (S)
Other Operations
• Injection well MIT (on MIT form) (S)
• Initial conversion from water injector
to WAG injector (S)
• Convert from injector to producer if for
more than 30 days. (S)
• Seal welding on bradenheads (S)
L norms Kequirect
-10-403 Required
-10-404 / 407 or other form Required
Pumping Operations, including using coil.
• Stimulations (frac or acid) (S)
• Remedial cementing operations
(including but not limited to)
o Casing shoes (outer annulus) (S)
• Repair casing
(including but not limited to)
o mechanical repairs (S)
o "pumping" repairs (cement or
gel squeezes) (S)
Other Operations
• Major welding repairs on wellheads
• Conductor "cutaways" and surface
casing welding repairs (S)
• Annular disposal (S)
(Reported on form 10-423)
Attachment
Incorporated by reference into Conservation Orders 261 A, 297 A, 341 D Rule 14, 347 A, 351 A and 556
Page 4of5
Well Work Operations and Sundry Notice/Reporting Requirements for Pools Subject to Sundry Waiver Rules
July 29, 2005
Rig/Coil Operations
• Alteration of mechanical completion
(including but not limited to)
o Pulling tubing ,milling packers (S)
• Repair Casing
(including but not limited to)
o Mechanical repairs (S)
(scab liners, tiebacks, etc)
Attachment
Incorporated by reference into Conservation Orders 261 A, 297 A, 341 D Rule 14, 347 A, 351 A and 556
Page 5 of 5
NY PUBLIC LIBRARY DIV E, GRAND
CENTRAL STATION
POBOX 2221
NEW YORK, NY 10163-2221
US MIN MGMT SERV, CHIEF OCS
STATS & INFO
381 ELDEN ST MS 4022
HERNDON, VA 20170-4817
TECHSYS CORP,
BRANDY KERNS
PO BOX 8485
GATHERSBURG, MD 20898
SD DEPT OF ENV & NATRL
RESOURCES, OIL & GAS PROGRAM
2050 W MAIN STE #1
RAPID CITY, SO 57702
LINDA HALL LIBRARY, SERIALS DEPT
5109 CHERRY ST
KANSAS CITY. MO 64110-2498
XTO ENERGY,
SUSAN lILL Y
210 PARK AVE STE 2350
OKLAHOMA CITY, OK 73102-5605
OIL & GAS JOURNAL,
LAURA BELL
POBOX 1260
TULSA, OK 74101
DEGOL YER & MACNAUGHTON,
MIDCONTINENT DIVISION
ONE ENERGY SQ, STE 400
4925 GREENVILLE AVE
DALLAS. TX 75206-4083
SHELL WESTERN E&P INC,
G.S. NADY
POBOX 576
HOUSTON. TX 71001-0574
RAY TYSON
2016 MAIN #1415
HOUSTON, TX 71002-8844
e
OFFICE OF THE GOVERNOR,
JOHN KATZ STE 518
444 N CAPITOL NW
WASHINGTON, DC 20001
LIBRARY OF CONGRESS, STATE
DOCUMENT SECTION
EXCH & GIFT DIV
10 FIRST ST SE
WASHINGTON, DC 20540
US GEOLOGICAL SURVEY, LIBRARY
NATIONAL CTR MS 950
RESTON, VA 22092
AMOCO CORP 2002A, LIBRARY/INFO
CTR
POBOX 87703
CHICAGO, IL 60680-0703
ALFRED JAMES III
107 N MARKET STE 1000
WICHITA, KS 67202-1811
IOGCC,
POBOX 53127
OKLAHOMA CITY, OK 73152-3127
BAP! RAJU
335 PINYON LN
COPPELL, TX 75019
STANDARD AMERICAN OIL CO,
AL GRIFFITH
POBOX 370
GRANBURY, TX 76048
H J GRUY,
ATTN: ROBERT RASOR
1200 SMITH STREET STE 3040
HOUSTON, TX 77002
CHEVRON,
PAUL WALKER
1301 MCKINNEY RM 1750
HOUSTON. TX 77010
.
ARENT FOX KINTNER PLOTKIN KAHN,
LIBRARY
WASHINGTON SQ BLDG
1050 CONNECTICUT AV NW
WASHINGTON, DC 20036-5339
US DEPT OF ENERGY,
PHYLLIS MARTIN MS EI823
1000 INDEPENDENCE SW
WASHINGTON, DC 20585
DPC,
DANIEL DONKEL
2121 NORTH BAYSHORE DR #616
MIAMI, FL 33137
ILLINOIS STATE GEOL SURV, LIBRARY
469 NATURAL RESOURCES BLDG
615 E PEABODY DR
CHAMPAIGN, IL 61820
UNIV OF ARKANSAS, SERIALS DEPT
UNIV LIBRARIES
FAYETTEVILLE, AR 72701
R E MCMILLEN CONSULT GEOL
202 E 16TH ST
OWASSO, OK 74055-4905
US DEPT OF ENERGY, ENERGY
INFORMATION ADMINISTRATION
MIR YOUSUFUDDIN
1999 BRYAN STREET STE 1110
DALLAS, TX 75201-6801
XTO ENERGY,
MARY JONES
810 HOUSTON ST STE 2000
FORT WORTH, TX 76102-6298
PURVIN & GERTZ INC, LIBRARY
2150 TEXAS COMMERCE TWR
600 TRAVIS ST
HOUSTON, TX 77002-2979
OIL & GAS JOURNAL,
BOB WILLIAMS
1700 W LOOP SOUTH STE 1000
HOUSTON, TX 77027
PETRAL CONSULTING CO,
DANIEL L LIPPE
9800 RICHMOND STE 505
HOUSTON, TX 77042
MARK ALEXANDER
7502 ALCOMITA
HOUSTON, TX 77083
EXXON EXPLORATION CO.,
T E ALFORD
POBOX 4778
HOUSTON, TX 77210-4778
PETR INFO.
DAVID PHILLIPS
POBOX 1702
HOUSTON, TX 77251-1702
EXXONMOBIL PRODUCTION
COMPANY,
GARY M ROBERTS RM 3039
PO BOX2180
HOUSTON, TX 77252-2180
CHEVRON CHEM CO, LIBRARY & INFO
CTR
POBOX 2100
HOUSTON, TX 77252-9987
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
105070 W MAPLEWOOD DR
LITTLETON, CO 80127
C & R INDUSTRIES, INC...
KURT SAL TSGAVER
7500 W MISSISSIPPI AVE STE C4
LAKEWOOD, CO 80226-4541
e
GAFFNEY, CLINE & ASSOC., INC.,
LIBRARY
1360 POST OAK BLVD., STE 2500
HOUSTON, TX 77056
MARATHON OIL CO,
GEORGE ROTHSCHILD JR RM 2537
PO BOX 4813
HOUSTON, TX 77210
EXXON EXPLOR CO,
LAND/REGULATORY AFFAIRS RM 301
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
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
JERRY HODGDEN GEOL
408 18TH ST
GOLDEN, CO 80401
e
MURPHY EXPLORATION &
PRODUCTION CO.,
BOB SAWYER
550 WESTLAKE PARK BLVD STE 1000
HOUSTON, TX 77079
UNOCAL, REVENUE ACCOUNTING
PO BOX 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
TESORO PETR CORP.
LOIS DOWNS
300 CONCORD PLAZA DRIVE
SAN ANTONIO, TX 78216-6999
ROBERT G GRAVELY
7681 S KIT CARSON DR
LITTLETON, CO 80122
US GEOLOGICAL SURVEY, LIBRARY
BOX 25046 MS 914
DENVER, CO 80225-0046
NRG ASSOC.
RICHARD NEHRING
POBOX 1655
COLORADO SPRINGS, CO 80901-
1655
RUBICON PETROLEUM, LLC,
BRUCE I CLARDY
SIX PINE ROAD
COLORADO SPRINGS, CO 80906
US GEOLOGICAL SURVEY, LIBRARY
2255 N GEMINI DR
FLAGSTAFF, AZ 86001-1698
BABSON & SHEPPARD,
JOHN F BERGQUIST
POBOX 8279 VIKING STN
LONG BEACH, CA 90808-0279
TEXACO INC, Portfolio Team Manager
R W HILL
POBOX 5197x
Bakersfield, CA 93388
H L WANGENHEIM
5430 SAWMILL RD SP 11
PARADISE, CA 95969-5969
MARPLES BUSINESS NEWSLETTER,
MICHAEL J PARKS
117 W MERCER ST STE 200
SEATTLE, WA 98119-3960
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
YUKON PACIFIC CORP,
JOHN HORN VICE CHM
1049 W 5TH AV
ANCHORAGE, AK 99501-1930
e
JOHN A LEVORSEN
200 N 3RD ST #1202
BOISE, ID 83702
MUNGER OIL INFOR SERV INC,
POBOX 45738
LOS ANGELES, CA 90045-0738
ANTONIO MADRID
POBOX 94625
PASADENA, CA 91109
US GEOLOGICAL SURVEY,
KEN BIRD
345 MIDDLEFIELD RD MS 999
MENLO PARK, CA 94025
ECONOMIC INSIGHT INC,
SAM VAN VACTOR
POBOX 683
PORTLAND, OR 97207
DEPT OF REVENUE,
BEVERLY MARQUART
550 W 7TH A V STE 570
ANCHORAGE, AK 99501
STATE PIPELINE OFFICE, LIBRARY
KATE MUNSON
411 W4THAVE,STE2
ANCHORAGE, AK 99501
DEPT OF ENVIRON CONSERVATION,
DIV OF AIR & WATER QUALITY
TOM CHAPPLE
555 CORDOVA STREET
ANCHORAGE, AK 99501
FOREST OIL,
JIM ARLINGTON
310 K STREET STE 700
ANCHORAGE, AK 99501
PRESTON GATES ELLIS LLP, LIBRARY
420 L ST STE 400
ANCHORAGE, AK 99501-1937
e
TAHOMA RESOURCES,
GARY PLAYER
1671 WEST 546 S
CEDER CITY, UT 84720
LA PUBLIC LIBRARY, SERIALS DIV
630 W 5TH ST
LOS ANGELES, CA 90071
ORO NEGRO, INC.,
9321 MELVIN AVE
NORTH RIDGE, CA 91324-2410
SHIELDS LIBRARY, GOVT DOCS DEPT
UNIV OF CALIF
DAVIS, CA 95616
US EPA REGION 10,
THOR CUTLER OW-137
1200 SIXTH AVE
SEATTLE, WA 98101
TRUSTEES FOR ALASKA,
1026 W. 4th Ave, Ste 201
ANCHORAGE. AK 99501
DEPT OF REVENUE, OIL & GAS AUDIT
DENISE HAWES
550 W 7TH A V STE 570
ANCHORAGE, AK 99501
DEPT OF REVENUE,
DAN DICKINSON, DIRECTOR
550 W 7TH AVE, SUITE 500
ANCHORAGE, AK 99501
GUESS & RUDD,
GEORGE LYLE
510 L ST, STE 700
ANCHORAGE, AK 99501
ALASKA DEPT OF LAW.
ROBERT E MINTZ ASST ATTY GEN
1031 W 4TH AV STE 200
ANCHORAGE, AK 99501-1994
GAFO,GREENPEACE
PAMELA MILLER
125 CHRISTENSEN DR. #2
ANCHORAGE, AK 99501-2101
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
DEPT OF NATURAL RESOURCES, DIV
OF OIL & GAS
BRUCE WEBB
550 W 7TH AVE, SUITE 800
ANCHORAGE, AK 99501-3560
HDR ALASKA INC,
MARK DALTON
2525 C ST STE 305
ANCHORAGE, AK 99503
ALASKA OIL & GAS ASSOC,
JUDY BRADY
121 W FIREWEED LN 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
DICK FOLAND
6881 ABBOTT LOOP RD
ANCHORAGE, AK 99507
UON ANCHORAGE, INST OF SOCIAL
& ECON RESEARCH
TERESA HULL
3211 PROVIDENCE DR
ANCHORAGE, AK 99508
TRADING BAY ENERGY CORP,
PAUL CRAIG
5432 NORTHERN LIGHTS BLVD
ANCHORAGE, AK 99508
e
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 AND ENG SERVICE,
MIKE TORPY
2000 W. INT'L AIRPORT RD #C-1
ANCHORAGE, AK 99502-1116
ANADARKO,
MARK HANLEY
3201 C STREET STE 603
ANCHORAGE, AK 99503
ANADRILL-SCHLUMBERGER,
3940 ARCTIC BLVD #300
ANCHORAGE, AK 99503-5711
JAMES E EASON
8611 LEEPER CIRCLE
ANCHORAGE, AK 99504-4209
AMERICNCANADIAN STRATIGRPH CO,
RON BROCKWAY
4800 KUPREANOF
ANCHORAGE, AK 99507
THOMAS R MARSHALL JR
1569 BIRCHWOOD ST
ANCHORAGE, AK 99508
US BLM AK DIST OFC, GEOLOGIST
ARTHUR BANET
949 EAST 36TH AVE STE 308
ANCHORAGE, AK 99508
e
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
JIM STOUFFER
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
BAKER OIL TOOLS, ALASKA AREA
MGR
4710 BUS PK BLVD STE 36
ANCHORAGE, AK 99503
N-I TUBULARS INC,
3301 C Street Ste 209
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
PETER J DITTON
6881 ABBOTT LOOP ROAD
ANCHORAGE, AK 99507
BUREAU OF LAND MANAGEMENT,
GREG NOBLE
6881 ABBOTT LOOP ROAD
ANCHORAGE, AK 99507
VECO ALASKA INC.,
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, AK OCS
REGIONAL DIR
949 E 36TH AV RM 110
ANCHORAGE, AK 99508-4302
REGIONAL SUPRVISOR, FIELD
OPERATNS, MMS
ALASKA OCS REGION
949 E 36TH AV STE 308
ANCHORAGE, AK 99508-4363
US MIN MGMT SERV,
FRANK MILLER
949 E 36TH AV STE 603
ANCHORAGE, AK 99508-4363
CIRI, LAND DEPT
POBOX 93330
ANCHORAGE, AK 99509-3330
PHILLIPS ALASKA, LAND DEPT
JAMES WINEGARNER
POBOX 10036
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
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
ARMAND SPIELMAN
651 HILANDER CIRCLE
ANCHORAGE. AK 99518
e
US MIN MGMT SERV,
RICHARD PRENTKI
949 E 36TH AV
ANCHORAGE, AK 99508-4302
US MIN MGMT SERV, LIBRARY
949 E 36TH A V RM 603
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,
MARK MAJOR A TO 1968
POBOX 100360
ANCHORAGE, AK 99510-0360
PHILLIPS ALASKA, LEGAL DEPT
MARK P WORCESTER
POBOX 100360
ANCHORAGE, AK 99510-0360
AL YESKA PIPELINE SERV CO.
PERRY A MARKLEY
1835 S BRAGAW - MS 575
ANCHORAGE, AK 99512
DAVID W. JOHNSTON
320 MARINER DR.
ANCHORAGE, AK 99515
NORTHERN CONSULTING GROUP,
ROBERT BRITCH, P.E.
2454 TELEQUANA DR.
ANCHORAGE, AK 99517
ASRC,
CONRAD BAGNE
301 ARCTIC SLOPE AV STE 300
ANCHORAGE. AK 99518
e
GORDONJ.SEVERSON
3201 WESTMAR CIR
ANCHORAGE, AK 99508-4336
US MIN MGMT SERV, RESOURCE
EVAL
JIM SCHERR
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
JODY COLOMBIE
6811 ROUND TREE DRIVE
ANCHORAGE, AK 99516
GERALD GANOPOLE CONSULT GEOL
2536 ARLINGTON
ANCHORAGE, AK 99517-1303
DAVID CUSATO
600 W 76TH A V #508
ANCHORAGE. AK 99518
HALLIBURTON ENERGY SERV,
MARK WEDMAN
6900 ARCTIC BLVD
ANCHORAGE, AK 99518-2146
JACK 0 HAKKILA
POBOX 190083
ANCHORAGE, AK 99519-0083
MARATHON OIL CO, LAND
BROCK RIDDLE
POBOX 196168
ANCHORAGE, AK 99519-6168
EXXONMOBIL PRODUCTION
COMPANY,
MARK P EVANS
PO BOX 196601
ANCHORAGE, AK 99519-6601
BP EXPLORATION (ALASKA) INC,
PETE ZSELECZKY LAND MGR
POBOX 196612
ANCHORAGE, AK 99519-6612
AMSINALLEE CO INC,
WILLIAM 0 VALLEE PRES
PO BOX 243086
ANCHORAGE, AK 99524-3086
D A PLATT & ASSOC,
9852 LITTLE DIOMEDE CIR
EAGLE RIVER, AK 99577
COOK INLET KEEPER,
BOB SHAVELSON
PO BOX 3269
HOMER, AK 99603
DOCUMENT SERVICE CO,
JOHN PARKER
POBOX 1468
KENAI. AK 99611-1468
PENNY VADLA
POBOX 467
NINILCHIK, AK 99639
e
e
OPST AD & ASSOC,
ERIK A OPSTAD PROF GEOL
POBOX 190754
ANCHORAGE, AK 99519
ENSTAR NATURAL GAS CO,
PRESIDENT
TONY IZZO
POBOX 190288
ANCHORAGE, AK 99519-0288
UNOCAL,
POBOX 196247
ANCHORAGE, AK 99519-6247
BP EXPLORATION (ALASKA), INC.,
MARK BERLINGER MB 8-1
PO BOX 196612
ANCHORAGE, AK 99519-6612
BP EXPLORATION (ALASKA) INC,
MR. DAVIS, ESQ
POBOX 196612 MB 13-5
ANCHORAGE, AK 99519-6612
L G POST O&G LAND MGMT CONSULT
10510 Constitution Circle
EAGLE RIVER, AK 99577
JAMES RODERICK
PO BOX 770471
EAGLE RIVER, AK 99577-0471
PHILLIPS PETROLEUM CO. ALASKA
OPERATIONS MANAGER
J W KONST
PO DRAWER 66
KENAI, AK 99611
KENAI PENINSULA BOROUGH,
ECONOMIC DEVEL DISTR
STAN STEADMAN
POBOX 3029
KENAI, AK 99611-3029
BELOWICH,
MICHAEL A BELOWICH
1125 SNOW HILL AVE
WASILLA, AK 99654-5751
TESORO ALASKA COMPANY,
PO BOX 196272
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, INF(
RESOURCE CTR MB 3-2
POBOX 196612
ANCHORAGE, AK 99519-6612
BP EXPLORATION (ALASKA) INC,
SUE MILLER
POBOX 196612 M/S LR2-3
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
RON DOLCH OK
POBOX 83
KENAI, AK 99611
NANCY LORD
PO BOX 558
HOMER, AK 99623
PACE,
SHEILA DICKSON
POBOX 2018
SOLDOTNA, AK 99669
JAMES GIBBS
POBOX 1597
SOLDOTNA, AK 99669
AL YESKA PIPELINE SERVICE CO,
VALDEZ CORP AFFAIRS
SANDY MCCLINTOCK
POBOX 300 MS1701
VALDEZ,AK 99686
NICK STEPOVICH
543 2ND AVE
FAIRBANKS, AK 99701
FAIRBANKS DAILY NEWS-MINER,
KATE RIPLEY
POBOX 70710
FAIRBANKS, AK 99707
K&K RECYCL INC,
POBOX 58055
FAIRBANKS, AK 99711
UNIV OF ALASKA FBX, PETR DE VEL
LAB
SHIRISH PATIL
437 DICKERING
FAIRBANKS, AK 99775
DEPT OF ENVIRON CONSERV SPAR,
CHRIS PACE
410 WILLOUGHBY AV STE 105
JUNEAU, AK 99801-1795
e
KENAI NATL WILDLIFE REFUGE,
REFUGE MGR
POBOX 2139
SOLDOTNA, AK 99669-2139
VALDEZ VANGUARD, EDITOR
POBOX 98
VALDEZ, AK 99686-0098
COOK AND HAUGEBERG,
JAMES DIERINGER, JR.
119 NORTH CUSHMAN, STE 300
FAIRBANKS, AK 99701
C BURGLlN
POBOX 131
FAIRBANKS, AK 99707
ASRC,
BILL THOMAS
POBOX 129
BARROW, AK 99723
UNIVERSITY OF ALASKA FBKS, PETR
DEVEL LAB
DR AKANNI LAWAL
POBOX 755880
FAIRBANKS, AK 99775-5880
e
VALDEZ PIONEER,
POBOX 367
VALDEZ, AK 99686
UNIV OF ALASKA FAIRBANKS, PETR
DEVEL LAB
DR V A KAMATH
427 DUCKERI NG
FAIRBANKS, AK 99701
RICK WAGNER
POBOX 60868
FAIRBANKS, AK 99706
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
,
.
.
,.
fl
I'
d
Lb
~
FRANK H. MURKOWSKI, GOVERNOR
AI.ASIiA. OIL AND GAS
CONSERVATION COMMISSION
333 W. 7'" AVENUE, SUITE 100
ANCHORAGE, ALASKA 99501-3539
PHONE (907) 279-1433
FAX (907) 276-7542
ADMINISTRATIVE APPROVAL NO. 207.17
ADMINISTRATIVE APPROVAL NO. 311B.01
ADMINISTRATIVE APPROVAL NO. 329A.01
ADMINISTRATIVE APPROVAL NO. 341D.01
ADMINISTRATIVE APPROVAL NO.345.01
ADMINISTRATIVE APPROVAL NO. 452.01
ADMINISTRATIVE APPROVAL NO. 457A.01
ADMINISTRATIVE APPROVAL NO. 471.01
ADMINISTRATIVE APPROVAL NO. 484.01
George Blankenship
GPB Field Manager
BP Exploration (Alaska), Inc.
PO Box 196612
Anchorage, Alaska 99519
Dear Mr. Blankenship:
Conservation Order No. 492, dated June 26, 2003, amended the
conservation orders adopting pool rules for all pools within the Prudhoe
Bay field to add rules addressing sustained annulus pressures in devel-
opment wells. Upon further review, the Commission has determined that
paragraph 6 of these annulus pressure rules should be clarified.
Paragraph 6 provides that before a shut-in well is placed in
service, any annulus pressure must be relieved to a suffi-
cient degree that specified annulus pressures at operating
temperature will not be reached or exceeded. However,
paragraph 3 of the annulus pressure rules contemplates that
there may be wells that can be safely operated with an annu-
lus pressure in excess of a maximum specified in paragraph
6, and in such cases it would not be practicable or meaning-
ful to relieve annulus pressure to the degree required under
paragraph 3 when placing a shut-in well in service. In addi-
tion, the Commission may approve different pressure limits
for well start-up on a case-by-case basis under paragraphs 4
and 5.
Go:' <0,/ L\,''''~E'J\ r 'Uf' r, l" 2nO*)
ø~H~~j'ìl .L., A l'J n .) ),1
t'
July 29,2003
Page 2 of2
Accordingly, Conservation Orders No. 207, 311B, 329A, 341D,
345,452, 457A, 471, and 484 are amended to replace paragraph 6 of the
annulus pressure rules adopted in Conservation Order No. 492 with the
following revised paragraph 6:
.
.
I
6. Except as otherwise approved by the AOGCC under para-
graph 4 or 5 of these rules, before a shut-in well is placed in
service, any annulus pressure must be relieved to a suffi-
cient degree (a) that the inner annulus pressure at operating
temperature will be below 2500 psig for wells processed
through the Lisburne Production Center and below 2000
psig for all other development wells, and (b) that the outer
annulus pressure at operating temperature will be below
1000 psig. However, a well that is subject to paragraph 3,
but not paragraph 5, of these rules may reach an annulus
pressure at operating temperature that is described in the
operator's notification to the AOGCC under paragraph 3,
unless the AOGCC prescribes a different limit.
DATED at Anchorage, Alaska and dated July 29, 2003.
fiG/< ,~, ,¡;;"
BY ORDER OF THE COMMISSION
#14
•
Katrina Garner, P.E.
Base Management Manager
March 31, 2014
,RECEWPo
APR 0 2 2014
BP Exploration (Alaska) Inc.
P.O. Box 196612
900 E Benson Boulevard
Anchorage
AK 99519-6612
UNITED STATES OF AMERICA
Alaska Oil and Gas Conservation Commission
333 W. 7jh Avenue, Suite 100 Phone:+1-907-230-4212
Anchorage, AK 99501-3539
Re: Conservations Order CO 45713.003 and CO 341 D.005 for well S-26
(commingled production)
Dear Commissioners,
In a letter dated September 30, 2013 (copy enclosed) BP Exploration (Alaska)
Inc. (BPXA) reporteda lapse in our special reporting requirements under the
above -referenced Conservation Orders on well S-26, with a recommended
action plan to address the allocation issues. We have completed a review of the
situation and report the following.
All collected samples have been analysed and we have back -calculated the
impact of misallocation between the zones. The total discrepancy of 15,857 bbl
was allocated to the Kuparuk that should have been allocated to the Ivishak. A
plot of daily average daily production for the Aurora field is shown below with
both the previously -reported splits (red) and the new correct splits (blue).
•
0
Page 2
—+—Avg Daily Aurora Production
350 7
i
300
250
150
100
- N Daily Avg on 47% Aur Split
50
0
F+
N
A
01
V
l0
Y Y
N
�a
lJU
V
06
!-+
Y Y
W
to
O1
00
Y
Y Y W
Ql
N
N
N
N
O
N
tD
Y
v Qo
v
(n
O
N
N
O
N
\
p
N
\
N N
N
p
N
N
N
\ N C
Y
O
O
W
O
O
O N
O
Y
coo
N
coo
Y
O
O
O
N C Y
Y
Y
1-
O
Y Y
Y
Y
Y
Y
Y Y
N
N
N
N
Y
N W
W
W
W
W
Y ja
Y
N
W
To prevent future misallocations, we have established an automated reminder
system to ensure the samples are collected in a timely manner and properly
allocated between the oil pools.
Please contact the Base Management Team Leader for the West End Area,
Werner Schinagl, or myself with any questions regarding this matter.
Respectfully,
Katrina Garner, P.E.
Base Management Manager
Attachments:
Letter dated September 30, 2013
#13
Katrina Garner, P.E.
Base Management Manager
September 30, 2013
RECEIVED •
OCT 0 2 2013
AOGCC
5 4 0
BP Exploration (Alaska) Inc.
P.O. Box 196612
900 East Benson Boulevard
Anchorage, Alaska
AK 99519.6612
UNITED STATES OF AMERICA
Phone: +1.907.230.4212
Alaska Oil and Gas Conservation Commission
333 W. 7th Avenue, Suite 100
Anchorage, AK 99501-3539
Re: Conservation Order CO 457B.003 and C0341 D.005 for well S-26
(commingled production)
Dear Commissioners,
BPXA recently discovered a lapse in our special reporting requirements under CO
457B.003 and CO 34D.005 on well S-26. This well is a commingled producer
completed in the Prudhoe Oil Pool and the Aurora Oil Pool. Your letter dated
November 27, 2007 requires geochemical sampling every 6 months and not less
frequently than every 7 months. Our last update of the allocation factors is dated
May 3, 2010. Samples have been taken since then as follows:
• February 21, 2011
• January 2, 2012
• June 22, 2012
• January 2, 2013
• June 26, 2013 (two samples)
The delay from May 3, 2010 to February 21, 2011 resulted from the well being
shut in between October 5, 2010 and February 16, 2011. Unfortunately, we did
not take a sample between February 2011 and January 2012, The analysis of the
samples taken is being performed now.
I have asked the team responsible for the West End Area to implement the
following plan:
• Analyze all samples
• Ensure samples are taken at the required intervals
• Back -calculate any amount of impact due to potential misallocation
between the zones
• Update the allocation on a point -forward basis
•
•
Page 2
I will keep you informed about any impact of misallocation between the different
oil pools as well as on progress of the plan outlined above.
Please contact the Base Management Team Leader for the West End Area,
Werner Schinagl, or myself with any questions regarding this matter.
Respectfully,
zt/Vr�.P/L-
Katrina Garner, P. E.
Base Management Manager
#12
0 •
T SITATE DEF AELASEA SEAN PARNELL, GOVERNOR
CONSERVATION ALASKA OIL AND GAS 333 W. 7th AVENUE, SUITE 100
CONSERVATION COMI'IISSION ANCHORAGE, ALASKA 99501 -3539
PHONE (907) 279 -1433
FAX (907) 276 -7542
June 27, 2011
Dave Norton, P.E.
Manager, Engineering
Alaska Gasline Development Corporation
PO Box 101020
Anchorage, Alaska 99510
Re: Gas Off -take for Instate Gas Pipeline
Dear Mr. Norton:
Thank you for the update regarding the in -state gas pipeline project. As to your
inquiry regarding gas offtake rates, in 1977 the Prudhoe Bay Field rate was set, by Rule 9
of Conservation Order 341D, at a total of 2.7 billion standard cubic feet per day. Due to
the reservoir's development, additional information and the passage of time, in 2005 the
Commission initiated an investigation into the need to update Rule 9. On July 10, 2007,
the Commission determined "no change in Rule 9 is necessary at this time." Therefore,
given the parameters of your inquiry, an offtake of a half billion standard cubic feet per
day would be authorized under Rule 9.
.� - el,
a i
o • ► . Norman
om ' sioner
cc: Commissioner Daniel T. Seamount, AOGCC
Commissioner Cathy P. Foerster, AOGCC
*11
• •
ALASKA ** RECEIVED
*
ASUNE * * *
DEVELOPMENT CORP. Alaska Oil & Cons. Commission
GAS FOR BLNSKNNS Anr13eraGc
May 24, 2011
Alaska Oil and Gas Conservation Commission
Attn: Cathy Foerster
333 W. 7 Ave., Ste 100
Anchorage, AK. 99501
Subject: Gas Off -Take For Instate Gas Pipeline
Dear Commissioner Foerster:
As you know from our briefing with you last June we are developing a project plan for an in -state
gas pipeline that will deliver gas to Fairbanks and Southcentral Alaska. We have developed the
plan to the point where we wish to clarify with the Commission the availability of a gas off -take
rate. We currently envision first gas into our pipeline from the Prudhoe Bay Unit 2019 ramping
up to about 500 MMscf /day by 2020.
Based on this information please advise us what, if any, orders or regulatory actions would be
taken by the Commission before gas off -take could commence. We wish to include your
guidance in our report due July 1, so we would appreciate your response by June 15.
Sincerely your.
/ 4.
Dave Norton, P.E.
Manager, Engineering
cc: Dan Fauske
A L A S K A G A S L I N E D E V E L O P M E N T C O R P O R A T I O N
P.O. Box 101020 Anchorage, Alaska 99510 1 411 West Fourth Avenue, Suite 1E, Anchorage 99501
Tel. 907 - 277 -4488 1 Fax 907 - 277 -4484 1 www.gasline.us.com
310
bp
•
RECEIVED
/R 2 9 ZOOS
Alaska Oil & Gas Cons. Commission
John Norman Anchor *.
Alaska Oil and Gas Conservation Commission
333 West 7 Avenue, Suite 100
Anchorage, AK 99501
RE: Conservation Order 457B (Rule 13) and Conservation Order 341D (Rule 18) —
Commingled production from the Aurora Oil Pool and Prudhoe Oil Pool in Well S -26
Dear Chairman Norman,
As set forth in Alaska Oil and Gas Conservation Commission's Conservation Orders 457B and
341D (as amended), BP Exploration (Alaska) Inc. has complied with the commingled production
of the Aurora Oil Pool (AOP) and the Prudhoe Oil Pool (POP) within well S -26 to determine a
reliable and acceptable production allocation method. Over the course of the six month
commingled test period (August 20, 2008 through February 20, 2008) BP has fulfilled the
Commission's requirements in obtaining Production Profiles, Static Bottom Hole Pressure
Surveys, Geochemical Samples and Well Tests. The results of the collected surveillance data
are included in this letter.
Please call either of us or Danielle Ohms 564 -5759 (POP) or Pat Collins at 564 -4363 (AOP) if
you have any questions or wish to discuss further.
Sincerely,
rank Paskv % Scott 'gent
Resource Manager, GPB West Resource Manager, GPB Waterflood
Attachment 1: OilTracers Report No. 09 -826 (CONFIDENTIAL)
Attachment 2: Schlumberger PL Advisor for S -26 10 -10 -08 PPROF
Attachment 3: Schlumberger PL Advisor for S -26 2 -16 -09 PPROF
1
•
History of S -26
S -26 was originally drilled and completed as a Prudhoe producer in 1990. Zone 4 Stimulations,
including both frac and acid treatments, were performed in 1991 and 1992 to maximize
production. By late 2007, S -26 was producing 200 to 250 bopd at approximately 75% watercut
and 6000 GOR from the Prudhoe Oil Pool.
Well S -26 penetrates the AOP and POP in areas where well rates from both Pools are low. A
stand alone Aurora producer in this area could not be justified due to the expected low rates and
associated problems with paraffin and hydrate deposition. A RWO to commingle production
from the two pools within the S -26 well -bore was planned to maximize oil production from the
two oil pools.
Prudhoe production was isolated on 12- 15 -07. A RWO to recomplete and enable Aurora
production was completed in January 2008. Aurora perfs were added and an initial Aurora only
SBHP was obtained on 4 -3 -08. The Aurora reservoir pressure at this time was 3615 psi. The well
was put on production on 4 -4 -08 though total fluid rates were low and the well was SI on 4 -7 -08.
An Aurora only frac placed approximately 188,000# proppant in the formation on 5/12/08. S -26
was put on production again on 5 -16 -08 with significantly increased production rates post frac
from the Aurora only. Plugs were drilled out to re -open the Prudhoe on 8- 17 -08. Commingled
production began on 8- 20 -08; it has remained commingled since.
The commingling of the Prudhoe and Aurora pools has shown to have a positive impact on oil
production from S -26. The Aurora oil production to date from S -26 is 183,500 bbls. The total
incremental commingled oil rate from S -26 (over 2007 Ivishak only production) is
approximately 600 bopd.
Results Obtained from Commingled Test
During the course of the commingled testing period, two production profiles using
Schlumberger's DEFT and GHOST tool, 7 geochemical samples, and 19 welltests were gathered
to assess performance of the Prudhoe and Aurora. PL Advisors interpreting the oil/ water and
gas splits between the pools were performed by Schlumberger, and were completely independent
from the oil Geochemical analysis performed by Oil Tracers L.L.C. Neither were privy to the
other's analysis or results. Both the PL Advisors and the Oil Geochemical Report reference the
Ivishak layer of the Prudhoe Oil Pool, so please note that reference to the Ivishak and Prudhoe
are meant to represent the same oil. The PL Advisor reports from Schlumberger are included in
the Appendix.
A summary of the Production Profile logging of the Aurora and Prudhoe Oil Pools in S -26 is
shown in Table 1.
Oil % Water % Gas %
Aurora 10/10/2008 51 16 35
2/16/2009 55 34 26
Prudhoe 10/10/2008 49 84 65
2/16/2009 45 66 74
Table 1. S -26 Aurora/Prudhoe PPROF Results
Monthly geochemical samples were collected over the commingled test period and results are
shown in Table 2. Separate end member samples of the Prudhoe oil (9/3/07 sample) and the
2
• •
Aurora oil (5 /19/08 and 5/20/08 samples), all from S -26, were used to determine commingled oil
splits. The Geochemical report from Oil Tracers L.L.C. is included in the Appendix.
Geochem
% Geochem
Prudhoe % Aurora
Date Oil Oil
8/30/08 26.83 73.17
9/18/08 51.61 48.39
10/10/08 37.09 62.91
11/14/08 46.10 53.90
12/21/08 43.81 56.18
1/5/09 59.20 40.79
2/11 /09 47.01 52.99
Table 2. S -26 Aurora/Prudhoe Geochemical Analysis Results
Reservoir pressures were obtained from the separate pools during the last period they were
produced in isolation. While the Prudhoe reservoir pressure is higher than the Aurora at face
value, if converted to the Aurora datum of 6700' TVDss assuming a water gradient of 0.44 the
pressures are very similar. Table 3 below lists the results.
Reservoir
Oil Pool Date TVDss Pressure
Prudhoe 9/23/2007 8800' 3223 psi
Aurora 4/3/2008 6700' 3615 psi
Table 3. Aurora and Prudhoe Reservoir Pressures
Welltests were conducted over twice a month during the commingled test period, and at least
once per month for the periods of individual Aurora and Prudhoe production. Prior to obtaining
PPROF data, initial commingled spills were assessed and applied to allocated pool production
based on separate zone tests. Using the 11/27/07 welltest as representative of Prudhoe only
production and the 8/1/08 welltest as representative of Aurora only, initial splits were calculated
and shown in Table 4. A summary of all welltests since 2007 is shown in Table 5.
Oil % Water % Gas %
Prudhoe split 38 94 63
Aurora split 62 6 37
Table 4. Initial Splits based on Separate Zone Tests
3
•
a ►- x
g re
rt
Well Date '
o " = O r 3 3 J J
(! 3 (7 (7 V a u. 3 0 t7 1-
S-26 3/22/2009 4 6 1358 602 756 1797 2986 94.8 222 104 55.7 3010 1305 3540
S -26 3/3/2009 4 6 1349 617 732 2197 3559 94.8 219 102 54.3 3080 1412 3912
S -26 2/18/2009 4 6 1668 792 876 6110 7712 94.9 257 98 52.5 3680 1800 5869
S -26 2/11/2009 4 6 1408 660 748 2092 3171 94.4 222 102 53.1 3060 1367 3659
S -26 2/7/2009 4 6 1408 652 756 2096 3215 94.4 219 102 53.7 3040 1357 3648
S -26 1/21/2009 4 6 1427 691 736 2055 2973 94.4 220 101 51.6 3070 1372 3591
S -26 1/5/2009 4 8 1689 906 783 2482 2740 55.5 495 108 46.4 3580 1614 3589
S -26 12/22/2008 4 6 1447 811 636 2361 2910 93.6 231 101 43.9 3510 1555 4057
S -26 12/19/2008 4 6 1514 866 648 2334 2695 93.6 230 103 42.8 3440 1525 3814
S -26 12/17/2008 4 6 1502 870 632 2385 2741 93.6 231 102 42.1 3480 1553 3905
S -26 11/25/2008 4 6 1506 870 636 2425 2788 93.7 234 103 42.2 3460 1520 3908
S -26 11/14/2008 4 6 1584 932 652 2573 2761 94.0 235 102 41.2 3520 1560 3847
S -26 10/31/2008 4 6 1497 901 596 2710 3009 92.7 228 103 39.8 3510 1548 4155
S -26 10/18/2008 4 6 1509 885 624 2750 3107 91.6 212 101 41.4 3420 1522 4089
S -26 10/4/2008 4 6 1713 937 776 2577 2751 91.7 197 107 45.3 1910 1008 2619
S -26 10/1/2008 4 6 2646 1378 1268 2569 1865 91.7 204 119 47.9 1630 975 1587
S -26 9/20/2008 4 6 1545 813 732 1815 2233 90.6 208 110 47.4 1510 883 2152
S -26 9/9/2008 4 8 1743 942 801 2208 2345 90.6 209 112 46.0 1530 921 2145
S -26 8/23/2008 4 6 2219 895 1324 3222 3599 91.2 240 119 59.7 2140 1198 2416
S -26 8/1/2008 4 6 799 719 80 1552 2157 90.6 219 74 10.0 2000 1033 4446
S -26 7/20/2008 4 6 697 653 44 1425 2182 90.6 217 72 6.3 2030 1009 4957
S -26 6/24/2008 4 6 790 722 68 1588 2200 89.3 210 80 8.6 1940 938 4466
S -26 6/6/2008 4 6 1085 989 96 1874 1896 92.4 214 82 8.9 2000 882 3571
S -26 5/21/2008 7 4 1630 1461 169 2320 1588 92.0 340 89 10.4 1400 1900 2282
S -26 5/21/2008 4 4 3145 1369 1776 2147 1569 44.8 205 74 56.5 1570 963 1182
S -26 4/5/2008 4 6 81 61 20 602 9938 94.8 189 72 24.8 1990 1338 32000
S -26 12/8/2007 4 6 898 194 704 1197 6183 94.7 211 106 78.4 1980 1456 3538
S -26 11/27/2007 4 6 909 197 712 1172 5943 94.7 218 103 78.3 1970 1225 3457
S -26 11/19/2007 4 6 916 220 696 1395 6335 94.7 208 104 76.0 2030 1226 3739
S -26 11/11/2007 4 6 941 217 724 1406 6496 94.7 205 103 77.0 2030 1239 3651
S -26 11/3/2007 4 6 978 198 780 1422 7200 94.7 197 105 79.8 2030 1244 3530
S -26 10/21/2007 4 6 961 205 756 1490 7270 59.7 288 105 78.7 2040 1307 3673
S -26 9/4/2007 4 6 1186 406 780 1425 3509 94.8 226 112 65.8 3270 1574 3959
S -26 8/12/2007 4 6 1224 288 936 1394 4841 95.0 219 116 76.5 2070 1296 2830
S -26 7/30/2007 4 6 929 201 728 1189 5928 95.0 229 112 78.4 2030 1172 3465
S -26 7/15/2007 4 6 866 242 624 1068 4415 95.0 237 107 72.1 2070 1241 3624
S -26 6/25/2007 4 6 940 212 728 1005 4748 95.0 242 105 77.5 2040 1243 3239
S -26 6/8/2007 4 6 848 216 632 976 4525 95.0 231 103 74.6 2060 1229 3580
S -26 6/1/2007 4 6 935 227 708 1155 5096 95.0 242 104 75.8 2060 1218 3439
S -26 5/9/2007 4 6 939 239 700 1104 4627 95.0 228 104 74.6 2020 1199 3327
S -26 4/21/2007 4 3 844 197 647 969 4931 95.0 236 104 76.7 2020 1103 3541
S -26 3/3/2007 4 4 909 213 696 1570 7379 94.9 245 99 76.6 2480 1263 4455
S -26 2/8/2007 4 4 802 244 558 1578 6475 94.9 244 94 69.6 2550 1267 5147
S -26 1/19/2007 4 4 804 222 582 1641 7404 94.9 224 100 72.4 2420 1237 5051
IPrudhoe only Welltests
(Aurora only Welltests
(Commingled Prudhoe and Aurora Welltests
Table 5. S -26 Welltest Data
The average oil rate over the 7 months of commingled tests shown in the welltest data table is
843 bopd. The initial commingled welltest watercut of 59.7 % is higher than average and is
attributed to the Prudhoe production cleaning up after an extend shut in period. Aside from that
initial welltest, watercuts have been on a gradual increase which is expected as both pools are
being waterflooded. A Welltest plot annotated with the periods of individual pool production and
commingled tests is shown in Figure 1.
4
•
S-26
10,000 _ =-
x T
• � _ p�
• • • Y • • • • � ;a i t .... �
W. 1,000 -- -_ -' =,-' -
O • t _ ,
C7 _��
A 100 -4 °' ° y
O
m
w 10
U
Jan -07 Apr -07 Jul -07 Oct -07 Jan -08 Apr -08 Jul - 08 Oct - 08 Jan - 09 Apr - 09
Prudhoe only welltests Aurora only Commingled welltests
-a-Gross Fluid -Oil -GOR • Gas Lift Pressure • Manifold Pressure r Manfold Temperature -1- TGLR
100.0 _ _ 100.0
iW 80 . 0 �- ��_. __ _ - 80.0 en
60.0 ~ �, • 60.0 m
m 40.0 0 40.0 m
0.
20.0 _ 20.0 °
0.0 r 0.0
Jan -07 Apr -07 Jul -07 Oct -07 Jan -08 Apr -08 Jul -08 Oct -08 Jan -09 Apr -09
-e- Water Cut -+- Choke
Figure 1. S -26 Welltest Plot
Conclusions
A summary of the allocated production reported for both the Aurora and Ivishak pools to date is
shown in Table 6. The high Aurora oil split in August is due to S -26 being produced Aurora
only until 8/20/08 when production between the 2 pools was commingled. Engineered splits
were applied in September and October until the 10/10/08 preliminary PPROF results were
applied starting in November. Final PPROF analysis results were applied starting in January
2009. The 2/16/09 PPROF results were applied to allocated production starting in March 2009.
Oil Prod Water Prod Water Gas Prod Gas Prod
Oil Prod Rate Rate Aurora Prudhoe Rate Prod Rate Aurora Prudhoe Rate Rate Aurora Prudhoe
STB /DAY S- STB /DAY S- Oil split Oil Split STB /DAY S STB /DAY Water Water MSCF /DAY MSCF /DAY Gas split Gas
Date 26_AURA 26_PBU % % 26 AURA S -26 PBU split % Split % S -26 AURA S- 26_PBU % Split %
8/31/2008 526 121 81.3% 18.7% 53 317 14.2% 85.8% 918 446 67.3% 32.7%
9/30/2008 400 245 62.0% 38.0% 42 661 6.0% 94.0% 531 904 37.0% 63.0%
10/31/2008 560 343 62.0% 38.0% 45 713 6.0% 94.0% 1012 1723 37.0% 63.0%
11/30/2008 413 372 52.6% 47.4% 95 499 16.0% 84.0% 701 1707 29.1% 70.9%
12/31/2008 355 320 52.6% 47.4% 88 463 16.0% 84.0% 631 1538 29.1% 70.9%
1/31/2009 409 393 51.0% 49.0% 100 528 16.0% 84.0% 736 1368 35.0% 65.0%
2/28/2009 313 301 51.0% 49.0% 104 548 16.0% 84.0% 1248 2317 35.0% 65.0%
3/31/2009 299 245 55.0% 45.0% 224 435 34.0% 66.0% 679 1933 26.0% 74.0%
Table 6. S -26 Monthly Allocated Production
Based on the allocated production splits, the Prudhoe formation GOR increased in February and
March to approximately 7800 scf /stbo. This corresponds with MI injection into Prudhoe injector
S -20A in November through December of 2008 and interaction time with S -26 is typically 3
months. MI interactions between S -26 and offset Prudhoe injectors S -20A and S -06 are fairly
5
well established and are expected to be recognizable when they occur. These wells are not on
MI often as the area is becoming mature for MI in the Prudhoe oil pool.
A comparison of the commingled oil splits from both the production profiles (data from Table 1)
and Oil Geochemical fingerprinting (data from table 2) is presented in Figure 2. Oil production
splits were obtained from the commingled geochemical samples and are in close approximation
with the Production profile logging results. The geochemical sample obtained on 10/10/08 and
the PPROF started on 10/10/08 were over 10 hours apart. Flucuations in gas lift rates and well
head pressures can have an impact on oil production splits from the 2 zones, thus the slight
variation in the more frequent Geochemical analysis.
S -26 Aurora vs. Ivishak Oil Splits
100.00 - _
80.00
60.00 -
40.00
20.00
0.00
8/1/08 8/31/08 9/30/08 10/30/08 11/29/08 12/29/08 1/28/09 2/27/09
Geochem % Aurora Oil - Geochem % Prudhoe Oil
10/10/08 PPROF Aurora Oil % 10/10/08 PPROF Ivishak Oil %
a 2/16/09 PPROF Aurora Oil % 2/16/09 PPROF Ivishak Oil %
Figure 2. S -26 Comparison of Oil Geochem and PPROF Splits
Oil production splits were obtained from the commingled geochemical samples and are in close
approximation with the Production profile logging results. The geochemical sample obtained on
10/10/08 and the PPROF started on 10/10/08 were over 10 hours apart. Flucuations in gas lift
rates and well head pressures can have an impact on oil production splits from the 2 zones, thus
the slight variation in the more frequent Geochemical analysis. The average Aurora oil split over
the commingled test period from the 2 PPROF's was 53 %. This is very closely matched by the
average of the geochemical analysis Aurora oil split of 55% (for all 7 samples) or 53%
(excluding initial sample when Prudhoe just reopened and cleaning up).
Obtaining more frequent Oil Geochemical samples is preferred over the more intrusive PPROF
logging. Geochemical analysis provides quicker insight to production changes between the
pools that may occur in the future. It also reduces risk by minimizing running into the well with
tool strings. Occasional PPROFs or separate zone tests may be needed to determine water and
6
• •
gas splits between the 2 zones that are not readily explained by injection changes in interacting
offset injectors.
Based on the good agreement between the methods of measuring Aurora and Prudhoe oil splits,
BP believes that geochemical analysis has been demonstrated to provide an accurate and
appropriate method of allocating oil between the two pools. Therefore, BP proposes that from
May 1, 2009 forward, geochemical fingerprinting be utilized for oil allocation purposes. The
geochemical sampling frequency will be twice per year and not less frequently than every 7
months. When major changes in production characteristics occur, which cannot be readily
explained by changes in offset injectors for either Pool, a production log will be obtained to more
accurately allocate the water and gas production.
Sincerely,
Frank Paskvan / Scott Digert
BPXA GPB Subsurface Resource Managers, WEST / WF
BP Exploration (Alaska) Inc.
P.O. Box 196612
Anchorage, AK 99519 -6612
7
• •
CONFIDENTIAL MATERIALS
HELD IN CONFIDENTIAL ROOM
•
•
bp
::
0 Schiumber
PL Advisor
Production Log Interpretation
With GHOST and DEFT
Company : BP Exploration (Alaska), Inc.
Field : Prudhoe Bay
Well : S -26
Date Logged : 16- Feb -2009
Date Processed : 12- Mar -2009
Reference Number : AYTU -00014
API Number : 50- 029 - 22047 -00
Log Analyst : Erika Bowen
Alaska Data and Consulting Services
2525 Gambell Street, Suite 400
Anchorage, Alaska 99503
(907) 273 -1700
411 interpretations are opinions based on inferences from electrical or other measurements and we cannot, and do not guarantee the accuracy or correctness of any interpretations and
we shall not, except in the case of gross or willful negligence on our part, be liable or responsible for any loss, cost, damages or expenses incurred or sustained by anyone resulting
from any interpretation made by any of our officers, agents or employees. These interpretations are also subject to clause 4 of our general terms and conditions as set out in our current
'rice schedule.
• •
BP Exploration (Alaska), Inc. Well: S -26
Job Number: AYTU -00014 Field: Prudhoe Bay
1. Production Logging Objectives:
The objective of this logging suite was to evaluate production splits between the Aurora and Ivishak pools.
Three phase production interpretation was performed to determine oil, gas, and water splits.
2. Main Results:
Table 1: Interpreted Downhole Rates from multiphase solver.
Tot.DH Oil Gas Water
Pool Perforation prod. % Rate % rate % rate ok
From, ft To, ft B/D B/D B/D B/D
Aurora 6870 6894 1695.8 31.30% 404.4 55.00% 1034.2 26.30% 257.2 34.10%
Ivishak 8951 9053 3726.8 68.70% 331.4 45.00% 2899.1 73.70% 496.3 65.90%
8951 8960 2594.0 47.8% 189.5 25.8% 2404.5 61.1% 0.0 0.0%
8965 8990 539.6 10.0% 123.4 16.8% 395.1 10.0% 21.1 2.8%
8995 9012 593.5 10.9% 18.6 2.5% 99.8 2.5% 475.1 63.1%
Below 9012 Trace Trace Trace Trace
Total: 5422.6 735.8 3933.3 753.5
Table 2: Interpreted Surface Rates converted from downhole rates.
Gas Water
Pool Perforation Oil Rate rate rate
To,
From , ft ft STB /D % Mscf /D % STB /D %
Aurora 6870 6894 359.8 55.40% 385.2 26.70% 250 34.30%
Ivishak 8951 9053 289.7 44.60% 1059.1 73.30% 479 65.70%
8951 8960 167.2 25.7% 854.4 59.2% 0.0 0.0%
8965 8990 104.1 16.0% 218.2 15.1% 20.3 2.8%
8995 9012 15.7 2.4% 56.7 3.9% 456.3 62.6%
Below 9012 Trace Trace Trace
Total: 649.5 1444.3 729
* *Splits within the Ivishak are as requested. Zonation within a flowing interval has higher uncertainty due
to instability in the flow regime.
Surface rates on the day the product log was acquired were:
792 bpd oil; 876 bpd water; 1610 mscf gas
2
•
BP Exploration (Alaska), Inc. Well: S -26
Job Number: AYTU -00014 Field: Prudhoe Bay
3. Production Log Interpretation:
BP Exploration (Alaska), Inc. (BP) well S -26 is a producing well located in Prudhoe Bay field. This well is
producing from two separate pools, the upper Aurora (Kuparuk) and lower Ivishak (Prudhoe Bay). The
Ivishak is producing from a perforated 7.0" cemented liner with open perforations from 8951 -9053 MD. The
upper Aurora pool is producing from a 9.625" cemented casing open from 6870 -6874. 4.0" tubing is run
between the two intervals and above the Aurora with gas lift mandrels (see well sketch at end of report).
The S -26 well was logged with the PS Platform production logging tools consisting of gamma ray, CCL,
temperature, pressure, gradiomanometer, 2.5" continuous spinner, in -line spinner, X -Y caliper, GHOST and
DEFT. Both the upper and lower intervals were logged with three sets of up /down passes at both
production intervals (no logged continuously between due to large distance between production zones).
Station stops were recorded at 9020, 8992, 8963, 8900, 8593, 8570, 8000, and 6650 at both gas lift rates.
The well was shut in for 1 hour and two station stops were recorded at 8000 MD.
The downhole temperature and pressure at 9010 ft. are 223.9 °F and 1507 psi.
Data quality:
Field data was depth matched to open hole gamma ray recorded May 24, 1990. Data quality is high,
pressure and temperature is consistent within the logging passes indicating that well production was fairly
stable. DEFT and GHOST holdup corrections were applied.
Interpretation:
Over -all downhole rates are lower than reported surface rates.
Due to the changes in ID with this completion, inflow for perforated zones was computed in the 4.5" tubing
for consistency. The increase to the 9.625" casing at the upper Aurora pool is causing apparent water
recirculation.
3
• •
BP Exploration (Alaska), Inc. Well: S -26
Job Number: AYTU -00014 Field: Prudhoe Bay
3.1. Interpretation Results: 16-Feb-2009 Survey
The figure below shows cumulative production along with comparison between the reconstructed curves and stacked
input curves for the full interval.
Depth ell Sketc Z Density match Gas holdup match Water holdup match Velocity match QZT Q
(ft) (in) 0 glcc 1.2 0 1 0 1 -50 fVmin 350 -500 BID 6500 -500 B/D 6500
7 ?W4 G -
6700 I r- ����� ,, II
6800 MM 11! A
7000 1.1111111111111111 MO= ■
Mt 1 •PIIIMIIIIMIIIIIralliall III um
MR • NIB
I III I Mil III
IN 1 111111111MMEM11111111 II 1.
PI II MI= III MI
NI MEI MI IN
rt mum . al ' mu IN
11 : t - NM . •
8000 - �I- . El II
II MIE11111111=1111
NW µ - ��� murimmr. 'r 1111
PI ' 11111111111111, IIMME
r IN
9000 =_ �I All
IN 4111111111M1=■1111M1111 I 11 t -- I I I
4
• •
BP Exploration (Alaska), Inc. Well: S -26
Job Number: AYTU -00014 Field: Prudhoe Bay
16- Feb -2009: Cumulative production and reconstruct overlays for the upper Aurora and lower Ivishak pools.
Depth Vell Sketc Z Density match Gas holdup match Water holdup match Velocity match QZT a
(ft) (in) 0 g/cc 1.2 0 1 0 1 -50 ft/min 350 -500 B/D 6500 -500 BAD 6500
- 7.8Tc�74 FP -5,11 Y' *"J EFT 3511 VASP I 35,11
_ _ 1 1
1 l
- - 6700 - i'
— — I ,.
i
- - 6800
-.4. ♦'
-6900 C
-_ - i
•
- 7000 -
•
- 7100 - I $$ •
- - -
— - — I f
_ I ¢¢
- - 7200 -
Dept Vell Sketc - Density match Gas holdLp - notch Water holdup matcr Velocity matcr QZT a
(ft) (in) 0 dcc 1 2 0 1 C 1 -50 ft/min 550 -500 B/D 6500 -500 B/D 8500
- 7.87W4 D ' 511 - _.,
- X
- 870)
' r - _ . _.
—
- 6'
q1
- 3300 - y is it
R {(
— 7
t
- - 890J I i
r i
_
1
— 900J —
I I
I I
910)
I * 1 I
■ I
I
— 920) f
5
III
BP Exploration (Alaska), Inc. Well: S -26
Job Number: AYTU -00014 Field: Prudhoe Bay
16- Feb -2009: Correlation display for the upper Aurora and lower Ivishak pools..
tsp. Well View #1 II Sk- Z GR TENS CCLD ID ER 21 PFC2
(ft) (g - >Top) (in) 0 GAPI 450 500 lb 1500 -8 8 -5 in 6 8 in 0 0 in 8
9'. te
1 -
-
, \ i ce 4. III ...?
_, ,
i 4 .1.• pm
1
I
S
,i.
•11 I j
1
I
I i 11 1 t ti , i I ! ;IP
,,,
...
,
1 il ,
s
t 61=10
1 fss '; I
,i
y
lPi
1.
� a j }
W e View Y1 115k- L GR TENS CCLD ID PFD 1 PFC2
(ft-> ToF) (in) 0 GAPI 457 500 b 1500 -0 8 -E. i 6 0 in 0 0 in 8
I
I I
i
i I
I
1
mi
i
I
t� � I
J 11
1
I
I1.
6
•
•
BP Exploration (Alaska), Inc. Well: S -26
Job Number: AYTU -00014 Field: Prudhoe Bay
19- Feb -2009: PSP sensors up and down passes overlay display for the upper Aurora and lower Ivishak pools
Depth ell Sketc Z GR WPRE WTEP UWFD SPIN SCVL
(ft) (in) 0 GAPI 450 900 psia 1120 182 °F 210 0.2 glee 1 -10 rps 45 -120 ib/min 120
- - ,:„ 1
-_ - r �
'_6700- .'`
I Ii it; 1f
-= --- 1 I ll t ' '
-6800- \ ¢ - --
T
I I11!
8900 i -700 0-
— l!t ttii
t
- 7100 - � r)
I
Y f
- - 7200 t .. 7•
Depth ell Sketc Z GR WPRE WTEP UWFD SPIN SCVL
(ft) (in) 0 GAPI 450 1380 psia 1520 214 °F 226 0.2 g'cc 1.2 -10 rps 18 -120 fUmin 120
- 8700 '
_ - ¢ f
8 0 - 0 / 4 I .,."
__;_-:---11 9°_: :_::::. ' : - a � it, 9000 I. -_ _ -__—
.'
- i i
-
5100
-
-
- 920 - 0 _
7
S •
BP Exploration (Alaska), Inc. Well: S -26
Job Number: AYTU -00014 Field: Prudhoe Bay
19- Feb -2009: GHOST down passes overlay plot. Note high water holdup due to recirculation in the 9.625 casing interval.
•ep. DFH1 DFH2 DFH3 DFH4 D1RB YW_DFT DEFT 32 D bb 32
(ft) 0 1 0 1 0 1 0 1 0 360 0 1 1 Fr 2 0 0 829 563
I.
( ( ( i : .1“,
E ' -s
.f... , i i i i I - .,
I , „... i
.,..
■
1 7l
R w.
.t. ;
i c °'»
c ' 1
j r j :
f , A
}
A
I �, ♦ Ill
UFH1 UhH "l C FH3 UFHY D 1Rt3 1 "�V_Url Utr tL U CUUG '
Al
0 1 0 1 0 1 0 1 0 360 0 0 _ _ _ -, 1 2-
70. x s, .. ay
11111 ... i ....
.„
11111111 , ,,
1
,,...
_ .
4 iii
i 1 A ,
00. .______..
a
101
20
8
• •
BP Exploration (Alaska), Inc. Well: S -26
Job Number: AYTU -00014 Field: Prudhoe Bay
19- Feb -2009: GHOST down passes overlay plot
Depth GHH5 GHH6 GHH7 GHHB D1RB2 YG GHOST 32 G BUB 32
(ft) 0 1 0 1 0 1 0 1 0 360 0 1 0 -1 0.75 0 a 1245.42
= 6700 — I • 'L. ,..
_ _
= f
i 4
di t
- 6800 - , w1. A.. -• -i
s f
- - , . w+ . a
Ili . .
— 6900 — _ kr
- - - - T-. X
- - lid f
- 7000 — a.'! it ; -
, , ~k
_ 7100 _ - .1 _ - \
T.
— - 7200 — .i; . 1 ) J J 4 r
_ - _ x _ w
— .
— 7300 — 4 A= — t
Depth GHH5 GHH6 GHH7 GHH8 D1RB2 YG GHOST 52 G BUB 52
( — 0 1 0 1 0 1 0 1 0 360 0 1 0 0.75 0 1 582.751
— 8700 — L
— 880 0 E r 1 ) i _
_ _ _
_ _
'. = = , - 8 900 It"-
I
— ,i'. r —
a_
= 9000 - =
i
— - 9100 —
9
•
BP Exploration (Alaska), Inc. Well: S -26
Job Number: AYTU -00014 Field: Prudhoe Bay
3.3. Spinner Calibration:
_30 •
X
_20
0
X _10 sf�:
-200 7 0 200
_ -10
_ -20
_ -30
_ -40
rps versus ft/min
Threshold ( +) 9.8 ft/min Threshold ( -) -9.8 ft /min
Calib. Zone Slope ( +) Slope ( -) Int ( +) Int ( -) Int. Diff.
ft ft /min ft /min ft/min
❑ 6707.8- 6747.7 0.089 N/A - 281.01 N/A 0.00
O 6779.2- 6839.5 0.089 N/A -50.22 N/A 0.00
+ 6914.2- 7014.1 0.089 0.090 -50.14 -63.27 13.13
X 7065.8- 7221.8 0.089 N/A - 184.34 N/A 0.00
❑ 8727.1- 8903.9 0.099 N/A -58.58 N/A 0.00
✓ 9001.2- 9011.6 0.100 0.090 -0.13 -19.98 19.85
Spinner Calibration plot.
10
•
•
BP Exploration (Alaska), Inc. Well: S -26
Job Number: AYTU -00014 Field: Prudhoe Bay
3.4. Summary Table Results:
Summary table of inflow zones:
Zones 1 Zones 2 Zones 3 Zones 4 Zones 5
From , ft 6870 8951 8965 8995 9022
To,ft 6894 8960 8990 9012 9053.1
Water
FVF 1.0287 1.0362 1.0403 1.0414 1.0418
Viscosity, cp 0.357 0.3102 0.2854 0.281 0.2793
Density, g /cc 0.99 0.98 0.98 0.98 0.97
Oil +Gas
FVF 1.126 1.144 1.1861 1.1881 1.1892
Viscosity, cp 1.918 1.5363 1.1544 1.1319 1.1219
Density, g/cc 0.81 0.8 0.78 0.78 0.78
Gas
FVF 0.0174 0.0161 0.0114 0.0114 0.0114
Viscosity, cp 0.0141 0.0146 0.0158 0.0159 0.0159
Density, g /cc 0.055 0.0593 0.0835 0.0837 0.084
Temperature,
'F 187.13 207.28 220.44 223.09 224.08
Pressure,
psia 945.46 1056.2 1488.6 1500.2 1508.7
Diameter, in 3.958 3.958 6.275 6.275 6.275
Deviation, ° 20.1 17.7 4.93 4.88 4.81
Roughness 1.16E -04 2.53E -04 1.59E -04 1.59E -04 1.59E -04
Rs, cf /bbl 148 160 232 233 234
Rsw, cf /bbl 6 6.45 8.67 8.75 8.79
V mixture,
ft/min 267 179 20.6 10.8 0
Visc. Mixture
, cp 0.54 0.39 0.31 0.28 0.28
Vpcf 0.89 0.89 0.84 0.83 0.5
dQ res., B/D 1695.79 2594.01 539.62 593.54 0
% at 31.27 47.83 9.95 10.95 0
dQw res.,
B/D 257.21 0 21.13 475.14 0
dQw s.c.,
STB/D 250.04 0 20.31 456.27 0
dQo res., B/D 404.39 189.48 123.44 18.6 0
dQo s.c.,
STB /D 359.78 167.22 104.07 15.65 0
dQg res., B/D 1034.18 2404.53 395.05 99.8 0
dQg s.c.,
Mscf /D 385.26 854.43 218.24 56.72 0
Yw 0.248 0.309 0.786 0.954 1
Yo 0.232 0.186 0.075 0.011 0
Yg 0.52 0.505 0.14 0.034 0
Vslip, ft/min 243.443 204.263 50.854 43.702 0
Vslip W-O,
ft/min 2.553 3.776 19.855 19.952
Regime Froth /chum Slug liquid -gas Bubble Bubble No flow
Corral. Aziz and Govier Aziz and Govier Aziz and Govier Aziz and Govier Aziz and Govier
Stanford Drift Stanford Drift Stanford Drift Stanford Drift Stanford Drift
Correl. W -O Flux LL Flux LL Flux LL Flux LL Flux LL
11
• S
BP Exploration (Alaska), Inc. Well: S -26
Job Number: AYTU -00014 Field: Prudhoe Bay
4. Table of abbreviations:
Tool
Mnemonic Channel Description
Units: Description CVEL Cable velocity
CCLD /
B/D Barrels per Day CCLC Casing Collar Locator Discriminated / Calibrated
DFB1/2/3/
scf /bbl Standard Cubic Feet per Barrel 4 DEFT bubble count per probe
DFH1 /2/3/
cp Viscosity centipoises 4 DEFT water holdup per probe
ft/m Feet per minute SCV1 Depth corrected cable speed to in -line spinner
g /cc Grams per cubic centimeter SCVL Depth corrected cable speed to spinner
MMSCF /D Million Standard Cubic Feet per Day GHHM2 Field calculated combined gas holdup
MSCF /D Thousand Standard Cubic Feet per Day DFHM Field calculated combined water holdup
Res. To denote reservoir conditions (downhole) MWFD Field pressure derived density
rps Revolutions per second GR Gamma Ray
GHB1 /2/3/
S.C. To denote surface conditions (uphole) 4 GHOST gas bubble count per probe
GHH1 /2/3/
SCF Standard Cubic Feet 4 GHOST gas holdup per probe
STB /D Stock Tank Barrels per Day SPI1 In -line spinner
WPRE Pressure
PVT: Pressure Volume Temperature DPHZ Pressure derived density (from Emeraude)
Bo Oil volume factor PFC1 / PFC2 PSP Caliper 1 and Caliper 2
Bw Water volume factor Q Rate
Relative bearing for probe 1 of second tool
Bg Gas volume factor D1 RB2 (GHOST)
FVF Fluid volume factor D1 RB Relative bearing of probe 1
GOR Gas Oil Ratio SPIN Spinner (fullbore or turbine)
Watercut Ratio of produced water to total fluids WTEP Temperature
Holdup Fraction of fluid present in an interval of pipe TENS Tension
Uncorrected Fluid Density (from
UWFD gradiomanometer)
Interpretation: WFDE Well fluid density (from gradiomanometer)
Correlation Model L -G: Liquid Gas W -H: Water
Correl. Hydrocarbon; O -W Oil -Water
ID Internal Diameter PSP Production Services Platform
Q Cumulate Rate with continuous solution DEFT Digital First Entry Tool (Water holdup)
QZI Incremental rate per zone GHOST Gas Holdup Optical Sensor Tool (Gas holdup)
QZT Cumulative Rate track with zonal contribution
Regime Modeled Spinner Calibration:
Slope of rps/ (ft/m). Defines conversion of
YG Gas Holdup Slope spinner to velocity.
YO Oil Holdup Int Intercept of line of slope (defines velocity)
Difference between up /down passes. This is the
YW Water Holdup Threshold velocity required to initiate rotation of the spinner.
YW DFT Water Holdup from DEFT
Z Zone:
Yellow - spinner calibration
Red - Perforation
White - Inflow Zones
Gray: Calculation (stable) zone
•
12
• •
BP Exploration (Alaska), Inc. Well: S -26
Job Number: AYTU -00014 Field: Prudhoe Bay
5. Tool Diagram:
MH-22 6 48.9
MH-22
AH - SAG G 47.3
AH u
EQF - 43 1 45.8
EQF
EQF - 43 1 39.8
EQF
EQF - 43 33.8
EQF-43
Detail MT
TelStatus
CTEM .L _ 27.8
PSPT - A/B 27.8
PSC-A
PSPT -A
PSTC 876
PBMS -A 772 GR _ 24.1
10k Sapphire_Mano
RT6 Thermometer
GR — Well Temp 21.0
CCL Manometer 20.9
PBMS CCL 20.3
PBMS PSTC 19.6
PGMC - A/B ACCE 19.6
PGMC -B 852 Gradioman _ 18.1
Accelero
PSOI Gradio
PGMC 14.8
PILS - A 14.8
PI LS 870 Spinner _ 132
GHOST - A2 12.3
Flowmetor Probes
Relative Bearing
Caliper
GHOC -C 701 GHOST2 Pr 7.2
GHOH -C GHOST2 Ca 7.1
GHOST2 Ca 5.1
PFCS Spin - .�
PFCS Cali 1.9
PFCS - PFCS Prob 0 1 5.1
Holdup Probes GHOST2 Wa HV
Spinner 2.5 GHOST2 Re
Relative Bearing PFCS Wave
Caliper PFCS Rela
PFCC -A 856 PFCS Cart
PFCH -A 856 Tension /' 0 .0
TOOL ZERO
MAXIMUM STRING DIAMETER 1.69 IN
MEASUREMENTS RELATIVE TO TOOL ZERO
ALL LENGTHS IN FEET
13
1 11/ III
BP Exploration (Alaska), Inc. Well: S -26
Job Number: AYTU -00014 Field: Prudhoe Bay
6. Well Schematic:
TREE = 4" OW SAFETY NOTES: NOTIFY GC OF ANY WELL
OPCDCRATION t
A S
TUATOR 0115 -26 EROSION RATEST03' SKID PLO POTENTIAL
KB. ELEV = 05.09' V EROSION) ""GMLOMETBG "PIMIOLE LEAK IN 9 -3/8'
B. ELEV= - 3749' USG' / 7200 - 8484'°"
KOP= 4400'
M9 =2 @51 2029' H4- 1/PF$SX NP. ID= 3.813'
i5idurninc - _ 3073'
Detwn T\/D- 0000' 0.S
GAS LIFT ALAtJCRES
120' CONDUCTOR, D =? H 110' ST MC TVD CEV TYFE VLV LATCH PORT DATE
I
4 3635 3635 0 MNAG DONE PK 16 05/14/08
13 -3'8" MG, 686, L - 30 BUTT, D - 12015' H 26$3' 3 5304 5251 23 MC DMY PK 0 04/ 181/08
2 6217 6094 22 MMG M fXAY PlC 0 05/27106
(4.1 /2 "SYA/PHONYGUASEw /1-WREIC =3.94" H 6608' I 1 6537 6391 21 MMG SO PK 22 05/27/08
I 611/ H" its X rip, = 3.813- I
Minimum ID = 3.80" @ 8613' _ _
4 - 1/2" OTIS XN NIP, MILLED OUT �� I
6691' &518'X4- 1 /2'BKRS -3 PKR, IO= 3.875'
I 6715' H4- 112" HES X NP, ID= 3 813" I
4 -1/2" TBG, 12. 6#x, 13CR VAM TOP. H 6780'
.C152 bpf, ID = 3.958"
6780' H4 112" W1LEG, ID= 3.958' I
PN HOLE LEAK f4 9.5/8" CSG '
(8E1-IND LOWER ISOLATION STRINGI PM �. 7042' — 19 -518' X 4 -1/2' BKRS -3 PKR, 0= 3.875" I
4 -112" TBG. 12.611, 13CR VAM TOP. --I 8515' • 7066' h11 2" HES X, ID= 3:813" I
.5152 bpf, ID= 3.958"
1A-1`2" TBG STL£ (12 /2607) 8520' 8531' 9 5/8" X 4 1/2' UNIQUE OVERSHOT I
0:4 ,—. 8540' H 9 618' X 4 1/2' OTIS PKR IC - 3.85" 1
ITOP OF 7' LNR 111111a1111 8570' 9-5/6" X r" 198< HUH, U = Z I
I 8593' H4.12" PARYJ3tSWS MP, D =3..813' I
1 8613' I - 1 /2 " Uf6XN NP, MLLhL IL) 3.80"(12(38/0.') I
4 -112" 76G. 126#, L E0 TDS, . 0152 bpf, I D = 3.958" 8625' 4 -1 /2' WA_EG,10 = 3.958'
I c -5)8" (:SC,, 4711 NM' MSCr T) = f. 681" H 8818' I e62r H ELMDTT LOGGED 08/15'90 I
F'ELI-URA I ION SUTAMA KY
PEP LOG SNS EIFICS ON 05/24/x0
ANGLE AT T P F 19' @ 6879'
NA.k. R of xi Pi Wuaun DG for hisLLxLai pelf data I 9030' H7" 20NA- IS0 .ATION P144, (07/28/07) I
SIZE: NI- N :L)RVAL Orrt/ SW DA IC
3.3/3" 4 6870 - 6894 0 04/73/08
3 -3/3° 4 8951 - 8961 0 08/26)90 `7 9139' I— FSH- BKR ECP, SCOOP G1A)E5,
3.:1//3' 4 8965 - 9053 C 08p6/90 • RLRNNC TOOL, A NO OLD BP
3 3/3' 4 9085 9130 S 00/10/94
3 -3/3' 4 9184 - 9186 S 09/10,94 I 9178' H 7" MA RKERJC4NT 1
P670 i TAG'S 01 /17,93) ma.
ONOM
17" LNR, 280,L-80 LUIS, 0283 bpf, D = E276" H 943(
DATE REV BY CCNIVENTS DATE REV BY COMMENTS FRJCHOE3AY UNT
08/04/90 N1IX ORIGINAL COMPLETION 05/14,08 KSB/TLH GLV G0 WELL 5-.26
01)02108 014 RWO 0501416 BAV/Tr) GLV on (5'77)00) FFRMT Uir x 1900581
04/C6/06 FR / SV PERFORATIONS (04)03100) 07/0208 01-1YYPJC DRLG DRAFT CORRECT10NS API 'Jo 50- 029 - 22047 -DC
04/50/00 DAV /PJC GLV CIO 09195,00 -A5PJC PULL rASDRLL (00/17/00) MC 35, T121 R12C 1335 rNL & 110C fWL.
04/0/08. KS8YPJG GLV U/U
05159/08 ?/ PJC DRLG DR4FTCORRECTIONS BP Exploration (Alaska)
14
• S
bp
oy. $ cblumberger
PL Advisor
Production Log Interpretation
With GHOST and DEFT
(Revised Format — April 2009)
Company : BP Exploration (Alaska), Inc.
Field : Prudhoe Bay
Well : S -26
Date Logged : 10 -Oct -2008
Date Processed : 30 -Oct -2008
Reference Number : 12017505
API Number : 50- 029 - 22047 -00
Log Analyst : Erika Bowen
Alaska Data and Consulting Services
2525 Gambell Street, Suite 400
Anchorage, Alaska 99503
(907) 273 -1700
All interpretations are opinions based on inferences from electrical or other measurements and we cannot, and do not guarantee the accuracy or correctness of any interpretations and
we shall not, except in the case of gross or willful negligence on our part, be liable or responsible for any loss, cost, damages or expenses incurred or sustained by anyone resulting
from any interpretation made by any of our officers, agents or employees. These interpretations are also subject to clause 4 of our general terms and conditions as set out in our current
'srice schedule.
• •
BP Exploration (Alaska), Inc. Well: S -26
Job Number: 12017505 Field: Prudhoe Bay
1. Production Logging Objectives:
The objective of this logging suite was to evaluate production splits between the Aurora and Ivishak pools.
Three phase production interpretation was performed to determine oil, gas, and water splits.
2. Main Results:
Table 1:3.5 MMSCF Gas Lift: Interpreted Downhole Rates from multiphase solver.
Tot.DH Oil Gas Water
Pool Perforation prod. % Rate % rate % rate %
From, ft To, ft B/D B/D B/D B/D
Aurora 6870 6894 1717.4 36.07% 297.9 51.40% 1367.9 35.39% 51.6 16.31%
Ivishak 8951 9053 3043.4 63.93% 281.7 48.60% 2496.9 64.61% 264.8 83.69%
8951 8960 2588.2 54.4% 226.2 39.0% 2362.1 61.1% 0.0 0.0%
8965 8990 187.6 3.9% 52.7 9.1% 134.9 3.5% 0.0 0.0%
8995 9012 267.6 5.6% 2.8 0.5% 0.0 0.0% 264.8 83.7%
Below 9012 0.0 0.0% 0.0 0.0% trace trace
Total: 4760.8 579.6 3864.8 316.4
Table 2: 3.5 MMSCF Gas Lift:lnterpreted Surface Rates converted from downhole
rates.
Oil Gas Water
Pool Perforation Rate rate rate
To ,
From , ft ft STB /D % Mscf /D % STB /D %
Aurora 6870 6894 263.4 52.60% 527.9 29.06% 50.3 16.51%
Ivishak 8951 9053 237.4 47.40% 1288.7 70.94% 254.3 83.49%
8951 8960 190.7 38.1% 1208.1 66.5% 0.0 0.0%
8965 8990 44.3 2.6% 77.8 4.3% 0.0 0.0%
8995 9012 2.4 0.1% 2.8 0.2% 264.8 86.9%
Below 9012 0.0 0.0% 0.0 0.0% trace
Total: 500.8 1816.6 304.6
2
•
BP Exploration (Alaska), Inc. Well: S -26
Job Number: 12017505 Field: Prudhoe Bay
Table 3: 2.1 MMSCF Gas Lift: Interpreted Downhole Rates from multiphase solver.
Tot.DH Oil Gas Water
Pool Perforation prod. % Rate % rate % rate
From, ft To, ft B/D B/D B/D B/D
Aurora 6870 6894 1742 35.79% 237.6 40.83% 1443 36.46% 61.5 18.77%
Ivishak 8951 9053 3125.6 64.21% 344.3 59.17% 2515.1 63.54% 266.2 81.23%
8951 8960 2650.0 54.4% 276.2 47.5% 2373.8 60.0% 0.0 0.0%
8965 8990 206.3 4.2% 65.6 11.3% 140.7 3.6% 0.0 0.0%
8995 9012 269.2 5.5% 2.5 0.4% 0.6 0.0% 266.2 81.2%
Below 9012 0.0 0.0% 0.0 0.0% trace trace
Total: 4867.6 581.9 3958.1 327.7
Table 4: 2.1 MMSCF Gas Lift:lnterpreted Surface Rates converted from downhole
rates.
Oil Gas Water
Pool Perforation Rate rate rate
To ,
From , ft ft STB /D % Mscf /D % STB /D
Aurora 6870 6894 210.4 41.97% 537.7 29.36% 59.8 18.95%
Ivishak 8951 9053 290.9 58.03% 1293.6 70.64% 255.7 81.05%
8951 8960 233.5 46.6% 1208.3 66.0% 0.0 0.0%
8965 8990 55.3 11.0% 82.3 4.5% 0.0 0.0%
8995 9012 2.1 0.1% 3.0 0.2% 255.7 81.0%
Below 9012 0.0 0.0% trace trace
Total: 501.3 1831.3 315.5
3. Production Log Interpretation:
BP Exploration (Alaska), Inc. (BP) well S -26 is a producing well located in Prudhoe Bay field. This well is
producing from two separate pools, the upper Aurora (Kuparuk) and lower Ivishak (Prudhoe Bay). The
Ivishak is producing from a perforated 7.0" cemented liner with open perforations from 8951 -9053 MD. The
upper Aurora pool is producing from a 9.625" cemented casing open from 6870 -6874. 4.0" tubing is run
between the two intervals and above the Aurora with gas lift mandrels (see well sketch at end of report).
The S -26 well was logged with the PS Platform production logging tools consisting of gamma ray, CCL,
temperature, pressure, gradiomanometer, 2.5" continuous spinner, in -line spinner, X -Y caliper, GHOST and
DEFT. Both the upper and lower intervals were logged with three sets of up /down passes at two different
rates of gas lift, first at 3.5MMSCF gas lift, than allowed to stabilized for 3 hours and logged at 2.1 MMSCF
gas lift. Station stops were recorded at 9020, 8900, 8593, 8570, 8000, and 6650 at both gas lift rates. The
well was shut in for 1 hour and two station stops were recorded at 8000 MD.
Surface rates were recorded as 2.4 MMSCF formation gas, 800 BOPD, and 560 BWPD at 3.5 MMSCF gas
lift and 2.4 MSCF formation gas, 940 BOPD, and 550 BWPD at 2.1 MMSCF gas lift.
The downhole temperature and pressure at 9010 ft. are 223.8 °F and 1519 psi at 3.5 MMSCF gas lift;
223.8 °F and 1508 psi at 2.1 MMSCF gas lift.
3
• •
BP Exploration (Alaska), Inc. Well: S -26
Job Number: 12017505 Field: Prudhoe Bay
Data quality:
Field data was depth matched to open hole gamma ray recorded May 24, 1990. Data quality is high,
pressure and temperature is consistent within the logging passes indicating that well production was fairly
stable. Variation within the station stops was less than 5 psi pressure, and under 10 rps change on
spinners.
DEFT probe #3 was not working after the first set of up /down passes at the Aurora pool at 3.5 MMSCF gas
lift. DEFT probe #3 was removed from the water holdup computation for the remaining passes.
Additionally a few minor spikes in DEFT and GHOST holdups data were removed to aid in stacking passes.
Interpretation:
Data indicated mostly standing water column at base of well up to 8958 MD. Spinner, density, DEFT, and
GHOST indicate close to sump (no -flow) conditions below 9000MD.
Over -all downhole rates are lower than reported surface rates.
For the Ivishak interval, it was requested to break down the inflow into sub - zones. Since there are no
stable intervals the division of production is suspect to higher uncertainty. From data indicators the lowest
entry at 8998MD is majority water and some oil. The entry at 8974MD is predominately oil, and the main
gas contributor is the upper perforation at 8951- 8961MD. Spinner response indicates fluid recirculation in
the 7.0" casing interval below the 4.5" tubing.
Due to the changes in ID with this completion, inflow for perforated zones was computed in the 4.5" tubing
for consistency. The increase to the 9.625" casing at the upper Aurora pool is causing water to drop out
and recirculate in this interval. This is shown with the high water holdups and spinner response. Since
water is recirculating in this interval before lifting again in the 4.5" tubing the water attributed to this zone
has a higher uncertainty.
There is approximately only a 10 psi pressure change between 3.5MMSCF gas lift and 2.1 MMSCF gas lift.
There is less than 2 rps difference in spinner response also. Apparent downhole rates between the two
sets of surface gas lift rates are essentially the same.
There was no enough downhole rate variation with change in surface gas lift rates for a SIP (selective
inflow performance) plot to be generated.
4
• •
BP Exploration (Alaska), Inc. Well: S -26
Job Number: 12017505 Field: Prudhoe Bay
3.1. Interpretation Results: 3.5 MMSCF Gas Lift
3.5 MMSCF Gas Lift: The figure below shows cumulative production along with comparison between the
reconstructed curves and stacked input curves.
I II Ske Density match Gas holdup match Water holdup match Veloc match OZT 0
tint 0 grcc 12 0 I 0 1 -50 ftfmin 350 -500 BID 6500 -1000 B/D 6000
> > U4 /FD Si, 11 - ''. 't I i- . ,6 Il VASPIN 56.11
yr S611 Y' / !OFT S6 11 VASPst47 Sell
_ IIIIM ' I1 I! -41
1 iM I MI III: 1
All
E I M1 -
1111 MINIS= ( I MI
I Ell
IN I I
_ , 1 I
It I � F
I t II
111 I � I
111 I I
11. MIMI= I I
m I I
n. I I
le I I
mr. u = I �I m
i . ,j 1 1 im
PP
f I 1 �1
N F I 1• I 1
.�r I..M AIM
t
.n. ,
5
• •
BP Exploration (Alaska), Inc. Well: S -26
Job Number: 12017505 Field: Prudhoe Bay
3.5 MMSCF Gas Lift: Cumulative production and reconstruct overlays for the upper Aurora and lower Ivishak pools.
� - - Water holdup match • QL I Q
0 g cc 1 2 0 1 0 1 -50 fVmin 350 -500 13+D 6 6500 -1000 &D 6000
JW - LI 5�z `t YGZ -> i 11 `MI DFTZ a r? VASPIN S
YG S6 11 YW DFT 5611 VASP'N7 53,11
1111 ,
r .1 11 ._.� 1 TIIIIIIIMI
I J I TI
I , , „ill,
...._.
. .....
, ,
... i
t
II V
1 11 II
..
I
11 A
i
i i � I
■
Depthell Sket Z Density match Gas holdup match Water holdup match Velocity match OZT 0
(It) (m) 0 glcc 1 2 0 I 0 1 -50 flmin 350 -500 BID 6500 -500 B/D 7000
- 7 UWFD S6 11 __ �. ,.+ li VASP1N SO 11
YG 5611 YW DFT n = ''INZ -.- SC
.
_
- - L
- - -
I
anon.
s:
- ��
1
, : : ,,, . I -* 1 I I
!ii 1 I
I I
71.
, :
pH
i I
6
• •
BP Exploration (Alaska), Inc. Well: S -26
Job Number: 12017505 Field: Prudhoe Bay
3.5 MMSCF Gas Lift: Correlation display for the upper Aurora and lower Ivishak pools..
ept Well View #1 Z ell Sketch ID PFC1 PFC2 COLD GR
(ft) (ft -> Top) iIn) -6 in 6 2 in 8 2 in 8 -6. 8. 0 GAPI 300
9500 5800 7
— 1 1 .
:,
4
:yc I
t'
T
I 1 ___ „k,
____
. _ --
1
1 It
1
1 z
i
1oc ir 1
I
i
i
Pept1 WeII View #1 Z Weil Sketcf� ID PFC1 PFC2 CCLD GR
(ft) (ft -> Top) (in) -6 in 6 2 In a 2 in 3 -3 6. 0 GAPI 300
9500 5800 -7 7
i
-- II
I
i
I I I __
i s
- -
I
- - 1
_ _ i L
3.121.75. — i
I
1 '
1 I 1—
-_
I. ,
1 I
1 ___
.6...
r
f -- S
1
7
• •
BP Exploration (Alaska), Inc. Well: S -26
Job Number: 12017505 Field: Prudhoe Bay
3.5 MMSCF Gas Lift: PSP sensors up and down passes overlay display for the upper Aurora and lower Ivishak pools
Depth Z Well Sketch 1 ID WPRE WTEP UWFD SPIN
(ft) in -6. In 6 960 psia 1110 1 -8 F 206 0 gfcc 1 -5 rps 40
I 1.
` I l
. ;,- .
— —
j
I }11
- - 11 )
- - I I
1 5 � ti.,
I ' ! f
- - �
1 ' i
- ,,,,, i l f i
.+�+ E"
! ! 1 ■ 1 I ii
Depth Z Well Sketch ID WPRE WTEP UWFD SPIN
eft) In -6 in 6 1340 psla 1540 212 F 226 0 g/cc 1 2 -15 rps 30
— — ; I
— — I
I
- n.�a. - I ;
I 4
l
El I . 1
\ I
I II
- I
1 .
n
■
8
•
BP Exploration (Alaska), Inc. Well: S -26
Job Number: 12017505 Field: Prudhoe Bay
3.5 MMSCF Gas Lift: GHOST down passes overlay plot. Note high water holdup due to recirculation in the 9.625 casing interval.
3eptt Z GHHS GHH6 GHH7 GHH8 D1RB2 YG GHOST DN20
tft) .0 2 1.2 -O 2 1 2 -0.2 1 2 -O 2 1 2 0 360 0 1 3 :; I
I I 1 1 1 1 I
1 P I ) .
I.}. / ( (
a s
s I 1
_ - _
} :79 L �. ,
(s ✓
{ i / 7 .) ,
r I
- ,,i" / ....E.
_ _
L-1,4 ( I1 ,
Depth Z GHH5 GHH6 GHH7 GHHS D1RB2 YG GHOST Dni2
(ft1 -0.2 1.2 -0 2 1 2 -0.2 1 2 -0.2 1 2 0 360 0 1 0 IF=MMIN 1
_ _ I i ji; . , II I ! r
J i. I J
I ,
i 1 I / / / '
— 1 I --I— --.1 I r f
■
I
r I; LI I
— — I I
I r
II ii � � {r
'�'�. -- �aew - -- a
l _
�,�„ { '®
9
•
•
BP Exploration (Alaska), Inc. Well: S -26
Job Number: 12017505 Field: Prudhoe Bay
3.5 MMSCF Gas Lift: GHOST down passes overlay plot
Z II Sk.e DFH I DFH2 DFH3 DFH4 D1RB Yw OFT DEFT Dn18
on; -0 2 1 2 -0 2 1.2 -0-2 1 2 -0 2 1 2 0 360 0 10 ■ 1
1 i 1 I
1 it , i I
c., _
�t- !/ I/ MIMS
1 1
— 4 �
_ a
i
x v- i zr_
,, I �
I -r - -_ "_
,. ( =
Z ISke DFH1 DFH2 DFH3 DFH4 D1RB YW_DFT DEFTDn34
(in) -02 I2 -02 12 -0.2 12 -02 12 0 360 0 1 0IMMINNE:i1
11111 I I I __ _i
i !
1 I I
, I I I
I
! 5
i j I I I :
I i I I I I
I i I I I I ~_
I I I I I i
I I
I II!
� i r
l f
-- l�s+
1 �
10
I •
BP Exploration (Alaska), Inc. Well: S -26
Job Number: 12017505 Field: Prudhoe Bay
3.2. Interpretation Results: 2.1 MMSCF Gas Lift
2.1 MMSCF Gas Lift: The figure below shows cumulative production along with comparison between the
reconstructed curves and stacked input curves.
Depth II Sket Z Density match Gas holdu• match Water holdup match Veber match QZT 0
( II) on, 0 g +cc 1 0 1 0 1 - 20 R'min 420 -500 BID 6500 -500 BID 8000
7.874 ;511 VASPIN S511
Pc'i S I YG S511 YW DM' S,'" ''ASRI/47
MN EMI
1 ■
UMW Me
IIIIMMEMER
11 C I r
IMMIM1111.0111 111
MI
.J.
a I
II --
: _-
3
e.
u
I 111011.1M.111111.1
IIIMMININIE=1111=1111 111.
T
i _
_ — a AIM
11
•
BP Exploration (Alaska), Inc. Well: S -26
Job Number: 12017505 Field: Prudhoe Bay
2.1 MMSCF Gas Lift: Cumulative production and reconstruct overlays for the upper Aurora and lower lvishak pools.
Depth ell Sket) Z Density match Gas holdup match Water holdup match Velocity match QZT 0
(ft) (in) 0 g?cc 1 2 0 1 0 1 -20 ft/min 420 -500 BD 6500 -500 BiD 8000
-7.874 VASPIN 5511
JV+°'^ - - ,, i1 < - '., S. 1 Yt. "d rIFT S5 :' VASPINZ> S°+ Ii
— — i
i I
— y
1 t I i
1 _ 1 _ _
i
_ _ ..
i ...= ,
i
_ _ 1
_ al L ,
T .-
1
-
1t :,
i .
r
i
– I
Depth ell Sket Z Density match Gas holdup match Water holdup match Velocity match 0ZT 0
( (in) 0 g+cc 1 2 0 1 0 1 -20 ftimin 420 -500 BID 6500 -500 B/D 8000
-7.874 r ,:; r_ ,5 I I VASPIN 55 i I
UWFD S r i t VG S5 I I YW DFT S511 VAST" " ::'
II
I .-� Y
t
- _
- 1 i
1i
i1 I
_ i 1
– – I
1 i
C
Y
I :
–
I I
_ _ y
I I
12
•
•
BP Exploration (Alaska), Inc. Well: S -26
Job Number: 12017505 Field: Prudhoe Bay
2.1 MMSCF Gas Lift: Correlation display for the upper Aurora and lower Ivishak pools
Depth Well View #1 Z Veil Sketcr ID PFC.) PFC2 CCLD GR
(ft) (ft -> Top) (in) - in 6 2 in 8 2 in = • 8 0 GAPI 300
9350 7500 - 874874
r .
__ r
p
i
t
_
A .
_
a t
,,,..
„,,
(i
^
1 I !
Depth Well View #1 Z Nell Sketcf ID PFCI PFC2 CCLD GR
(ft) (ft -> Top) (In) -6 In 6. 2 in 8 2 in 8 -6. 8 0 GAPI 300
7500 6000 -7 874874
:£
7-_— -. 7
— — — t
P1 : 1
i 4
ono
I _ _
i
nn --' i � lll
7
-onn
13
•
•
BP Exploration (Alaska), Inc. Well: S -26
Job Number: 12017505 Field: Prudhoe Bay
2.1 MMSCF Gas Lift: PSP sensors up and down passes overlay display for the upper Aurora and lower Ivishak pools
Dept!' Z 'ell Skett ID WPRE WT EP UWFD SCVL SPIN
(hi (in) -6 in 6 960 psis 1130 178 F 208 0 9 /cc I -120 ft/min 140 -10 rps 45
1: . 1
I
■ i ____ -�, i _
II I i I
- -
I 1 I I 1 I `
I I 1 I {+
z 1, H ' _
1 i
; i i '''H' 1 1 !
1 1 - _
! ! I I ■ !`
I 1
!
?eptF Z ellSket ID WPRE WI EP UWFD SCVL SPIN
(It) On) -6 in 6 1350 psia 1520 212 F 226 0 grcc 12 -140 ft'mui 140 -15 fps 30
J � L
-- I t I
.., {
I i
,
1 1
_=
- i
I'
- - f
----; \ ,\,..
- 1
r 1
14
• •
BP Exploration (Alaska), Inc. Well: S -26
Job Number: 12017505 Field: Prudhoe Bay
2.1 MMSCF Gas Lift: DEFT down passes overlay display for the upper Aurora and lower Ivishak pools
Depth Z DFH1 DFH2 DFH3 DFH4 DIRE YW_DFT DEFT Dn94
(ft) -0 2 1 2 -0 .2 1 2 -0 2 1 2 -0 2 1.2 0 360 0 1 0 1
T ® f, i
r ; b
—
il
1 _.
! _
_ _
....at,
n ; " i
lk
I
1 r
Isi
- - I
! j
.-:„, . -....., . 1117 , -
g i 4 1
T
1 t
i
..p. 1 -
= .....T X 31 r i
Depth Z DFH1 DFH2 DFH3 DFH4 DiRB YW_DFT DEFT Dn113
(6) -0 2 1.2 -0 2 1 2 -0 2 1 2 -0 2 1 2 0 360 0 1 0 1
- ► — �.. ' ��
r ,� 1
• z l I ,
{ , f
_ = L a 1
C t--.3 i -F ,,
- - -f ±_ )
- - rl
- _ 1
' �
r .1 T
�_ I 4
- - - � -
.- ..
1 t
n I 4
1
15
�� ��
�� ��
BP Exploration (Alaska), Inc. Well: S-26
Job Number: 12017505 Field: Prudhoe Bay
2.1 MMSCF Gas Lift: GHOST down passes overlay display for the upper Aurora and lower Ivishak pools. Note high
water holdup due to recirculation in the 9.625 casing interval.
Depth Z GHH5 *y*n Gm*" GHH8 01R62 ,s o*ooro"*^
.� 0 . o / o ` 0 / " ' 360 o . o��
_---_
���. .�� mom. �
� � | ,� � �
° = -c^__ �
_ � - / | /
- | — , / / � /
- - _ / � � �� ' --- /
[ Ii,
% ' . '' ]
_ 5 �
� � ^~^-- - !
�--- ����_ _ — —
_ — — � ~� ,.
_ _ _ ��' -,
�—. I / �� _
I r--- A.-
� � ��
__
- - -
-
�~.- r /
I i ��'
- c | ^�'
__
� � | '
-. . __- ,_
-__ ,
� � I � � ~ �, �� J __ _,~ — � =�� , 7 � ( y ' / ' |
Depth z o**o upmn GHH7 GHH8 mRBu ,G s*000"/oo
'11; 0 / v / v , v / o 360 u , n KEREM `
- -
- i ] | | |
-` ^' -����'
__ �`
1�� '� -��` _
_-
- -
.--- - -: . . . .7. _ ...
;:,-' . 1 ...... '''./.: . 4- ,. :7:
rife
`..
'
16
• .
BP Exploration (Alaska), Inc. Well: S -26
Job Number: 12017505 Field: Prudhoe Bay
3.3. Spinner Calibration:
0
_30
13
_20
® X
/P
® _10 ,
-160 44000/frary•,, 80 160
_ -10
_ -20
_ -30
_ -40
rps versus ft/min
Threshold ( +) 11.5 ft/min Threshold ( -) -11.5 ft/min
Calib. Zone Slope ( +) Slope ( -) Int ( +) Int ( -) Int. Duff.
ft ft/min ft/min ft/min
E 6715.0- 6751.0 0.089 N/A - 285.98 N/A 0.00
✓ 6783.0- 6853.0 0.098 N/A 40.49 N/A 0.00
+ 7059,0- 7179.0 0.089 N/A - 184.45 N/A 0,00
X 8585.0 - 8642.0 0.089 0.089 - 124.17 - 146.25 22.08
L1 8699.0- 8903.0 0.089 N/A -35.35 N/A 0.00
✓ 8967.8- 8984.9 0.112 0.057 -17.12 -40.12 23.00
* 9007.0- 9024.0 0.101 0.080 13.11 -9.89 23.00
3.5 MMSCF Gas Lift: Spinner Calibration plot. Default 0.089 spinner slope used in 4.5" tubing section for consistency
between flowing rates.
17
• •
BP Exploration (Alaska), Inc. Well: S -26
Job Number: 12017505 Field: Prudhoe Bay
_30 u -
X
20
0
v j .-
B ' 10 J
X
-160 160
_ -l
_ -20
_ -30
_-40
rps versus ft/min
Threshold ( +) 11.5 ft/min Threshold ( -) -11.5 ft/min
Calib. Zone Slope ( +) Slope ( -) Int ( +) Int ( -) Int. Diff.
ft ft/min ft/min ft/min
o 6715.0- 6751.0 0.089 N/A - 302.94 N/A 0.00
Q 6783.0- 6853.0 0.080 N/A -84.45 N/A 0.00
+ 7059.0- 7179.0 0.089 N/A - 199.78 N/A 0.00
X 8585.0 - 8642.0 0.089 N/A - 145.38 N/A 0.00
A 8699.0- 8903.0 0.089 N/A -44.94 N/A 0.00
✓ 8968.2 - 8988.7 0.109 0.080 -10.69 -41.41 30.72
* 9007.0- 9024.0 0.091 0.092 5.71 -17.29 23.00
2.1 MMSCF Gas Lift: Spinner Calibration plot. Default 0.089 spinner slope used in 4.5" tubing section for consistency
between flowing rates.
18
• •
BP Exploration (Alaska), Inc. Well: S -26
Job Number: 12017505 Field: Prudhoe Bay
3.4. Summary Table Results:
Summary table for 3.5 MMSCF Gas Lift.
From ,ft 6870 8951 8965 8995 9022
To , ft 6894 8960 8990 9012 9053.3
Water
FVF 1.0268 1.0389 1.0397 1.0412 1.0418
Viscosity, cp 0.3698 0.291 0.2875 0.2816 0.2791
Density, g/cc 0.99 0.98 0.98 0.98 0.97
Oil +Gas
FVF 1.1311 1.1861 1.1889 1.1911 1.1926
Viscosity, cp 1.9065 1.1738 1.149 1.1216 1.1081
Density, g /cc 0.81 0.79 0.78 0.78 0.78
Gas
FVF 0.0159 0.0114 0.0113 0.0113 0.0112
Viscosity, cp 0.0141 0.0158 0.0159 0.0159 0.016
Density, g /cc 0.061 0.0849 0.086 0.0859 0.0862
Temp. F 182.42 217.27 219.25 222.73 224.21
Press psia 1012.9 1476.6 1500.3 1511.5 1521.4
Diameter 8.681 6.275 6.275 6.275 6.275
Devi. ° 19.51 4.9 4.93 4.88 4.81
Roughness 1.42E -04 1.59E -04 1.59E -04 1.59E -04 1.59E -04
Rs, cf /bbl 164 235 238 238 239
Rsw, cf /bbl 6.42 8.6 8.73 8.8 8.86
Q tot res., B/D 5726.62 3044.4 454.8 267.63 0
dQ res., B/D 1717.44 2588.2 187.56 267.63 0
% Qt 36.07 54.36 3.94 5.62 0
Qw tot res., B/D 312.76 264.22 264.42 264.79 0
Qw tot s.c.,
STB/D 304.61 254.32 254.32 254.32 0
dQw res., B/D 51.64 0 0 264.79 0
dQw s.c.,
STB /D 50.29 0 0 254.32 0
Qo tot res., B/D 569.94 281.58 55.53 2.83 0
Qo tot s.c.,
STB /D 503.87 237.41 46.71 2.37 0
dOo res., B/D 297.87 226.15 52.71 2.83 0
dQo s.c.,
STB/D 263.35 190.7 44.33 2.37 0
Qg tot res., B/D 4843.91 2498.59 134.85 1.00E -02 0
Qg tot s.c.,
Mscf /D 1799.84 1288.67 80.59 2.81 0
dQg res., B/D 1367.93 2362.05 134.85 1.00E -02 0
dQg s.c.,
Mscf /D 527.86 1208.08 77.79 2.81 0
Yw 0.304 0.497 0.912 0.997 1
Yo 0.393 0.122 0.039 0.002 0
Yg 0.303 0.38 0.049 0.001 0
Regime Elongated bubble Elongated bubble Bubble Bubble No flow
Corral. Petalas and Aziz Petalas and Aziz Petalas and Aziz Petalas and Aziz Petalas and Aziz
Stanford Drift Stanford Drift Stanford Drift Stanford Drift Stanford Drift
Corral. W-O Flux LL Flux LL Flux LL Flux LL Flux LL
19
0 III
BP Exploration (Alaska), Inc. Well: S -26
Job Number: 12017505 Field: Prudhoe Bay
Summary table for 2.1 MMSCF Gas Lift.
From , To , ft ft ( I I I 6894 8960 8990 9012 I 2 91186
Water
FVF 1.0272 1.039 1.0396 1.0412 1.0417
Viscosity, cp 0.367 0.2911 0.2881 0.2817 0.2797
Density, g/cc 0.99 0.98 0.98 0.98 0.97
Oil+Gas
FVF 1.1295 1.183 1.1857 1.188 1.1892
Viscosity, cp 1.9106 1.1871 1.1638 1.1342 1.123
Density, g /cc 0.81 0.79 0.78 0.78 0.78
Gas
FVF 0.0161 0.0115 0.0114 0.0114 0.0114
Viscosity, cp 0.0141 0.0158 0.0158 0.0159 0.0159
Density, g/cc 0.0594 0.0828 0.0839 0.0838 0.0841
Temp. F 183.43 217.26 218.94 222.65 223.86
Press psia 1005.4 1465.6 1489.9 1501.3 1509.1
Diameter 8.681 6.275 6.275 6.275 6.275
Devi. ° 19.51 4.9 4.93 4.88 4.81
Roughness 1.41 E-04 1.59E -04 1.59E -04 1.59E -04 1.59E -04
Rs, cf /bbl 160 230 233 233 234
Rsw, cf /bbl 6.37 8.55 8.67 8.75 8.8
Q tot res., B/D 5845.62 3126.82 475.16 269.24 0
dQ res., B/D 1742.04 2649.99 206.32 269.24 0
% Qt 35.79 54.44 4.24 5.53 0
Qw tot res., B/D 324.06 265.63 265.79 266.19 0
Qw tot s.c.,
STB/D 315.49 255.66 255.66 255.66 0
dQw res., B/D 61.45 0 0 266.19 0
dQw s.c.,
STB/D 59.83 0 0 255.66 0
Qo tot res., B/D 570.39 344.15 68.05 2.45 0
Qo tot s.c.,
STB/D 505 290.93 57.39 2.06 0
dQo res., B/D 237.59 276.22 65.6 2.45 0
dQo s.c.,
STB /D 210.38 233.54 55.33 2.06 0
Qg tot res., B/D 4951.17 2517.04 141.32 0.6 0
Qg tot s.c.,
Mscf /D 1811.29 1293.6 85.3 3.01 0
dQg res., B/D 1443 2373.77 140.72 0.6 0
dQg s.c.,
Mscf /D 537.65 1208.3 82.29 3.01 0
Yw 0.307 0.474 0.902 0.997 1
Yo 0.386 0.148 0.047 0.002 0
Yg 0.307 0.378 0.051 0.001 0
Regime Elongated bubble Elongated bubble Bubble Bubble No flow
Correl. Petalas and Aziz Petalas and Aziz Petalas and Aziz Petalas and Aziz Petalas and Aziz
Stanford Drift Stanford Drift Stanford Drift Stanford Drift Stanford Drift
Correl. W-0 Flux LL Flux LL Flux LL Flux LL Flux LL
20
•
BP Exploration (Alaska), Inc. Well: S -26
Job Number: 12017505 Field: Prudhoe Bay
4. Table of abbreviations:
Tool
Mnemonic Channel Description
Units: Description CVEL Cable velocity
CCLD /
B/D Barrels per Day CCLC Casing Collar Locator Discriminated / Calibrated
DFB1 /2/31
scf /bbl Standard Cubic Feet per Barrel 4 DEFT bubble count per probe
DFH1 /2/3/
cp Viscosity centipoises 4 DEFT water holdup per probe
ft/m Feet per minute SCV1 Depth corrected cable speed to in -line spinner
g /cc Grams per cubic centimeter SCVL Depth corrected cable speed to spinner
MMSCF /D Million Standard Cubic Feet per Day GHHM2 Field calculated combined gas holdup
MSCF /D Thousand Standard Cubic Feet per Day DFHM Field calculated combined water holdup
Res. To denote reservoir conditions (downhole) MWFD Field pressure derived density
rps Revolutions per second GR Gamma Ray
GHB1 /2/3/
S.C. To denote surface conditions (uphole) 4 GHOST gas bubble count per probe
GHH1/2/3/
SCF Standard Cubic Feet 4 GHOST gas holdup per probe
STB /D Stock Tank Barrels per Day SPI1 In -line spinner
WPRE Pressure
PVT: Pressure Volume Temperature DPHZ Pressure derived density (from Emeraude)
Bo Oil volume factor PFC1 / PFC2 PSP Caliper 1 and Caliper 2
Bw Water volume factor O Rate
Relative bearing for probe 1 of second tool
Bg Gas volume factor D1 RB2 (GHOST)
FVF Fluid volume factor D1 RB Relative bearing of probe 1
GOR Gas Oil Ratio SPIN Spinner (fullbore or turbine)
Watercut Ratio of produced water to total fluids WTEP Temperature
Holdup Fraction of fluid present in an interval of pipe TENS Tension
Uncorrected Fluid Density (from
UWFD gradiomanometer)
Interpretation: WFDE Well fluid density (from gradiomanometer)
Correlation Model L-G: Liquid Gas W -H: Water
Correl. Hydrocarbon; O -W Oil -Water
ID Internal Diameter PSP Production Services Platform
O Cumulate Rate with continuous solution DEFT Digital First Entry Tool (Water holdup)
QZI Incremental rate per zone GHOST Gas Holdup Optical Sensor Tool (Gas holdup)
QZT Cumulative Rate track with zonal contribution
Regime Modeled Spinner Calibration:
Slope of rps/ (ft/m). Defines conversion of
YG Gas Holdup Slope spinner to velocity.
YO Oil Holdup Int Intercept of line of slope (defines velocity)
Difference between up /down passes. This is the
YW Water Holdup Threshold velocity required to initiate rotation of the spinner.
YW DFT Water Holdup from DEFT
Z Zone:
Yellow - spinner calibration
Red - Perforation
White - Inflow Zones
Gray: Calculation (stable) zone
21
•
•
BP Exploration (Alaska), Inc. Well: S -26
Job Number: 12017505 Field: Prudhoe Bay
5. Tool Diagram:
DOWNHOLE EQUIPMENT
MH-22 48.9
MH
SAH - G 47.3
SAH 1015
EQF - 43 1 45.8
EOF
EQF -43 ' 39.8
EOF-43
EQF -43 1 33.8
EOF-43
Dotal MT
TelStatus
CTEM 1 _ 27.8
PSPT -A/B 27.8
P3C-A
PSPT -B 870
PSTC 876
PBMS -B 878 GR _ 24.1
COG F Mono
RTD Thermometer
OR 676 Well Temp 21.1
CCL 876 COG Mranom — 20.7
PBMS 876 CCL = 20.3
PBMS PSTC 19.6
PGMC - A B 19.6
PGMC -A 1839 Gradioman _ 18.1
PSOI 3726
PGMC 14.8
PILS - A 14.8
PILS - A889 Spinner — 132
GHOST - A2 12.3
Flowmeter Probes 733
Relative Bearing 733
G
GHOST2 Ca ,/ 7.1
GHOST2 Ca 5.1
PFCS Spin
PFCS Cal 1.9
PFCS -A PFCS Prob / 5.1
Holdup Probes 762 GHOS We HV
Spinner 2.5 762 GHOST2 Re
Relative Bearing PFCS Wave
Caliper 762 PFCS Rela
PFCC -A 762 PFCS Cart
PFCH -A 762 Tension \ 0,0
TOOL ZERO
MAXIMUM STRING DIAMETER 1.69 IN
MEASUREMENTS RELATIVE TO TOOL ZERO
ALL LENGTHS IN FEET
22
BP Exploration (Alaska), Inc. Well: S -26
Job Number: 12017505 Field: Prudhoe Bay
6. Well Schematic:
TREE = 4' OW �1 ^ SAFETY NOTES: NOTIFY GC OF ANY WELL
A - RIATOR 0113 \ - f '� O OPEDERATION
T0 SKID F OWLB�E (POTENTIAL
KB. ELEV = 65.09' v
EROSION) "`"CIROMETBCi'"'PINHOLE LEAK IN 9-3/8'
BF. ELEV = 37.49' GSG N 7200 - 9464""'
KOP= 4400' I
'1a e-
xAngl23 °Q D1 7 8 ' ' ' I 2029' H4- 1/7 FiES XNP ID= 3813' 1
Datum MC = 30
Datum TVD = may SS GAS LIFTMANDRE_S
120" CONDUCTOR, D = ? H 110' ST MC TVD CEV TYPE VLV LATCH PORT DATE
4 3635 3635 0 M&MG DOME PK 15 05/14/08
13 -3'8" CSG, 8811, L -30 BUTT, ID - 12.415' 2683' 3 5304 5251 23 1,94C DMV FE 0 04118/08
2 6217 6094 22 M943 DMY PK 0 05/27/08
I4 - 1/2" SYMPHONY GL/A3Ew11 - A/RE IC = 3.94" H 6608' I M 1 6537 6391 21 WAG SO PK 22 05/27/08
I I 6670' H41/2" IBS X NI', IU= 6 -813" I
Minimum ID = 3.80" @ 8613'
4-1/2" OTIS XN NIP, MILLED OUT 6691' H9- 5 /8" X4 -1/2" BKRS -3 PKR iD= 3875' J
I 6715' H4- 112 " FESX MPH) = 3.813" I
4-1/2" TB3, 12.6A. 13CR VAM TOP. -"I 6780' l \
.0152 bpf, ID= 3 - 958"
, I 6780' H 412 "W/LEG . ID= 3.958' I
P1V HOLE LEAK Fl 9-5/8" COG -o
(BERND LOWER ISOLATION STRING) P0721 7042• H9- 5B " X4- 1 /2' BKR S -3PKR0 =3.875 I
4.1/2" TB3, 1264, 13CR VAM TOP. -{ 8515' j' I 7066' H4-1 I#S X NP, ID= 3.813' 1
.C152 bpf, ID = 3.958"
IL- 112"TBG STtE (12/29-07) H 8520' I r / 8531' "19 60 "X41 /2" UNIQUE OVERSHOT I
,-. 8540' I 518" X 4 112' OTIS FKR IC - 3.85'1
)TOP OE T LNR 1—E83757-1 8570' H 9-5)8' X /' LM( NUN, U ='/ I
I I 8593' I - 1412 " PARKER SWS NP, 0= 3.813' I
I I 8613' H4 "0113Xn NN, MLLEU it) S.80 "(12 /2t /u1) I
14- 112" TBG 126#, L-E0 TDB, . 0152 tact, i0.3.958' H 8625' I — ' I 8625' H4.12" W/LEG, D= 3.958' I
1 E-5I8" CSG, 478 NTBr ntscr, O = A 6411" H 8816'
8627' H ELMOTTLOGGE006/15'9C I
PEKI-ORA I ION SLIMA KY
REF LOG SWS 131 - CS ON 05/24/60
ANGLE AT TOP FEFF: 19' (c) 6873'
NJte. Rut ,u R r-duotiun DB for I/iatta Lral pert data I 9030' H7" ZONA ISO.ATION PKR (07/28/97) I
SILL BPI IV'. EKVAL OprVSg3 DA I_
3 -3/3' 4 8870 - 8894 0 04/33/08
3 -3/3" 4 8951 -8961 0 08/26/90 -I 9139' 1- FBH- BKR ECP. SCOOP GUDES,
3.314° 4 3965 -9063 C 08fl6U90 • RUVN*40 TOOL. AND OLD BP
33/3° 4 9085 - 9130 S 09/10194
3 -3/3" 4 9184 - 9186 S 09/10/94 I 9178' 1-1 7" MARKER JC4M 1
iPBTDiTAG:E001 /17,93) li 9 ,, ♦ , ♦ , ` , , ., 4 ,.,
17° LNR 2811, L -80 343, .0293 bpf, 13= 6.276° H 943d'
1
DATE REV BY COMMENTS DATE RE)/ BY COWE4TS PRJGNOE SAY UNIT
06/04/90 N18E ORIGINAL COMPLETION 05/14,08 KSB/71H GLV GO WELL 5-26
01/02/08 014 RWO 0601;06 - )AVT1 T) Cl V CIO (5'27 +09) PERMIT Vn F 1900531
04 /C6/06 FRCI SV PERFORATIONS (04103/08) 0710208 DHCVPJC DRLG OFAFT CORRECTIONS API Vo. 50- 029 - 22047 -0C
04 /CO /00 DAV /PJC GLV 010 09'36,00 - AR/PJC MLL (A00RILL (00/17/00) 3CC 35, T12N, R12E, 1335 PHI 8116C' IVA
04 /20 /08 KSH+WLI GLV LA/
051C9/08 ?/ PJC DREG DRA FTCORRECTIONS BP Exploration (Alaska)
23
•
6
• •
November 9, 2005
Presentation
BPXA, CPA and Exxon Gas
Cap Water Injection
Presentation (held confidential)
~8
Prudhoe Bay Field - Annual Surveillance Reporting Requirements to AOGCC
Group 1 IPA Group 2 GPMA Group 3 Satellites
Annual Surveillance Report 15-Mar 15-Jun 15-Sep
Annual Overview Presentation 22-Mar 22-Jun 22-Sep
Production Period to be Covered Jan 1-Dec 31 Apr i-Mar 31 Jut 1-Jun 30
e
e
Amends Order/Rule Order Date Comment
Group 1 - IPA Oil Pools
Note C0341 E (modified Pool Definition to
Prudhoe Oil Pool C0341 0 Rule 11 11/30/2001 include a portion of Put River Sandstone)
Put River Oil Pool C0559 11/22/2005 Corrected 2/14/2006
Group 2 - GPMA Oil Pools
Lisburne C0207,207A No rule on Surveillance reports
Niakuk C0329A Rule 9 6/4/1996
North Prudhoe Bay C0345 Rule 8 12/16/1994
pt. Mclntvre C0317B Rule 15 4/19/2000
Raven Oil Pool C0570 Rule 10 8/9/2006
West Beach Oil Pool C0311B Rule 13 8/1/2000
Group 3 - Prudhoe Satellite Oil Pools
Aurora C0457B Rule 8 6/25/2004 (corrected 8/9/2004)
Boreallis C0471 Rule 4 5/29/2002
Midnight Sun C0452 Rule 11 11/15/2000
Orion C0505A Rule 9 4/28/2006
Polaris C0484A Rule 9 11/3/2005
[Fwd: [Fwd: Re: surveillance report dates]]
.
.
Subject: [Fwd: [Fwd: Re: surveillance report dates]]
From: Jane Williamson <jane _ williamson@admin.state.ak.us>
Date: Fri, 20 Apr 2007 13:03:59 -0800
To: Jody J Colombie <jody_colombie@admin.state.ak.us>, Dave Roby <dave_roby@admin.state.ak.us>,
Cathy P Foerster <cathy _ foerster@admin.state.ak.us>, Alan J Birnbaum
<alan _ birnbaum@law.state.ak.us>
CC: Stephen E Mcmains <steve_mcmains@admin.state.ak.us>, art Saltmarsh
<art _saltmarsh@admin.state.ak.us>, Thomas E Maunder <tom _ maunder@admin.state.ak.us>
There is something I didn't get around to before I left and that was to administratively amend the COs for
PBU to include reporting dates agreed to verbally with BP (and DNR). Really, only pt. Mcintyre and Borealis
have the wrong dates in the CO's. The others are either ok, or not explicit. Attached are the COs affected.
I'm not sure how you want to handle. Jody. Please put this in the following CO files along with the
attachment.
Group 1 - IP A Oil Pools
Prudhoe Oil Pool C0341D
Put River Oil Pool C0559
Group 2 - GPMA Oil Pools
Lisburne C0207, 207 A
Niakuk C0329A Rule 9
North Prudhoe Bay C0345
Pt. McIntyre C0317B
Raven Oil Pool C0570
West Beach Oil Pool C0311B
Group 3 - Prudhoe Satellite Oil Pools
Aurora C0457B
Boreallis C0471
Midnight Sun C0452
Orion C0505A
Polaris C0484A
-------- Original Message --------
Subject:Re: surveillance report dates
Date:Thu, 31 Aug 2006 17:27:45 -0800
From:Jane Williamson <¡ane williamson(cì¿admin.state.ak.us>
Organization:State of Alaska
To:Lenig, David C <David.Lenig(iì)bp.com>
References:<CBF4D8E92B5A 704 79F64416582F6A17CB81AEO(cì¿bp 1 ancex005. bp 1.ad.bp.com>
Oops
Lenig, David C wrote:
Hi Jane,
10f3
4/23/2007 9:50 AM
[Fwd: [Fwd: Re: surveillance report dates]]
.
.
I didn't get the attachment.
David
From: Jane Williamson fmailto:jane williamson@admin.state.ak.us]
Sent: Thursday, August 31, 2006 5:14 PM
To: Lenig, David C
Subject: Re: surveillance report dates
E-mail is fine.
Attached is a list of the pools and orders/rules that will be amended with the Admin approval. Take a look and
see if this looks right to you. (Note, I'm only listing the rules that are affected by the new dates - there may be
additional amendments unrelated to the surveillance requirements that I've not listed.)
J'm flexible on the date for the Overview presentation. I'd be fine with specifying it to be within one or two months
of the report date rather than the POD overview that you've noted. What would you prefer?
Lenig, David C wrote:
Jane,
Here is a table showing the dates for the various Reports and
Presentations. I've added the production period as well. The IPA review
date remains problematic due to the proximity to spring break but we
seem to work around it each year.
Would you prefer that I put this in a letter requesting the changes? I
know we talked about this a little while ago I just haven't found the
time.
Thanks,
David
Plan of Development
Production Period
Jull-Jun30
IPA GPMA
March 15 June 15 September 15
March 22 June 22 September 22
March 30 June 30 September 30
Janl-Dec31 Aprl-Mar31
Satellites
Annual Surveillance Report
Annual Overview Presentation
-----Original Message-----
From: Jane Williamson [mailto:jane williamson@admin.state.ak.us]
Sent: Thursday, August 31, 2006 2:30 PM
To: Lenig, David C
Subject: surveillance report dates
Hi David.
When you get a second, could you please send back an e-mail that lists
all the surveillance report dates that we've agreed to for all PBU pools
(including GPMA)? Also, do you have dates for surveillance reviews?
I'll go through the list and make sure the Conservation orders are
correctly worded, then put out administrative amendments as necessary.
I checked with Cammy and she said an e-mail is fine for starting the
200
4/23/2007 9:50 AM
[Fwd: [Fwd: Re: surveillance report dates]]
. administrative action Icess.
.
Thanks.
Jane Williamson, PE <iane williamson((l}admin.state.ak.us>
Senior Reservoir Engineer (907) 793-1226
Alaska Oil and Gas Conservation Commission
Content-Type: application/vnd.ms-excel
surveillance report.xls
Content-Encoding: base64
300
4/23/2007 9:50 AM
*7
bp
-
..
o
B P Exploration (Alaska) Inc.
900 East Benson Boulevard
PO. Box 196612
Anchorage, Alaska 99519-6612
(907) 561-5111
November 30, 2001
Cammy Oechsli Taylor
Chairperson
Alaska Oil and Gas Commission
333 West ih Ave, Suite 100
Anchorage, Alaska
99501
Re: Prudhoe Oil Pool
Gas Cap Water Injection
Letter of Non-Objection
Dear Ms. Taylor:
BPXA, as Operator of the Prudhoe Oil Pool, does not object to the AOGCC's
plan to revoke Rule 4 of Conservation Order 341 C. We understand that the effect
of this revocation will be to make the practices that are currently covered by Rule
4 subject instead to the Commission's regulations, as revised in 1999.
Please let me know if you have any further questions or comments on this issue.
æ;UII~
Perry Richmond
Manager, East/West Group
Prudhoe Bay
BP Exploration (Alaska) Inc.
RECE\\/ED
Alaska on & Gas líQfl5~,t;oInmlSSï(ìf
Äl'!cnorag .
~6
bp
..
November 1, 2001
Cammy Oechsli Taylor
Chairperson
Alaska Oil and Gas Commission
333 West 7th Ave, Suite 100
Anchorage, Alaska
99501
Re: Prudhoe Oil Pool
-
0····················
:_·,C"
BP Exploration (Alaska) Inc.
900 East Benson Boulevard
P.O. Box 196612
Anchorage, Alaska 99519-6612
(907) 561-5111
Gas Cap Water Injection
Hearing Testimony
Additional Information
Dear Ms. Taylor:
Enclosed please find the additional information requested at the Hearing:
1) Section 4 - Water Movement Exhibits 7-11
2) Section 5 - MGS Relationship Exhibit 6
3) Section 6 - Surveillance Exhibits 5-6
4) Pressure Decline by region
5) Detailed Gas Cap map with well locations
6) Testimony Exhibits and text including movies
7) Section 4 - Water Movement Movies
8 1 /2x11 hard copy
8 1/2x11 hard copy
8 1 /2x11 hard copy
hard copy graphs
desk top size hard copy
digital format on CD
8 1 /2x11 hard copy
We understand upon receipt of this information, the record is closed. Please let
me know if we can be of further assistance.
Respectfully
--P~æ;(
Perry Richmond
Manager, EastlWest Group
Prudhoe Bay
BP Exploration (Alaska) Inc.
RECEIVED
NOV 0 1 2001
Alaska Oil & Gas Cons. CommIssIon
Anchorage
·
--
The following provides a list of additional material provided to the AOGCC from BP (Perry Richmond) in
support of the GCWI testimony. Provided 11/06101. List and Addendum #'s compiled by Jane Williamson.
ADDENDUM
DESCRIPTION
A-I
1980 OIL SATURATION MAP
A-2
1990 OIL SATURATION MAP
A-3
2000 OIL SATURATION MAP
A-4A
A-4B
2010 OIL SATURATION MAP wi GCWI
2010 OIL SATURATION MAP nol GCWI
A-5A
A-5 B
2020 OIL SATURATION MAP wI GCWI
2020 OIL SATURATION MAP nol GCWI
A-6A
A-6B
2031 OIL SATURATION MAP wi GCWI
2031 OIL SATURATION MAP nol GCWI
B-1
Year 2000 Filed C1/C3 Ratio
B-2
Year 2000 C1/C3
C
Water Saturations - X-Section Model Locations Shown
for C and D x-section slices
Vertical Water Saturations Year 2005 GCWI
Vertical Water Saturations Year 2010 GCWI
Vertical Water Saturations Year 2015 GCWI
Vertical Water Saturations Year 2020 GCWI
Vertical Water Saturations Year 2025 GCWI
Vertical Water Saturations Year 2031 GCWI
C-l
C-2
C-3
C-4
C-5
C-6
D-l
D-2
D-3
D-4
D-5
D-6
Vertical Water Saturations Year 2005 GCWI
Vertical Water SaturationsYear 2010 GCWI
Vertical Water Saturations Year 2015 GCWI
Vertical Water Saturations Year 2020 GCWI
Vertical Water Saturations Year 2025 GCWI
Vertical Water Saturations Year 2031 GCWI
E
Water Saturations - X-Section Model Locations Shown
for E x-section slices
Vertical Water Saturations Year 2005 GCWI
Vertical Water Saturations Year 2010 GCWI
Vertical Water Saturations Year 2015 GCWI
Vertical Water Saturations Year 2020 GCWI
Vertical Water Saturations Year 2025 GCWI
Vertical Water Saturations Year 2031 GCWI
E-l
E-2
E-3
E-4
E-5
E-6
GCWI ADDENDUM A-I
BP FFCM
BP provided to AOGCC ¡ J /06/0 J
Base Case at 1/1/1980
Base of Zone 3, Model Layer 10
GCWI ADDENDUM A-2
1990 OIL SATURATION MAP
BP FFCM
BP provided to AOGCC 11/06/01
Base Case at 1/1/1990
Base of Zone 3, Model Layer 10
GCWI ADDENDUM A~3
2000 OIL SA TURA TION MAP
BP FFCM
BP provided to AOGCC 11/06/0 J
A-4A
OIL SATURATION MAP
wI GCWI
BP FFCM
BP provided to AOGCC ] 1/06/0]
GCWI ADDENDUM A-4 B
2010 OIL SATURATION MAP
No GCWI
BP FFCM
BP provided to AOGCC 11/06/0]
Base Case at 1/1/2010
Base of Zone 3, Model Layer 10
A-SA
OIL SA TURA TION MAP
GCWI
P FFCM
provided to AOGCC I J/06/0 j
GCWI ADDENDUM A-5 B
020QIL SATURATION MAP
o GCWI
BP FFCM
BP provided to AOGCC 11/06/01
GCWI ADDENDUM A-6 A
GCWI at 1/1/2031
of ZOl1e 3, Model Layer 10
ÇWI ADDENDUM A~6
lOlL SA TURA TION MAP
No GCWI
BP FFCM
BP provided to AOGCC ¡ ¡ /06/0 ¡
at 1/1/2031
Base of Zone 3, Model Layer 10
Vertical Water Saturations
Year 2005 GCWI
BP FFCM 1=65
provided to AOGCC 11/06/01
1=65. 30X Vertical Exaggeration
CWI ADDENDUM
Vertical Water Saturations
Year 2010 GCWI
BP FFCM 1=65
BP provided to AOGCC 11/06/01
GCWI at 1/1/2010
1=65, 30X Vertical Exaggeration
"'CWI ADDENDUM C~3
erticaI Water Saturations
Year 2015 GCWI
BP FFCM 1=65
BP provided to AOGCC 11/06/01
1=65, 30X Vertical Exaggeration
GCWI ADDENDUM C-4
Vertical Water Saturations
Year 2020 GCWI
BP provided to AOGCC 11/06/01
1=65, 30X Vertical Exaggeration
GCWI ADDENDUM C-5
Vertical Water Saturations
Year 2025 GCWI
BP provided to AOGCC 11/06/01
1=65, 30X Vertical Exaggeration
GCWI ADDENDUM C-6
Vertical Water Saturations
Year 2031 GCWI
BP provided to AOGCC 11/06/01
GCWI at 1/1/2031
1=65, 30X Vertical Exaggeration
GCWI ADDENDUM D-l
Vertical Water Saturations
Year 2005 GCWI
BP provided to AOGCC 11/06/01
GCWI at 1/1/2005, Base Zone 3
Cross Section #2
GCWI ADDENDUM
Vertical Water Saturations
Year 2010 GCWI
BP provided to AOGCC 11/06/01
GCWI at 1/1/2010, Base Zone 3
GCWI ADDENDUM D-3
Vertical Water Saturations
Year 2015 GCWI
BP provided to AOGCC 11/06/01
GCWI ADDENDUM D-4
VemcalWater Saturations
Year 2020 GCWI
BP provided to AOGCC 11/06/01
GCWI at 1/1/2020, 8ase Zone 3
Cross Section #2
GCWI ADDENDUM D-5
Vertical Water Saturations
Year 2025 GCWI
BP provided to AOGCC 11/06/0 1
GCWI ADDENDUM
Vertical Water Saturations
Year 2031 GCWI
BP provided to AOGCC 11/06/01
GCWI at 1/1/2031, Base Zone 3
Cross Section #2
GCWI ADDENDUM E
BP provided to AOGCC 11/06/01
3
GCWI ADDENDUM E-l
W3ter S3tur3tions
Year 2005 GCWI
BP provided to AOGCC 11/06/01
GCW¡ at 1/112005
30X Vertical
GCWI ADDENDUM E-2
Vertical Water Saturations
Year 2010 GCWI
BP provided to AOGCC 11106/01
at 1/112010
Vertical Exaggeration
GCWI ADDENDUM
Vertical Water Saturations
Year 2015 GCWI
BP provided to AOGCC 11/06/01
GCW¡ at 1/1/2015
GCWI ADDENDUM E-4
Vertical Water Saturations
Year 2020 GCWI
BP provided to AOGCC 11/06/01
at 1/112020
GCWI ADDENDUM E-5
Water Satu.rations
2025 GCWI
BP provided to AOGCC 11/06/01
at 1/112025
GCWI ADDENDUM
Vertical Water Saturations
Year 2031 GCWI
BP provided to AOGCC 11/06/01
GCWI at 1/112031
30X Vertical Exaggeration
FFCM Pressure Prediction .. Cap Area
00
3900
3700
3500
3300
3100 .
2900
2700
500
1990 2 0 010 2020 030 04
GCW!
MJW 11/13/01
100
3900
3700
35
3300
31
27
GCWI
BP FFCM Pressure Prediction - Gravity Drainage Area
1
5
o
1
o
5
MJW 11/13/01
GCWI ADDENDUM B-1
Year 2000 Filed CVC3 Raito
Actual Field Measunnents
Id
3
tio
BP provided to AOGCC J J/06/0]
:;CWI ADDENDUM B-2
i ear 2000 C1IC3
3P FFCM Prediction
tio
provided to AOGCC 11/06/01
4100
3900
3700
3 0
3300
31
2700
GCWI
BP
Prediction", Gravity DrainagelWF
1
2035
o
15
MJW 11/13/01
100
3900
3700
3500 -
3300
3100
2900
700
2500
GCWI
FFCM
Prediction M Western
2000 2005 2010 201
o 2025
o
MJW 11/13/01
4100
3900
3700
3
3300
3100
27
GCW!
Pressure Prediction - Mid and Eastern
1
5
10 201
2020 2025
MJW 11/13/01
of Pulsed Neutron Logging
30,2001
Exhibit 5
ater
.
emaln
r Slowdown
8
9DVIEW Stwdy[udv$] Caaer]
T$me[01-JAN-20j5. 1
dayaJ
T"i tneStep[ 28]
Az.
Inj ectors
Water Movement Exhibit 9
9DVIEW Study[udv$] Daae[]
T$me[Ql ~AN-2a2Q_ 15588 daya]
T $ me S t e p [ 27 ]
Az
GCWI
ectors
30,2001
Movement Exhibit 10
9DVIEW Stwdy[udv~] Ca.~[]
T !I IT! ~ [ a j - .J AN 2 a 9 j _ :I 98 a 4 day $; ]
T'im~St~p[ 29]
Ax.
GCWI Inj
Movement
11
11III
Map of
, case
, time::: 0.01
, case
=
III
, time::::: 60.01
of
, time:: 90.01
, case
!III
1 x2
Dimensions: 42xlx50
Map of 'SW', case 'Otest', time == 120.01
11II
1 x2
42xl
Map of
, case 'Dtest', time::: 150.01
::::: 180.01
Map of 'SW', case
, time::: 0.01
Map of
:::::
, case
III!
=
11III
ft,
x50
Map
==
, case
11II
'SW', case
,time::::
iIII
lx50
= 360.01
, case
Di1nensions: 42x 1 x50
of
=
, case
III
Map of 'SW', case
:::::
II
, case 'Otest', time ::::::
II
of , case 'Otest', time::::: 480.01
II
of
, case
,time = 51
of 'SW', case
,time:::::
11II
'SW', case
=:
Map
, time::::: 600.01
11II
of
, case 'Dtest',
:::::
IIIi
Map of '5W', case
, time::: 660.01
iii
lx50
of
::
, case
B
lx50
'SW', case
:::::
II
of 'SW', case 'Otest', :=
of
:= 780.01
, case
11II
:: 0..01
118
Map of 'SW', case
::: 840.01
III!
'SW', case
=
fill!
Map 'SW', case
, time = 900.01
of
, time =
, case
11II
:::
IIIi
Map of
::::::
, case
:::: 1
, case
III
1
lx50
Map of
:::
, case
Map of
, time = 1
, case
iii!
of
:= 111
, case
of 'SW', case
== 11
11II
lx50
of
:::::: 11
, case
II
of 'SW', case
:::::
11II
== 1
11II
Map
, time:::: 1
, case
11II
e
, time:::: 1
III
Map
=1
1
lx50
of
:::: 1
, case
III
of 'SW', case
=1
11II
:::: 1
, time =: 1
11III
of
, case
=:
11II
1 x 2
42xlx50
of 'SW', case
::::
of 'SW', case
, time:::: 60.01
iii
of 'SW', case
,time=
1 ac x 2
1
of , case 'Otest', time =: 120.01
x 2 ft,
lx50
of
== 1
, case
III
1 x 2
. 42xl
of 'SW', case 'Otest',
::::: 180.01
of 'SW', case
,time:::::: 210.01
of
,time::::::
, case
ill
1 ac x 2
lx50
of 'SW', case 'Dtest', time :::::
11III
1 x 2
42xl
of 'SW', case 'Dtest', time == 300.01
1 ac x 2
42xlx50
of
== 330.01
, case
III
of 'SW', case 'Otest', ==
11II
1 x 2
: 42xl
of 'SW', case
, time =: 390.01
11II
of 'SW', case 'Dtest', ::
1 2
. 42xlx50
of
case
::
x50
of 'SW', case 'Otest',
= 480.01
of
, time =: 0.01
, case
ill
cf
, time := 540.01
, case
1 2
1 x 50
of 'SW' case ·Otest·, time = 570.01
11III
of 'SW', case 'Otest', time ==
of 'SW', case
,time::::
1 x2
1
of'SW',
==
11II
of 'SW', case
, time::::: 690.01
II!!
of 'SW', case
, time::::: 7:20.01
III
cf
, time == 750.01
, case
1/1
lac x
42xl
of 'SW', case 'Otest', time ::::
of 'SW', case
, time:= 810.01
2
42xlx50
of 'SW', case
, time ::::::
III
of 'SW', case
, time::::: 870.01
..
of
, case
=
..;e.
of
:= 930.01
, case
~
.
.
.." ...
",.
.
e
1
ALASKA OIL AND GAS CONSERVATION COMMISSION
2
PUBLIC HEARING
3
In Re:
4
Application of BP Exploration (Alaska)
5 Inc., Prudhoe oil Pool - Modification
to Pool Rules - Conservation Order
6 341C - Injection of Water into the
Prudhoe Bay Gas Cap.
7
8
TRANSCRIPT OF PROCEEDINGS
9
10
Anchorage, Alaska
October 30, 2001
9:00 o'clock a.m.
CAMMY OECHSLI TAYLOR, Chairperson
JULIE HEUSSER
DAN SEAMOUNT
11 COMMISSIONERS:
12
13 ALSO PRESENT:
ROBERT E. MINTZ
Assistant Attorney General
14
* * * * * *
15
16
17
18
19
20
21
22
23
24
25
METRO COURT REPORTING, INC.
745 West Fourth Avenue, Suite 425
Anchorage, Alaska 99501
(907) 276-3876
·
·
·
e
e
2
1
PRO C E E DIN G S
2
(On record)
3
CHAIR TAYLOR: Good morning. We'll call this meeting
4 -- this hearing to order. Today is Tuesday, October 30th,
5 2001, and the time is approximately 9:04. We're at the
6 offices of the Oil and Gas Conservation Commission at 333 West
7 Seventh Avenue. The subject of this hearing today 1S BP's
8 request for modification of the pool rules for implementation
9 of a Gas Cap Water Injection project in the Prudhoe Bay Oil
10 Pool.
11 First, I'd like to introduce people here at the head
12
of the room. To my far left is Julie Heusser.
To my
13 immediate left is Rob Mintz, our Assistant Attorney General,
14 who is here to advise the Commission on procedural and legal
15 questions. My name is Cammy Taylor. To my right is Dan
16 Seamount. To our very far right is Julie Gonzales from Metro
17 Court Reporting. This proceeding will be recorded and
18
transcribed.
If you wish to make arrangements for copies of
19 that transcript, you may do so directly with Ms. Gonzales
20 after the hearing. We would also ask that after the hearing
21 if all those people who are providing statements or testimony,
22 if you have cards with the correct spelling of your name, if
23 you wouldn't mind giving her a copy that would be helpful to
24 her.
25 Notice of this hearing was published in the Anchorage
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1 Daily News on September 29th, 2001.
These proceedings today
2 will be held in accordance with 20 AAC 25.540. We will ask
3 that the applicant present testimony first, and if there are
4 any other persons wishing to testify, we will hear from them
5 afterwards. We would ask that all persons who are going to
6 testify today, that when they're sworn, that they provide
7 their full name, spell their last name, and identify who they
8
are representing so that that's clearly on the record.
If you
9 wish to be considered as an expert witness, we ask that you
10 identify in what field you wish to be considered as an expert
11 and then provide us with that background.
If there are any
12 other folks who wish to provide your statements afterwards, we
·
13 will do so after all the testimony has been taken.
14 We ask that persons not ask questions directly.
If
15 you have questions that you would like to have put to
16 particular witnesses, we ask that you write them down, that
17 you write down the name of the witness you wish the question
18 to be put to, identify yourself as well in the note and pass
19 it to one of the Commission representatives. And I'll ask
20 that -- there are at least four people in the back room, if
21 you can just raise your hand.
If you'll pass whatever
22 questions you'd like to one of them, they'll make sure that it
23 comes up to the head table.
24 If there aren't any specific questions otherwise, why
25 don't we go ahead and start. We'll ask the applicant to
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1
introduce themselves and then we'll proceed.
2
MR. RICHMOND: Good morning, my name is Perry
3 Richmond. That's R-i-c-h-m-o-n-d.
I am the East/West Prudhoe
4 Bay Waterflood Resource Manager for BP Exploration Alaska Inc.
5 BP is the Operator of the Prudhoe Bay Unit.
6 This hearing has been scheduled to consider
7 information supporting the modification of pool rules for
8 implementation of gas cap water injection in the Prudhoe Bay
9 Oil Pool. The Gas Cap Water Injection project is a result of
10 studies to mitigate reservoir pressure decline for the Prudhoe
11 Bay Oil Pool.
It is a new element in the depletion strategy
12 of the Prudhoe Oil Pool and will improve recovery.
13
BP has previously submitted a request for revision to
14
the pool rules in correspondence to the Commission dated
15
September 21, 2001.
I would like -- now like to give to the
16 Commission a copy of the testimony and exhibits we will be
17 presenting today. We will use a projector to display the
18 exhibits as we read our prepared testimony.
19 The testimony we are presenting will be given by
20 representatives of the Owners, BP, ExxonMobil and Phillips,
21 and is divided into seven parts.
I will provide an overview
22 of the Gas Cap Water Injection project and a summary of other
23 pressure support options that were considered.
I will also
24 give a closing statement summarizing requested changes to
25 Conservation Order 341C. Bharat Jhaveri will testify about
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1 recovery benefitsl Matt Maguire about water movement I Lynn
2 Schnell about the relationship to major gas salesl and Jerry
3 Brady about surveillance.
4
A few notes about acronyms. We may occasionally use
5 the letters GCWI to refer to the Gas Cap Water Injection
6 project. You may also hear GDI which refers to the gravity
7 drainage area
8 of the field I and GDWFII G-D-W-F-II which identifies that part
9 of the field where gravity drainage and waterflood interact.
10 We will keep these terms to a minimum. We are asking that
11 each witness be qualified as an expert and each of us is
12 prepared to respond to questions concerning our testimony and
13
related exhibits.
lId now like to be sworn and qualified as
14
an expert witness.
15
CHAIR TAYLOR: Before I swear you inl Mr. Richmondl is
16 this
the binder that you provided to us this morning I is
17 that different than the one that was prefiled on Friday?
18
MR. RICHMOND: There are a few changes that we have in
19 the testimony here today and weIll note those when we give the
20 testimony.
21
CHAIR TAYLOR: Okay I thank you. Would you go ahead
22 and raise your right handl please.
23 (Oath administered)
24
MR. RICHMOND: I do.
25
CHAIR TAYLOR: Would you proceed and why don/t -- you
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1 wish to be considered as an expert witness?
2
MR. RICHMOND: Okay.
3
In the field of? Engineering?
CHAIR TAYLOR:
4 Petroleum.....
5
MR. RICHMOND: Yes.
6
. . . . . Engineering? Okay. Would you go
CHAIR TAYLOR:
7 ahead and state your qualifications for the record?
8
MR. RICHMOND: Okay. My name is Perry Richmond.
I am
9 a Resource Manager for BP, currently responsible for managing
10 the Prudhoe Bay waterflood in the Northwest Fault Block and
11 Flow Station 2 areas. Technical staff in my group will be
12 responsible for implement -- implementing and monitoring the
13
Gas Cap Water Injection project.
I received a Bachelor of
14
Science Degree in Petroleum Engineering from Texas A&M
15 University.
I was employed by ARCO in 1982 and have worked on
16 numerous engineering projects in Texas, Alaska, and overseas.
17
I have worked on the Prudhoe Bay field since January, 1998.
I
18 have been employed by BP since July, 2000.
19
CHAIR TAYLOR: Commissioner Heusser, Commissioner
20 Seamount, do you have any questions or any objection?
21
COMMISSIONER HEUSSER: No objection.
22
CHAIR TAYLOR: We'll go ahead and consider your
23 testimony as an expert witness.
24
MR. RICHMOND:
I will now provide an overview of the
25 project.
Since field startup in 1977, cumulative production
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from the Prudhoe Bay Oil Pool is now over 10 billion barrels.
2 This surpasses the original estimate of 9.6 billion barrels.
3 This excellent performance has resulted from optimizing total
4 recovery by progressively using multiple recovery mechanisms,
5 such as gravity drainage, gas cycling, oil vaporization,
6 waterflooding, and miscible flooding. These same recovery
7 mechanisms, particularly gravity drainage and gas cycling,
8 result in liquid hydrocarbon and gas voidage from the
9 reservoir, leading to a steady decline of reservoir pressure.
10 Exhibit 2 shows the history and forecast of reserVOlr
11 pressure under the existing recovery mechanisms.
Currently,
12 reservoir pressure is declining at 25 to 35 psi per year. The
·
13 Working Interest Owners have studied options to mitigate
14 pressure decline and have reported annually the progress of
15 these studies to the Commission. As a culmination of these
16 studies, the Working Interest Owners sanctioned the Gas Cap
17 Water Injection project in June, 2001. This project
18 represents a new element in the depletion strategy of the
19 Prudhoe Bay Oil Pool and will mitigate reservoir pressure
20 decline and improve recovery.
21 The project scope calls for ramping up to 650,000
22 barrels per day of seawater into the eastern portion of the
23 gas cap from an injection site located at the East Dock
24 Staging Pad. As shown by the chart, injection increases over
25 time. This is caused by the availability of more seawater as
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1 demand decreases in other projects, such as the Flow Station 2
2 and Point McIntyre water floods and grind and inject.
3 Facility construction is planned for this winter,
4 followed by start-up of injection in mid 2002. Water
5 injection is anticipated to continue for 20 years, with a
6 final injected water volume near four billion barrels. The
7 increase in hydrocarbon liquid recovery is expected to be 150
8 to 200 million barrels.
9 To implement the Gas Cap Water Injection project, a
10 new seawater pipeline from Flow Station 2 to the East Dock
11 Staging Pad will be constructed. The new line will have a 32
12 inch diameter, with a total length of approximately 18,000
13
feet.
It will tie into the existing 32 inch seawater line
14
running from the Eastern Seawater Injection Plant to Flow
15 Station 2.
16 Upgrades to pumps, piping, filters and plant control
17 systems are required at the Seawater Treatment Plant to
18
accommodate the seawater demand.
For the Eastern Seawater
19 Injection Plant, waste heat louvers will be upgraded. A
20 heated pig receiver/manifold module and well houses will be
21 installed at the East Dock Staging Pad to accommodate five to
22 seven new injection wells.
23 Exhibit 5 shows the proposed bottomhole locations of
24 the new injection wells. The wells are strategically located
25
away from the gas injection areas to the west, oil production
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1 at drill site 18 to the southwest¡ and truncation of the
2 Ivishak formation to the east. Basically¡ we want to optimize
3 injection by having sufficient Ivishak pay at the bottom hole
4 locations of the injectors¡ while maintaining sufficient
5 distance from the gas injection and oil producing areas. The
6 majority of the drill site 18 producers and all the gas
7 injectors are more than two miles from the water injection
8 wells. However¡ three producers have been sidetracked to
9 within two miles.
For the record¡ the last two sentences are
10 a change to the pre-filed testimony.
11 Exhibit 6 shows a representative well completion plan.
12 Each completion will include 13 and three-eighths inch surface
13
casing cemented to surface¡ nine and five-eighths inch
14
intermediate casing with cement brought to 1¡000 feet above
15 the shoe¡ and a fully cemented seven inch -- seven inch
16 injection liner. The tubing will be seven and five-eighths
17 inch and will include a seven inch subsurface safety valve and
18 two seven inch profiles. The tubing is large to accommodate
19 the high volume of water to be injected.
The tubing will also
20 be plastic coated to help minimize the friction losses.
21 Average surface pressure for these new injection wells will be
22 approximately 2¡700 psi. Maximum injection pressure is
23
expected to be approximately 3¡100 psi.
24
This concludes the project overview. I will now begin
25
my testimony on the other pressure support options that were
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1 considered.
2 The Owners formed a multi-companYr pressure studies
3 initiative team in 1991 to evaluate pressure mitigation
4 options for the Prudhoe Bay Oil Pool.
Prior to the PSI teamrs
5 focus on gas cap water injectionr several pressure support
6 options were screened. These options included supplemental
7 hydrocarbon gas injectionr nitrogen or flue gas injectionr
8 fuel gas alternativesr additional water injection in oil rim
9 areasr and gas cap water injection.
10 Many of the options considered were not viabler
11 primarily due to high capital costs and/or recovery benefits
12 limitations. These projects are summarized on Exhibit 8.
13
For supplemental hydrocarbon gas injectionr limited
· 14 gas sources exist. A Point Thomson type source was evaluated
15 in the screening study; howeverr high capital costs associated
16 with developmentr distributionr and compression facilities
17 makes this option unattractive.
18 Nitrogen or flue gas injection are also unattractive
19 since these options would require high capital costs for
20 compression or air separationr result in reduced vaporization
21 efficiency compared to lean hydrocarbon gasr and contaminate
22 the reservoir gas.
23 Options to replace the fuel gas used by Prudhoe
24 facilitiesr and thereby reduce reservoir voidager were also
25
screened.
Fuel gas options included importing gasr using oil
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1 as fuel, importing electricity, or developing gas hydrates.
2 The fuel gas options are unattractive due to high capital
3 costs, unproven technology, and the fact that replacing the
4 fuel gas causes a reduction in field gas off-take, resulting
5 in an immediate decrease in oil rate.
6 Exhibit 9 shows projects that have been identified as
7 viable and are now in various stages of implementation.
8 Projects that increase water injection into the oil Rim areas
9 have been justified based on overall recovery benefits, rather
10 than just pressure support benefits. Eileen West End
11 Waterflood, Updip Zone 4 Water/Miscible Injection, and Flow
12 Station 2 Updip Victor WAG Injection are being implemented as
13 projects with related pressure support benefits; however, they
14 have limited pressure support potential when compared to gas
15 cap water injection.
16 Gas cap water injection was screened and found to have
17 significant recovery benefits with reasonable capital cost
18 requirements. The PSI team thought this option was
19 potentially attractive to very attractive. The PSI team
20 recommended gas cap water injection be their focus for more
21 detailed study.
22 This concludes my prepared testimony. Are there any
23 questions?
24
CHAIR TAYLOR: Commissioner Heusser?
25
I have just a couple of
COMMISSIONER HEUSSER:
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1 questions. Here on page six at section two, you quote the
2 average surface pressures for these new water injection wells.
3 Do you know off the top of your head what the current gas
4 injection pressures are? At AGI, WGI, NGI?
5
MR. RICHMOND: The surface injection pressure there?
6
COMMISSIONER HEUSSER: Yeah.
7
MR. RICHMOND: I don't know offhand what those --
8 those are.
9
MR. BRADY: I can answer (indiscernible)
They're
10 running about 32 to 33 (indiscernible).....
11
COMMISSIONER HEUSSER: Thirty-two to 33? So.....
12
CHAIR TAYLOR: If I could just ask that if you speak
13 up or come up to the table so that the transcriber can pick it
14 up on the tape. Thank you.
15
MR. BRADY: My name is Jerry Brady, B-r-a-d-y. Those
16 pressures are roughly 32, 3,300 pounds.
In that ballpark.
17
COMMISSIONER HEUSSER: Thanks, Jerry. And I'm looking
18 again at page seven of this same section, and the statement
19 was made that several pressure support options were screened.
20 In kind of general terms, can you describe the level of
21 screening that took place for these other options?
22
MR. RICHMOND: Well, when they looked at the other
23
options, basically they scoped out what those projects would
24
entail, and did some cost estimating for those options, and
25
then compared those to the various options that were
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1 considered, including gas cap water injection, and then made
2 recommendations for which projects were worthy for consider-
3 for what we call more of a phase two set of studies, which
4 is where the Gas Cap Water Injection project became the focus.
5
COMMISSIONER HEUSSER: Okay. Another question here on
6 page eight, the same section. And you talk about Prudhoe Bay
7 fuel gas. What volume of fuel gas is currently being sold to
8 other fields?
9
MR. RICHMOND: Could you -- volume of.....
10
COMMISSIONER HEUSSER: Fuel gas.
11
MR. RICHMOND:
.... .fuel gas?
12
COMMISSIONER HEUSSER: Right. At one time Prudhoe Bay
13 was selling fuel gas to other fields.
14
MR. RICHMOND: Yeah. Right now the fuel volume
15 overall is about 450 million, but I don't know offhand what
16 the volume that is being sold.
17
COMMISSIONER HEUSSER: Okay. So you don't know if
18 it's a significant volume that -- even if it's still being
19 sold, or whether or not there is a significant volume being
20 sold to other fields?
21
MR. RICHMOND: Do you know that?
22
MR. MAGUIRE: My name is Matt Maguire, M-a-g-u-i-r-e.
23 In terms of fuel gas, there are sales to -- minor sales to
24 like Norgasco, I believe, which supplies gas in Deadhorse.
25
The only field I'm aware of that will shortly be taking fuel
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1 gas lS Northstar. And I think they have a little bit right
2 now to run some equipment, but I know it's under 100 million.
3
COMMISSIONER HEUSSER: Okay. So fuel gas sales to
4 Kuparuk is no longer going on?
5
MR. MAGUIRE: As I understand it, we have NGL's sold
6 to Kuparuk.
7
COMMISSIONER HEUSSER: Okay, but not fuel gas.
8
MR. MAGUIRE: If we have fuel gas, I'm not aware of
9 it.
10
COMMISSIONER HEUSSER: Okay, thank you very much. And
11 in
on page nine, same section. One of the projects that
12
you mention here is the Flow Station 2 Updip Victor WAG
Injection. That is not something that I believe that we know
much about. Can you either describe that in general terms
13
14
15 here or submit what is involved in that?
16 MR. RICHMOND: Yeah, I'll go ahead and summarize what
17 that project entails. That is located in the Flow Station 2
18 area, which is currently where we have waterflood operations.
19 The Updip Victor WAG project will essentially extent the
20 waterflood patterns about one pattern -- updip of existing
21 waterflood patterns in Zones 2 and 3. And also that project
22
includes expanding the MI injection to include drill sites 4
23
and 11, which is where these patterns will be operated out of.
24
So this project will essentially go after reserves in Zones 2
25
and 3 with both expanded waterflood operations as well
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1 miscible injection operations.
2
COMMISSIONER HEUSSER: Okay. So you're going to add
3 WAG up there, okay. Thank you.
4 CHAIR TAYLOR: Do you have any questions?
5
COMMISSIONER SEAMOUNT: I have no questions, thank
6 you.
7
CHAIR TAYLOR: Go ahead and proceed. Are you finished
8 and you're ready for somebody else or.....
9
MR. RICHMOND: Yes, the next four presentations will
10 describe key results from the detailed studies of gas cap
11 water injection. And first, Bharat Jhaveri will review the
12 recovery benefits.
13
CHAIR TAYLOR: Thank you.
14
MR. JHAVERI: Good morning. My name is Bharat S.
15 Jhaveri. I would now like to be sworn and qualified as an
16 expert witness.
17
CHAIR TAYLOR: In what field?
18
MR. JHAVERI: I'm a Consulting Reservoir Engineer with
19 BP Exploration Alaska Incorporated since 1995. I received a
20 PhD in chemical engineering from Stanford University in 1979.
21 I have been involved with the development and reservoir
22 management of the Prudhoe Bay field for over 20 years, from
23 1981 to 1994 at ARCO, and since 1995 at BP.
24
CHAIR TAYLOR: Mr. Jhaveri, do you want to be
25
considered an expert witness in the area of reservoir
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1 engineering?
2
MR. JHAVERI: Yes.
3
CHAIR TAYLOR: Would you raise your right hand,
4 please?
5 (Oath administered)
6
MR. JHAVERI: Yes, I do.
7
CHAIR TAYLOR: Do either of you have any questions or
8 any objection to Mr. Jhaveri being considered an expert
9 witness in the field of reservoir engineering?
10
COMMISSIONER HEUSSER: None at all.
11
COMMISSIONER SEAMOUNT: I have no questions.
12
CHAIR TAYLOR: Go ahead and proceed.
13
MR. JHAVERI: I will now testify about the recovery
14 benefit of the Gas Cap Water Injection Project. Average
15 reservoir pressure in the Prudhoe Bay field is declining at a
16 rate of 25 to 35 psi per year, as shown by the dashed blue
17 curve in this exhibit. The declining pressure reduces
18 efficiency of every recovery mechanism operating in the field.
19 The proposed Gas Cap Water Injection project injects up to
20 650,000 barrels per day of seawater in the eastern gas cap
21 area beginning mid 2002. The -- the pressure forecast with
22 GCWI is shown by the solid green curve in this exhibit. As
23
can be seen, the project essentially maintains a level
24
reservoir pressure until water injection ends in 2022.
25
The GCWI incremental. oil recovery was predicted using
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1 BP's Full Field Compositional Reservoir Model.
It includes
2 the oil that initially was in the gas cap and is immobile.
3 The model uses a 60 acre areal grid of the Prudhoe Bay field
4 as shown in this Exhibit. The recovery calculated by the full
5 field model was validated using mechanistic studies of GCWI
6 using fully compositional one dimensional, two dimensional,
7 strip, and pattern models.
8 The increased pressure resulting from GCWI improves
9 every recovery mechanism operating in the field. The next few
10 exhibits use a cross section schematic of the field, all the
11 way from the gas cap in the north to the aquifer in the south,
12 to explain GCWI recovery mechanisms. The benefits are
13
characterized for three regions in the field. Gas cap,
14
gravity drainage, and waterflood/EOR.
I will now describe the
15 benefits associated with each region starting with the gas
16 cap.
17
In the area of the original gas cap not invaded by
water, the vaporization of residual oil and retrograde
condensate by injection gas is more efficient at higher
18
19
20 pressure. The incremental recovery here is approximately 30
21 million barrels.
In the water invaded area, some hydrocarbon
22 liquids are trapped by the injected water. This prevents
23 vaporization by injected gas, reducing liquid recovery by
24
approximately 50 million barrels.
In total, there is a net
25
reduction of about 20 million barrels in the gas cap region.
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1
I will now describe the benefits associated with the gravity
2 drainage region.
3 As in the gas cap region, vaporization of residual oil
4 and retrograde condensate by the injected gas is more
5 efficient at higher pressure. The higher reservoir pressure
6 also reduces oil shrinkage and oil viscosity. Both of these
7 effects increase oil mobility and result in more efficient
8 gravity drainage. The improved vaporization and gravity
9 drainage processes yield about 200 million barrels of
10
incremental recovery from the gravity drainage region.
I will
11 now describe the benefits associated with the WaterfloodjEOR
12 region.
13
The higher reservoir pressure increases well capacity
14
ln the waterflood area. which in turn increases throughput.
15 Additionally, there is less oil shrinkage. And finally, the
16 higher reservoir pressure allows leaner miscible injectant,
17 thus greater supply and more EOR recovery. The WaterfloodjEOR
18 benefits are approximately 20 million barrels.
19 The incremental recovery from GCWI is approximately
20 200 million barrels in the full field model. The total
21
reflects a reduction of 20 million barrels in the gas cap
22
region, with increases of 200 million barrels in the gravity
23
drainage region and 20 million barrels in the WaterfloodjEOR
24
region.
25
In summary, the Gas Cap Water Injection project
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1 outlined here arrests pressure decline in the field and
2 increases recovery. All recovery mechanisms benefit from the
3 higher pressure. Vaporization, gravity drainage, waterflood
4 and EOR. Total incremental liquid recovery ranges from 150 to
5 200 million barrels. The range reflects modeling
6 uncertainties and the availability of sea water.
7 This concludes my prepared testimony. Are there any
8 questions?
9
CHAIR TAYLOR: Commissioner Heusser?
10
COMMISSIONER HEUSSER: I do. Dan, do you have any?
11
COMMISSIONER SEAMOUNT: I have one question.
COMMISSIONER HEUSSER: Go ahead.
COMMISSIONER SEAMOUNT: Mr. Jhavari?
12
13
14
MR. JHAVERI: Yes.
15
COMMISSIONER SEAMOUNT: Mr. Richmond testified that
16 there were a number of other options that you guys had
17 considered and had discounted for a number of good reasons.
18 Do you have numbers on incremental recovery that would be --
19 that would occur due to those other options?
20
MR. JHAVERI: I actually do not have the exact numbers
21 on top of my head, but I can tell you qualitatively that in
22 terms of the -- the scale of benefit, GCWI was actually the
23 largest, just in terms of the sheer benefits.
24
COMMISSIONER SEAMOUNT: It was larger than the other
25 -- what was it, five options?
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1
MR. JHAVERI: Yes.
2
COMMISSIONER SEAMOUNT: Okay, thank you.
3
CHAIR TAYLOR: Commissioner Heusser?
4
COMMISSIONER HEUSSER: I'm looking at page three of
5 your testimony.
6
MR. JHAVERI: Page.....
7
COMMISSIONER HEUSSER: Page three, and you've got a
8 picture of your model.
9
MR. JHAVERI: Yes.
10
COMMISSIONER HEUSSER: The model that you're using, I
11 know that there have been a variety of models used over the
12 years. Some modeled apex water inject and some modeled east
13 dock water injection. The picture presented here, or the
14 model that you're talking here, does that
is that east
15 water injector~ or apex water injectors? That -- you know,
16 this general discussion?
17
MR. JHAVERI: Yes. This is the model of the Prudhoe
18 Bay field where we actually have
okay. Actually, we have
19 used this model to investigate both the apex injection and the
20 east dock injection. So the model is basically capable of
21 simulating a variety of injection scenarios.
22
COMMISSIONER HEUSSER: I'm looking at page SlX of your
23 presentation.
24
MR. JHAVERI: Page six, okay.
25
COMMISSIONER HEUSSER: Right. And I have to ask this
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1 question. Here in the very first line, it talks about -- as
2 in the gas cap region, and then it talks about retrograde
3
condensate.
Is there retrograde condensate in the gravity
4 drainage area?
5
MR. JHAVERI: What we mean is, this is the gravity
6 drainage area which is the expanded gas -- you know, as the
7 gas cap expands and the oil drains, it creates this expanded
8 gas cap area where there is a residual oil saturation of
9 somewhere around 30, 35 percent. Now as the gas expands into
10 this region, there is maybe a possibility of some of the gas
11 cap liquid initially to drop out. Now later on when the
12 injected gas do come in contact with any dropped out
13
condensate, it will vaporize it.
So what we mean is higher
14
vaporization efficiency. At higher pressure it's more
15 efficient not only to vaporize any residual oil left behind in
16 the expanded gas/oil contact, but also to pick up -- if there
17 were any dropped out condensate.
18
COMMISSIONER HEUSSER: Okay, great.
I'm looking at
19 page nine of your presentation.
20
Page nine? Okay.
MR. JHAVERI:
21
COMMISSIONER HEUSSER: And what caught my eye on this
22 one 1S you talk -- the incremental recovery was going to be a
23
function of the availability of seawater, I think you said.
And you further said that - - you or somebody else said that
Point Mac, Flow Station 2, and NGI currently were using
24
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1 seawater injection? I thought there was only like one well at
2 GC- -- at Flow Station 2 that had seawater injection, the rest
3 was all produced water.
4
MR. JHAVERI: The - - the.... .
MR. RICHMOND: Do you want me to answer it?
MR. JHAVERI: Yeah, you go ahead.
MR. RICHMOND: Flow Station 2 is a combination of both
5
6
7
8 seawater and produced water injection.
9
COMMISSIONER HEUSSER: So it doesn't produce enough
10 water for its injection needs?
11
MR. RICHMOND: That's correct.
12
COMMISSIONER HEUSSER: I am so surprised. Okay. We
13 I had heard talk about a waterwheel project kind of going
14 on in the field, moving produced water from the point where
15 it's produced, utilizing existing perhaps oil flow lines and
16 moving it around the field to areas where produced water was
17 needed. When will that take place? will that take place?
18
MR. RICHMOND: Waterwheel is still under evaluation.
19 It hasn't been sanctioned yet by the Owners.
I can't tell
20 exact timing then of -- of when that project could actually be
21 implemented. The purpose of waterwheel as it relates to gas
22
cap water injection will -- it could give us additional
23
seawater for gas cap water injection, and that's primarily
24
because some of the produced water within the Prudhoe Bay
25
could be then injected at Point McIntyre which is currently on
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1 seawater. And if that's converted from seawater injection to
2 produced water injection, then that would free up additional
3 seawater to be placed into the Gas Cap Water Injection
4 proj ect.
5 So there is the possibility with waterwheel coming on
6 line to have more water and higher injection rate closer to
7 the 650,000 barrel a day level than the chart that I showed in
8 my testimony.
9
COMMISSIONER HEUSSER: So what's the maximum volume of
10 water that the 32 inch pipeline will carry?
11
MR. RICHMOND: The 32 inch line actually has a
12 capacity very similar to what the eastern seawater injection
13 plant capacity is, which is maybe somewhere around 900 to
14 950,000 barrels a day is what would be possible.
15
COMMISSIONER HEUSSER: And the seawater treatment
16 plant was originally designed for one million, two million
17 barrels of water per day?
18
MR. RICHMOND: I believe that's.....
19
COMMISSIONER HEUSSER: Barrels of seawater?
20
MR. RICHMOND: I'm not quite sure what the original
21 design is, but the capacity that we'll be up to with gas cap
22 water injection will be around the 900, 950,000 barrel a day
23 level.
24
COMMISSIONER HEUSSER: Okay. So ESIP will take
25
900,000, the flow line is 900,000, and then mods to STP will
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1 provide 900,000?
2
MR. RICHMOND: Yeah, STP -- the upgrades that we're
3 applying at STP are to bring it up to levels so that we can
4 maximize the ESIP capacity of the 900, 950,000.
So STP will
5 be able to deliver that as well.
6
COMMISSIONER HEUSSER: Okay.
Thank you.
7
MR. JHAVERI: Okay. This concludes my prepared
8
testimony.
If there are no more questions. Thank you. Next
9 Matt Maguire will review water movement.
10
MR. MAGUIRE: Good morning. My name 1S Matt Maguire,
11 M-a-g-u-i-r-e.
I'd now like to be sworn and qualified as an
12 expert witness in reservoir engineering.
13 CHAIR TAYLOR: Thank you. Would you raise your right
14 hand, please?
15
(Oath administered)
16
I am a Senior Reservoir Engineer
MR. MAGUIRE: Yes.
17 with Phillips Alaska, Incorporated, currently assigned to the
18 Greater Prudhoe Area Team.
In 1988, I received a Bachelor of
19 Science Degree in Petroleum Engineering from the University of
20 Alaska Fairbanks.
I started working for ARCO Alaska out of
21 college and am currently in my fourteenth year of working
22
Prudhoe Bay engineering projects.
I will now testify about
23 water movement.
24
CHAIR TAYLOR: Before you do that, do either
25
Commissioner Heusser or Commissioner Seamount have any
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1 questions or any objections to him being considered an expert
2 witness in the field of reservoir engineering?
3
COMMISSIONER HEUSSER: Absolutely none.
4
COMMISSIONER SEAMOUNT: No questions, no objections.
5
CHAIR TAYLOR: Why don't you go ahead and proceed.
6 Thank you.
7
MR. MAGUIRE: Thank you.
In my presentation, I am
8 going to talk about water movement and describe how and where
9 the water moves once it is injected into the gas cap.
I will
10 begin this by summarizing the water movement objectives for
11 the GCWI project.
12 Shown here is a map of the area surrounding the
13 proposed location of the GCWI injectors. The location of the
· 14 water injectors was chosen to keep the injected water in the
15 eastern part of the gas cap and limit interference with
16 operations in three other areas of the field.
These three
17 areas are the gas injection area to the west, the waterflood
18 area at drill sites 4 and 11, and the gravity drainage area at
19 drill site 18.
20 In the gas injection area, we want to avoid
21 significant impact to the gas injectors. This is important
22 because reduced gas injectivity reduces field gas offtake and
23 therefore oil production.
24 The following paragraph filed in the prefile had 2
25 errors which I will correct here in my testimony. The closest
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1 oil producers in the waterflood area are at drill sites 4 and
2 11. Water encroachment here is not a concern. This area is
3 already being waterflooded, waterflood -- water from the GCWI
4 injectors should complement the existing flood. Within the
5 gravity drainage area, we want to preserve oil recovery.
6 To accomplish this objective, the piston-like flood
7 font is desired. This slide shows two flood fronts that are
8 relevant to the discussion of this project. Each of these is
9 pictured in a 2D cross section. Our preference is the piston-
10 like flood front. This is characterized by efficient and
11 uniform displacement as opposed to having channels develop.
12 Here, the front is stable, moves slowly, and takes much longer
13 for water to break through.
14
With the channeling front, it is easy to see how water
15 breakthrough would occur earlier. As you can imagine, this
16 type of behavior within the GCWI project is not desirable.
17 For gas cap water injection, the displacement of gas
18 by water is very efficient and essentially piston-like. This
19 is because gas is 100 times more mobile than the water that
20 displaces it.
I will now demonstrate this for you with a flow
21 model.
22 I have two reservoir simulations to show you. Each
23 uses the reservoir description shown on this slide. The model
24 is 2D cross-sectional in nature, with an injector on the left
25 and a producer on the right. The cells are 208 feet square
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1 and two feet thick. The green cells have 500 millidarcy
2 permeability and the orange cells 5,000 millidarcy. The
3 orange cells represent a 20 foot thick thief zone in the
4 middle of the model.
5 The main difference In the model runs will be the
6
fluid within it.
In one simulation the model contains oil,
7 and in the other, gas.
In each simulation we will inject
8 water. The purpose of these comparison cases is to show how a
9 high permeability zone has little effect when water displaces
10 gas.
11 This first simulation is of water displacing oil.
12 Here we would expect the permeabilities to playa major role.
13 (Pause)
14
This is the end of the run. Let's run that one more
15 time.
16 (Pause)
17
Okay. Note water breakthrough right there.
18
(Pause)
19
As you've seen, the thief zone caused early water
20 breakthrough and channeling of the water. Now let's take a
21 look at the same simulation, however this time the model will
22 be loaded with gas instead of oil.
So, this simulation is of
23 water displacing gas.
Keep in mind the thief zone is in the
24
middle of the model.
25
(Pause)
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1
This is the end of the run.
Let's run this one more
2 time.
3 (Pause)
4 As you have seen, even a high permeability thief like
5 this one significantly dampened -- is significantly dampened
6 by such a favorable displacement process.
7 I have one comparison slide to summarize what we just
8 viewed.
The water displacing oil case shows the water moving
9 significantly faster through the high
permeability channel
In the water displacing
on the flood front, such
10 leading to early water breakthrough.
11 gas case, the thief has little effect
12
that the displacement is nearly piston-like.
The water
13 doesn't channel through the gas. This is because the gas is
14
approximately 100 times more mobile than the water. As a
15 result, this displacement process dampens the effect of
16 geologically reasonable variations in reservoir permeability.
17 At this point, I would like to show you some areal
18 water saturation maps from BP's full field model. This slide
19 shows water saturation within the high permeability Zone 3 on
20 1/1/2005, approximately 3 years after the start of injection.
21 The blue circle represents the bulb of water that has been
22 injected up to this date.
23 The next paragraph has a clarification to the prefiled
24
testimony.
For illustrative purposes, some of the GCWI
25
injectors are shown, as are some of the gas injectors closest
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1 to the project. Additionally I have noted where some of the
2 closest oil producers are located within the gravity drainage
3 and waterflood areas.
4 This slide shows the continued growth of the water at
5 2010, or after approximately eight years of injection.
6 This slide shows the continued growth of the water at
7 2015, which is approximately 13 years of injection.
8 And 2020, which is approximately 18 years of
9 injection.
10
And this is 2031. Water injection was stopped in
11 2022. Due to its low mobility, the water moves very little
12 between 2022 and 2031.
So a picture at 2031 is almost the
13 same as a picture at 2022.
14
As you can see water eventually reaches the closest
15 gas injectors and some oil producers at drill sites 4, II, and
16 18. Let me show you the effect on these three areas on the
17 next three slides.
18
First, GCWI has a small impact on gas injection.
It
19 occurs primarily late in field life when the gas oil ratios
20 are higher. This impact is incorporated into the benefits
21 analysis.
22 Second, this plot shows the cumulative oil production
23 for drill sites 4 and 11 with and without GCWI. As you can
24 see, oil recovery is slightly higher with GCWI. This is
25
because the additional water from GCWI drives updip oil
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1 towards the drill site 4 and 11 producers.
2
And finally, this plot shows cumulative oil production
3 for drill site 18 with and without GCWI. Oil recovery lS
4 slightly higher with GCWI because the water limits gas
5 encroachment and displaces some updip oil.
6
This concludes my prepared testimony. Are there any
7 questions?
8
CHAIR TAYLOR: Mr. Maguire, just for the record, real
9 quickly if you wouldn't mind identifying -- you showed two
10 video clips. If you would, just for the record, explain where
11 those are contained in the slides of the prefiled testimony.
12
MR. MAGUIRE: Tab 4A and 4B.
13
CHAIR TAYLOR: Okay. So 4A is the water displacing
14 oil and 4B is the water displacing gas, is that correct?
15
MR. MAGUIRE: That's correct.
16
CHAIR TAYLOR: Thank you.
17
MR. MAGUIRE: You're welcome.
18
CHAIR TAYLOR: Commissioner Seamount, Commissioner
19 Heusser, do you have any questions?
20
COMMISSIONER HEUSSER: Basic question.
21
MR. MAGUIRE: Sure.
22
COMMISSIONER HEUSSER: For those presentations that
23 are included in 4A and 4B, does the official exhibit include
24 full size copies of these slides?
25
MR. MAGUIRE: Oh, does it include real size.....
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1
COMMISSIONER HEUSSER: Yeah, real size copies in.....
2
MR. MAGUIRE: No, they're in handout size. So we can
3 certainly provide them, though.
4
COMMISSIONER HEUSSER: I think that for our record
5 that would be useful.
6
MR. MAGUIRE: Okay.
7
COMMISSIONER HEUSSER: Likewise, would you be able to
8 provide a larger size of page seven, eight, and nine, 10, and
9 11, again, to make our record easier to read?
10
MR. MAGUIRE: I'm not sure if I caught all the pages.
11 Seven, eight, nine, 10.....
12
COMMISSIONER HEUSSER: Seven, eight, nine, 10, and 11.
13 It's Zone 3 beginning in 1001 (sic) to 2005, going up to 1000
14
January 1st, 2031.
15
MR. MAGUIRE: Okay.
16
COMMISSIONER HEUSSER: I just find them pretty
17 difficult to read and I think our record needs to be readable.
18 I do have one last question, Mqtt.
19
MR. MAGUIRE: Yes.
20
COMMISSIONER HEUSSER: I always pictured that there
21 would be a significant gradient between the gas injection
22 wells, NGI, WGI, AGI, and the waterflood area. In the course
23 of your modeling, did you notice that? Or is it just.....
24
MR. MAGUIRE: And when you say gradient, are you
25 talking about pressure.....
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1
COMMISSIONER HEUSSER: Pressures.
2
MR. MAGUIRE:
. . . . .gradient?
3
COMMISSIONER HEUSSER: Pressure gradientsl yeah.
4
MR. MAGUIRE: The gas cap has very good conductivity.
5 As suchl I don/t believe there/s a very large gradient between
6 those two areas. If you follow the growth of the bulb as
7 welll there is a tendency of the bulb to grow a little bit
8 farther towards the gravity drainage and almost be pushed from
9 the side by the gas injectors.
10
COMMISSIONER HEUSSER: So the gas injectors work to
11 push the water down towards drill site 18 probably a little
12 faster than it -- than the water would head on over to those
13 drill site 4 wells? Off to the right?
14
MR. MAGUIRE: Yeahl that/s a good way to look at it.
15 The water tends to move radially outward I however it is
16 slightly compressed by the gas injectors. Certainly the
17 producers also intend to pull the bulb towards them. I think
18 there might a small tendency to move a little bit faster
19 towards drill site 181 but it/s -- it would be a very minimal
20 effect.
21
COMMISSIONER HEUSSER: So it IS an even radial movement
22 of water out from the east dock injectors? Kind of nice.....
23
MR. MAGUIRE: It is approximately radial I yes.
24
COMMISSIONER HEUSSER: And so when you commented that
25
the gas cap has good conductivitYI do you assume that the --
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1 relic (ph) oil saturation in the entire gas cap area is the
2 same? I mean, i.e. in that east side where there has actually
3 been no gas injection?
4
MR. MAGUIRE: The -- as I understand it, the BP full
5 field model 1S initialized with the oil saturations that we
6 expect were in the gas cap throughout at the beginning of the
7 field. For the purposes of all the simulation work, that oil
8 is immobile. I'm not sure if that answers your question.
9
COMMISSIONER HEUSSER: The gas cap oil is immobile?
10
MR. MAGUIRE: Yes, to waterflood. It's purely
11 recovered through vaporization.
12
COMMISSIONER HEUSSER: Okay. So do the modeling
13 results show that some of that oil has already been recovered?
14 MR. MAGUIRE: Has already been.....
15
Recovered through ga- -- you
16
COMMISSIONER HEUSSER:
know, the normal. . . . .
MR. MAGUIRE: Yes.
COMMISSIONER HEUSSER:
MR. MAGUIRE: Yes.
COMMISSIONER HEUSSER:
Okay.
17
18
. . . . .gas injection?
19
20
21
MR. MAGUIRE: The - - yes. The lean gas siphoning
project is recovering. . . . .
COMMISSIONER HEUSSER: From the eastern part?
22
23
24
. . . . .oil from the gas cap. And as I
MR. MAGUIRE:
25
understand it.....
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1
COMMISSIONER HEUSSER:
From the entire gas cap area?
2
MR. MAGUIRE: As I understand it, it is, yes.
3
MR. JHAVERI: Can I (indiscernible). Yeah, I think
4 the.....
5
CHAIR TAYLOR: Excuse me, could you come up -- on the
6 table there, there's a microphone at the table. Thank you.
7
I think the
as you can see
MR. JHAVERI:
8
(indiscernible) .
I think there is injection in this NGI --
9 NGI area of the gas cap, and the gas basically advances
10 just like the water is injected right here in this dark area.
11 We have been having injection in the AGI and NGI area. So
12 there is a -- from the gas point of view, now I'm talking
13 about injected gas, the injected gas that has been injected
14 moves outside and has been, you know, sweeping (ph) this area
15 of the gas cap.
So obviously there is more vaporization that
16 has occurred closer to the gas injector area. And as you get
17 farther and farther away, there is less and less vaporization.
18 And I don't know if you can put one of my slides back? Is it
19 possible to.....
20
UNIDENTIFIED VOICE: Which one?
21
MR. JHAVERI: The one with
you saw water invaded
22 areas in the (indiscernible) section. Benefits testimony.
23
Yeah, just go back one and then I'll ask you to stop. Keep on
going back. This lS good enough, actually.
So like - - so let me just start again. So here is the
24
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1 AGI, WGI, and here is where we are injecting, okay? And this
is the water invaded area.
In our benefits analysis, we do
it is a fully compositional model, so we do include all the
process that has happened in the field since the beginning of
gas injection. And at the time the water injection starts,
the gas here is somewhat richer and there is somewhat less
vaporization of liquid than if you had been in the NGI, AGI
area.
Now let me also add to my -- your answer, and that is
that some of the benefits that I do describe by the model,
this minus 20 did include -- if you remember I testified
earlier, minus 50 million barrels, somewhat of a reduction in
liquid in this area.
So those results include somewhat higher
yield and somewhat less vaporization of oil in this part of
the gas cap.
COMMISSIONER HEUSSER: Okay.
So the minus 50 does
include the area in the eastern part of the gas cap, . . . . .
MR. JHAVERI: Yes.
COMMISSIONER HEUSSER:
. . . . .but the oil that would not
be.....
MR. JHAVERI: That's where it is -- now this is a
positive part that also I mentioned, which is the -- in the
area which is not invaded by the water, the injected gas
continues to vaporize the relic oil, but at a higher
efficiency, because the pressure is higher, the thermodynamics
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1 is better. So the net effect of that is actually additional
2 30 million positive benefits of improved vaporization. Thus
3 the net effect of these two is only, you know, minus 20. But
4 what I want to add, you know, when I came into help out Matt
5 here lS, yes, we understand your question and that the gas is
6 going to be sweeping more of the -- the oil at the time of the
7 injection compared to the eastern area. And all this is --
8 and all these mechanisms are included, you know, with benefits
9 analysis.
10
COMMISSIONER HEUSSER: Thank you.
11
MR. RICHMOND: And just for the record, Bharat was
12 referencing Benefits Exhibit 8.
13
CHAIR TAYLOR: Thank you.
14
COMMISSIONER HEUSSER: That's it for me.
15
CHAIR TAYLOR: Commissioner Seamount?
16
COMMISSIONER SEAMOUNT: Mr. Maguire, have you modeled
17 any potential streaks of greater than five darcys, to see if
18 -- you know, is there a point where channeling would start to
19 have an effect? Some permeability?
20 MR. MAGUIRE: We have performed sensitivities to look
21 at high perm thief. The only geologic occurrence that we can
22 come up with that might be such a thief would be the open
23 framework conglomerate (ph). Geologically, none of the
24
geologists believe that that deposition would be channel-like.
25
The idea is it'd be very thin, would not be laterally
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1 continuous. But for our sensitivity case -- one of the
2 sensitivity cases, we did run a channel directly from the east
3 dock injectors straight down to drill site 18. And we
4 characterized it as a 40 darcy channel with a perm
5 modification to the bottom of layer -- to a bottom of a layer
6 in Zone 3. When we looked at the sensitivities between the
7 base case and this sensitivity, the expected time of arrival
8 of the water changed.
It became earlier by about two years.
9 That was a sensitivity that indicated that a thief of that
10 magnitude, even in the full field model, did not necessarily
11 change your arrival time or change your flood front.
12
COMMISSIONER SEAMOUNT: Do you perceive the
13 possibility of any faults acting as high permeability
14 conduits?
15
MR. MAGUIRE: There were sensitivities also run with
16 faults. What I can say on that is that, just as in the
17 example of the channel, if you have a mechanism that will pull
18 the water out in a certain fashion, the water still wants to
19 displace the gas. And unless you seal up the fault somehow,
20 you're still going to have the water going through it and
21 dissipating it pretty rapidly.
So you still continue to
22 dampen the effects of any kind of reservoir heterogeneities
23 like faults or potential thief zones.
24 COMMISSIONER SEAMOUNT: Now once the water reaches --
25
I think you -- did you mention that the water would reach some
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1 of the oil areas, like the northern oil producers, and you
2 talked about drill sites 4, 11, and 18?
3
MR. MAGUIRE: That's correct.
4
COMMISSIONER SEAMOUNT: Now once the water reaches
5 there, I guess I understand that the plot you showed, showed
6 there would actually be benefit. Is there a possibility if
7 the water reached there sooner that there would not be a
8 benefit?
9
MR. MAGUIRE: Yes.
10
COMMISSIONER SEAMOUNT: Okay.
11
MR. MAGUIRE: I think -- we could certainly come back
12 to this topic if you want. Jerry Brady will be talking about
13 surveillance and we'll certainly be monitoring the water front
14 to try to prevent that.
15
COMMISSIONER SEAMOUNT: Okay. Thank you, Mr. Maguire.
16
MR. MAGUIRE: You're welcome.
CHAIR TAYLOR: Thank you.
MR. MAGUIRE: Thanks for your time. The next section,
17
18
19 major gas sale relationship, will be presented by Lynn
20 Schnell.
21
MR. SCHNELL: Good morning. My name is Lynn W.
22 Schnell. I'd now like to be sworn and qualified as an expert
23 witness in reservoir engineering.
24
CHAIR TAYLOR: Raise your right hand, please.
25
(Oath administered)
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1
MR. SCHNELL: Yes, I do.
2
Please proceed with your
CHAIR TAYLOR:
3 qualifications.
4
I've been employed by ExxonMobil
MR. SCHNELL:
5 Production Company and its predecessors since graduating from
6 Washington State University in 1965 with a Bachelor of Science
7 degree in electrical engineering.
I've been involved with the
8 development and reservoir management of the Prudhoe Bay Field
9 almost continuously since June, 1968.
10
CHAIR TAYLOR: Thank you. Do either Commissioner
11 Heusser or Commissioner Seamount have any questions or any
12 objections?
13
COMMISSIONER SEAMOUNT: No questions, no objections.
14
COMMISSIONER HEUSSER: No questions, no objections.
15
CHAIR TAYLOR: Thank you, please proceed.
16
MR. SCHNELL: I will now testify about the
17 relationship of a major gas sale to the Gas Cap Water
18 Injection Project.
19 The purpose of this presentation is to address the
20 interaction of the Gas Cap Water Injection project with a
21 potential major gas sale. The primary focus will be on how a
22 gas sale would impact the estimated benefits of the project.
23 The secondary focus will be on how gas cap water injection is
24 expected to impact ultimate gas recovery.
25 Since the timing and rate of a gas sale have yet to be
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1 determined, a gas sale will be addressed broadly. As such, I
2 will focus on the mechanisms involved and will not try to
3 quantify these factors.
4 In general, the water injection project will maintain
5 reservoir pressure at a higher level under any currently
6 foreseeable gas sales scenario. A gas sale will reduce the
7 incremental oil recovery from gas cap water injection. This
8 will be shown and explained.
Finally, the impact of the
9 project on ultimate gas recovery will be addressed.
I will
10 show that gas recovery potential is virtually unchanged when
11 compared to a no gas cap water injection case.
12 This chart represents the average reservoir pressure
13
as predicted by the BP full field model.
It shows that gas
14
cap water injection results in a uniformly higher reservoir
15 pressure with major gas sales.
In this case, approximately
16 140 psi.
17 The blue dashed curve shows the pressure declining at
18 25 to 35 psi per year until a four bcf a day gas sale begins
19 in 2008, at which time the pressure drops at about 135 pounds
20 per year through 2025. The rate of pressure decline is
21 proportional to the gas sales rate. The pressure decline
22 moderates in the later years as the gas sales rate drops due
23 to pressure depletion.
24 The solid green curve is for the same gas sales
25
scenario, but with gas cap water injection.
Initially,
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1 reservoir pressure remains essentially constant until the
2 start of the gas sale in 2008. At that time, the pressure
3 parallels the case without injection.
This same relationship
4 lS characteristic of other gas sales rates and timing.
5 The higher pressure with the project means that even
6 with a major gas sale, the oil recovery mechanisms will
7 operate more efficiently. This is depicted in the next chart.
8
This graph shows the cumulative incremental oil
9 recovery due to gas cap water injection through 2030. While
10 the gas sale reduces the recovery, the incremental recovery
11 remains significant and the project remains viable.
12 The upper dashed blue curve represents the 200 million
13 barrels shown in Bharat Jhaveri's testimony. The solid green
14
curve represents the 135 million barrel incremental recovery
15 with a four bcf a day gas sale starting in 2008.
16 This reduction in recovery is caused by three
17 mechanisms.
First, with a major gas sale, the volume of gas
18 available for injection is reduced in order to meet the gas
19 sale demand. Thus, less oil is vaporized by injected gas.
20 This reduced vapor- -- this reduces vaporization recovery for
21 gas cap water injection.
Secondly, the ability of the
22 injected gas to vaporize the oil it contacts diminishes with
23 lower reservoir pressure. And finally, with the lower
24 pressure due to a gas sale, the oil becomes more viscous. It
25
drains more slowly and less is recovered.
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1
With this understanding of how major gas sales impacts
2 gas cap water injection, I would now like to address how gas
3 cap water injection would impact a major gas sale.
4 This chart is a plot of cumulative gas sales with time
5 through 2050 as forecasted by the BP full field model. It
6 shows that ultimate gas recovery will be essentially unchanged
7 by gas cap water injection. The primary reason for this is
8 that similar abandonment pressures can be realized with and
9 without the project. This requires a large water-free area
10 from which to produce the gas. During the final stages of
11 field life, after the recoverable liquids have been produced,
12 the operating objective will be to maximize gas recovery.
13 This is accomplished by blowing down the reservoir pressure
14 with the remaining wells. These will likely be former oil
15 wells that have been recompleted as gas wells into the
16 expanded and original gas cap. As you know, there are many
17 candidate wells in the gravity drainage area.
18 Gas well producing capacity is a strong function of
19 both reservoir pressure and water production. Without water,
20 a gas well can flow at economic rates with relatively low
21 relative reservoir pressure. However, if water is produced
22 along with the gas, a much higher reservoir pressure is needed
23 to sustain production. Consequently, a large water-free area
24 must remain in the reservoir late in field life. As shown on
25 the next slide, water injected into the cap remains highly
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1
localized.
2 This chart shows the water and hydrocarbon saturation
3 as predicted by the BP full field model in the high
4 permeability Zone 3 at 2035. The blue represents high water
5 saturation. Red represents high gas saturation in the
6 original gas cap. The somewhat darker, almost brownish
7 colored represents the high gas -- represents where gravity
8 drainage and vaporization have been responsible for oil
9 recovery.
10 The water injected into the gas cap is readily
11 apparent. This water remains relatively close to where it was
12 injected because of its low mobility compared to the gas it
13 displaces. The blue area around the lower edge is the
14 aquifer.
15 Although not apparent on this chart, most of the red
16 and brownish areas have been penetrated by many wells on
17 approximately 80 acre spacing.
It is through these wells that
18 the bulk of the late life gas reserves will be produced.
19 Within the red and brownish areas, the gas recovery mechanism
20 will be simple pressure depletion.
21 Because of this large water-free area, the gas cap
22 injection will not materially impact the final reservoir
24
23 pressure as shown on the next chart.
25
This is the same pressure chart shown earlier. Notice
how close the pressures are at the end.
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The next chart will then illustrate how reservoir
pressure depletion impacts gas recovery.
This chart shows gas recovery by pressure depletion as
a percent of the original gas in place. Gas recovery varies
inversely with pressure. Notice that recovery exceeds 80
percent when the pressure is reduced from the original 4,400
psi to about 850 psi. This is representative of what happens
8 in the absence of water in the original gas cap and throughout
9 much of the gravity drainage area.
10 The next chart will show what happens when water is
11 injected into the gas cap.
12 The solid green line in this chart depicts gas
13 recovery in the case where water has been injected into the
14 gas cap after the reservoir pressure has dropped from the
15 original 4,400 psi to 3500 psi. For reference, the pressure
16 depletion curve from the previous chart is also shown.
17 When water is injected, it displaces most of the gas.
18 In this example, gas saturation is reduced from an original 90
19 percent pore volume to a trapped gas saturation of 25% pore
20 volume. Just as water is able -- is unable to displace all of
21
the oil In a waterflood, it is unable to displace all of the
22
gas in the gas cap.
23
The solid green curve shows that prior to water
24
injection, about 17 percent of the original gas volume had
25
been recovered, or in this case expanded down into the gravity
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1 drainage area, by pressure depletion.
2 When water is injected, gas is physically displaced so
3 that almost 80 percent has been removed from the water invaded
4 pore volume. When reservoir pressure is subsequently reduced
5 during blow down, the trapped gas expands and once -- once
6 again becomes mobile.
7 Notice that at a reservoir pressure of 1,500 psi, the
8 gas recovery in the water invaded area is 90 percent. In
9 order to realize this level of recovery by pressure depletion
10 alone, the pressure has to be blown down to 500 psi.
11 Thus, it can be seen that gas recovery from the gas
12 cap where water is injected may exceed that from the rest of
13 the gas cap and gravity drainage area.
14
Now to summarize.
In conclusion, gas cap water
15 injection has been shown to yield higher reservoir pressure
16 with and without a major gas sale. Any water injected serves
17 to reduce total net voidage and thus maintain a higher
18 pressure. The gas sale does, however, reduce the incremental
19 oil recovery due to gas cap water injection for three reasons.
20 First, it reduces the volume of vaporized oil because less gas
21
is injected into the gas cap.
Second, the ability of the
22
injected gas to vaporize residual oil is somewhat lower at the
23
lower reservoir pressure associated with the gas sale.
24
Finally, gravity drainage is reduced.
25
Gas recovery will be virtually unchanged by the gas
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1 cap water injection. This is because the large water-free
2 area that remains during late field life enables effective
3 pressure depletion with only a slightly higher final pressure.
4 Also, it is likely that the gas recovery from the water
5 invaded area will be somewhat increased.
6 This concludes my prepared testimony. Are there any
7 questions?
8
CHAIR TAYLOR: Mr. Seamount, do you have any
9 questions?
10
COMMISSIONER SEAMOUNT: Mr. Schnell, what is the
11 sensitivity of oil and gas recovery to water injection rate or
12 water injection volume? Is there a big sensitivity? I mean,
13 if you injected twice as much, would your recoveries change
14 quite a bit?
15
If you inject so much water that it
MR. SCHNELL:
16 basically fills the whole gas cap, then, you know, you could
17 certainly have a major impact on the oil recovery. The effect
18 on gas recovery could also be negative to the extent that you
19 no longer had a water-free area from which to pressure
20 deplete.
21
So there'd be a breakover
COMMISSIONER SEAMOUNT:
22
point then, right? Where your benefit goes away for the gas.
Now for the oil, is there a breakover point?
MR. SCHNELL: Yes, there is - - there is a breakover
23
24
25
point, or there is an optimum time and rate at which to inject
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1 the water for a given field life scenario, for a given timing
2
and rate of major gas sales.
I think what we have now is a
3 project that is pretty much optimized given the uncertainty
4 that remains with regard to the rate and timing of gas sale.
5
COMMISSIONER SEAMOUNT: Okay, thank you.
6
CHAIR TAYLOR: Commissioner Heusser?
7
COMMISSIONER HEUSSER: A couple of just general
questions and you're the lucky person to get to answer these
because of your extensive Prudhoe Bay history. Why is this
8
9
10 gas cap water injection appropriate now and it wasn't five
11 years ago?
12
MR. SCHNELL: Well, it's appropriate now because five
13 years ago the oil rim was much less mature than it is today.
14 As such, there would have been a greater potential for having
15 some adverse impacts. More so in, say, drill site 18 area
16 than what we see today. More so also in reducing our ability
17 to inject gas. But now with a more mature field, I think it's
18 a better time to be injecting this water.
19
So when you use the term mature
COMMISSIONER HEUSSER:
20 field, you're -- are you saying that more oil has been
21 recovered.....
22
MR. SCHNELL: Yes.
23
COMMISSIONER HEUSSER:
.... . from that up-structure
24 area?
25
MR. SCHNELL: Yeah.
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1
COMMISSIONER HEUSSER: And so there's less to lose --
2 less reserves at stake?
3
MR. SCHNELL: There are fewer barrels at stake.
4 Development in the updip area has progressed with time, such
5 that the wells up there now are all producing at very high
6 gas/oil ratios.
7
COMMISSIONER HEUSSER: Okay. Lynn, again because of
8 your lengthy history with Prudhoe Bay reservoir development,
9 and for our record, would you provide just kind of a general
10 time line history of the evaluation process that all the co-
11 owners went through for this Gas Cap Water Injection project?
12 Just kind of walk us through that, please?
13
MR. SCHNELL: Oh, boy.
I'm probably weak on dates,
14
Julie, but I think -- you know, this is something
gas cap
15 water injection was looked at back in the early '70s. I
16 remember plugging it into a 2D three phase reservoir simulator
17 model that I was running back as early as about 1971 and '72.
18
I think the unit began looking very seriously at this in the
late '80s, early '90s. And I think there was work that was
done in-house by certain Exxon, and ARCO, and I'm sure BP as
19
20
21 well. Then the unit team was formed I believe in, what, 1991.
22 And that team has been active from then, you know, through
23 really this last spring when the project was sanctioned.
24
COMMISSIONER HEUSSER: So basically this project or a
25
variation of this has been under consideration since the early
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1
'70s, even before Prudhoe Bay field came on line?
2
MR. SCHNELL: That's right.
3
COMMISSIONER HEUSSER: Okay. So this is not a project
4 that was just thought up yesterday, this is a project that has
5 been considered over a fairly lengthy period of time?
6
MR. SCHNELL: That's right. We considered it from the
7 beginning and, you know, one of the first things that I
8 learned about this project in the early runs that I made was
9 that you could inject too much water too soon relative to the
10 producing life of the oil run.
11
COMMISSIONER HEUSSER: Thank you, that's all my
12 questions.
13
CHAIR TAYLOR: Thank you very much.
14
COMMISSIONER HEUSSER: Oh, I do have one other
15 request. Just like with Mr. Maguire's presentation, your
16 exhibit that's presented on page six, could you provide us
17 with a copy that.....
18
MR. SCHNELL: Eight and a half by 11 version?
19
COMMISSIONER HEUSSER: Yes, please.
20
MR. SCHNELL: You bet.
21
COMMISSIONER HEUSSER: Thank you. For our record.
22
MR. SCHNELL: Okay. Next Jerry Brady will discuss the
23 surveillance of the project.
24
CHAIR TAYLOR: Thank you.
25
MR. BRADY: Good morning.
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1
CHAIR TAYLOR: It's a surprise chair for you. There
2 lS actually a lever on either the left or the right side
3 one of them actually locks it into place, if that's.....
4
COMMISSIONER SEAMOUNT: Be careful, though.
5
MR. BRADY: I'll take it as it is. My name is Jerry
6 Brady, B-r-a-d-y. I'd like to be sworn and qualified as an
7 expert witness in petroleum engineering.
8
CHAIR TAYLOR: Would you raise your right hand,
9 please?
10 (Oath administered)
11
MR. BRADY: Yes.
12
CHAIR TAYLOR: Please proceed with your
13 qualifications.
14
MR. BRADY: I'm a Staff Engineer for BP Alaska
15 currently working as a Production Engineer on the Gas Cap
16 Water Injection project. I received a Bachelor of Science
17 Degree in petroleum engineering from Montana Tech in 1980. I
18 began my career with ARCO International in 1981 and moved to
19 Alaska in 1984 for ARCO Alaska. Since then I have worked on a
20 variety of production engineering projects in Alaska. I began
21 working on the GCWI surveillance plans in 1993.
22
CHAIR TAYLOR: Thank you. Commissioner Seamount,
23 Commissioner Heusser, do you have any questions or any
24 objections?
25
COMMISSIONER SEAMOUNT: No objections.
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COMMISSIONER HEUSSER: No objections.
2
CHAIR TAYLOR: Please proceed.
3
I will now testify about surveillance for
MR. BRADY:
4 the Gas Cap Water Injection project.
5 Let's begin with the objectives of the GCWI
6 surveillance plan. The objectives are to monitor the project
7 performance and ensure that the injection project is
8 performing as expected.
Critical elements of the plan are the
9 monitoring of the injection well conformance, water movement,
10 and reservoir pressure.
Injection well monitoring ensures
11 that the water injection is contained in the desired reservoir
12 interval. Water movement monitoring is assuring that the
13 water moves in the reservoir as expected. General waterflood
14 movement will be monitored using 4D surface gravity and
15 downhole pulsed neutron logs in offset wells. The leading
16 edge of the waterflood will be detected primarily with pulsed
17 neutron logs. Reservoir pressure will be obtained with the
18 current pressure reporting requirements for the Prudhoe Bay
19 oil pool.
20 The first component of the GCWI surveillance plan is
21 water injection well monitoring. The injection wells will be
22 monitored with surface measured temperature, pressure, and
23 injection rate. These measurements will be similar to other
24 injection wells within the Prudhoe Bay pool. With these
25 measurements it is possible to monitor injection
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1 characteristics, particularly changes in inject- -- in the
2 injectivity indices. The injectivity indices provide direct
3 evidence of changes in well performance.
4 Downhole measurements will be -- will provide
5 confirmation of the surface measurements and will also help
6 describe reservoir properties and hydraulic performance.
7
Downhole temperature logs will provide verification of
injection conformance and confirm that the fracture height
growth is confined within the Ivishak. Downhole pressure
8
9
10 measurements will be used to determine tubular pressure drop
11 and hydraulic performance.
Pressure falloff tests will be
12 undertaken to determine reservoir properties and wellbore
13 skin.
14
Water movement lS monitored to make sure it remains in
15 zone and it remain- -- and it moves as expected. Two
16 techniques will be utilized to provide information on the
17 water movement. They are pulsed neutron logging in off- in
18 offset wells and 4D surface gravity survey.
The pulsed
19 neutron logging will provide the downhole information on which
20 zones are being flooded, along with the regional information
21 on where the water is moving.
4D gravity will augment the
22 pulsed neutron logging by providing general water movement
23 information.
24 The next major component of the surveillance plan is
25 the pulsed neutron logging. This slide highlights the
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1 approximate area of interest for early time pulsed neutron
2 logging program.
3 The light blue region surrounded by the heavy dashed
4
line is the area of primary interest.
In the center of the
5 blue reglon lS a smaller dashed line that shows the proposed
6
location of the water injection wells.
The wells to be logged
7 will be selected from the suite of wells shown as green dots.
8 These wells are primarily Lisburne producing wells, none of
9 which have known cement problems that would prevent
10 confinement of injection into the Ivishak.
11 Pulsed neutron logs, specifically the RST logs, were
12 chosen because they can be run in the Lisburne wells completed
13 with two and seven-eighths inch tubing. They can also be run
14 in two modes to collect data for discerning a major change In
15 fluids, sigma and carbon/oxygen. The RST will help locate the
16 leading edge of the waterflood. It will also provide data in
17 determining the regional waterflood coverage.
18 The 4D gravity technique utilizes very sensitive
19 surface gravity measurements taken periodically. The method
20 measures small changes in gravity as the low density gas is
21 replaced with the higher density water. Baseline measurements
22 will be taken prior to water injection. Subsequent
23 measurements will be made at discrete time intervals and
24 compared to the baseline measurements. An increase in the
25
density of the fluids in the gas cap indicates the presence of
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1 water.
2
This slide shows the area for gravity monitoring which
3
covers the area of expected water movement.
The gravity
4 stations are shown by red dots. The center portion of the
5 gravity grid is the most important region and it is set up on
6 a 2,500 foot grid spacing. The center is also overlain with a
7 few closely -- with a few more closely spaced gravity lines to
8 improve the lateral sensitivity of the gravity processing.
9 Finally, the outer portion of the gravity grid is set up on a
10 station spacing of 5,000 ft.
11 The 4D gravity technique will enable us to map general
12 water movement, determine an average waterflood front, and
13 provide a means to perform a mass balance of injected water.
14 The major limitations of the 4D technique is that it cannot
15 detect small horizontal or vertical flood fronts and it cannot
16 provide any downhole zonal information.
17 In summary, the major components of the GCWI
18 surveillance plan are, one, injection wells will be monitored
19 as other water injection wells within the Prudhoe Bay pool.
20 Two, PNLs in -- in existing wells will provide downhole and
21 regional data on the water movement.
Three, 4D gravity will
22 provide a general view of water movement. And four, reservoir
23 pressure monitoring will be done according to Prudhoe Bay pool
24 rules.
25
This concludes my prepared testimony. Are there any
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1 questions?
2
CHAIR TAYLOR: Commissioner Seamount?
3
COMMISSIONER SEAMOUNT:
I guess I have no questions at
4 this time. Thank you.
5
CHAIR TAYLOR: Commissioner Heusser?
6
COMMISSIONER HEUSSER: I do have several. The first
1S just a - - the basic request for BP to provide the exhibit
on page five and page SlX in kind of eight and a half by 11
7
8
9 size so it can be read, for our record. Jerry, what
10 surveillance options were considered -- or what was the range
11 of surveillance options that were considered for this project?
12
MR. BRADY: Well, obviously early on, the first
13 requirement that we looked at was the well spacing and seeing
14 what wells were there to try and use traditional methods to
15 log, you know, through using Lisburne wells, exploration
16 wells, whatever wells that might be in the area. After taking
17 a look at the spacing of those wells in the area where water
18 injection was, we considered other possibilities and that's
19 when we looked at the 4D gravity. We also briefly looked at
20 4D seismic. Those are the two that come to mind right away.
21 I think there were others, Julie, but I don't remember right
22 off.
23
COMMISSIONER HEUSSER: Was the option of using any of
24
the newly drilled water injection wells for early surveillance
25
one of the options that you considered?
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1
MR. BRADY: We -- I'm not -- for monitoring the water
2 move men t ?
3
COMMISSIONER HEUSSER: Yeah.
MR. BRADY: Those wells will be logged with injection
profiles as soon as the well is put on line to see where the
4
5
6 water is going within the zones in the well.
It's -- am I
7 answering your question?
8
COMMISSIONER HEUSSER: Let me ask it in a different
9 way. Were -- I know that the drilling is going to be staged.
10 Was it con- -- were any of the newly drilled wells slated for
11 water injection considered for surveillance? For example,
12 hold off on water injection in -- down one of them for the
13 first year and use it as a surveillance well to get a feel for
14 how the water is moving, l.e. is it moving as a piston or is
15 there any fingering going on?
16
MR. BRADY: So pre-drill an injection well and use
17 that as a monitoring well?
18
COMMISSIONER HEUSSER: Uh-huh, was that something.....
19
MR. BRADY: That was discussed.
I. . . . .
20
MR. RICHMOND: Yeah, I can comment on that. That was
21 discussed as a possibility, and with the presence of some of
22 the Lisburne wells and the other wells in the area, as options
23 to do the neutron logging surveillance. That option was not
24
carried forward because we had this other option that we
25
thought was more preferable, and use the wells that we drill
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1
for the injection operations and not for the surveillance.
2
COMMISSIONER HEUSSER: Okay.
So you intend to, as
3 soon as you drill these wells, put water down them right away?
4
MR. RICHMOND: Right.
5
COMMISSIONER HEUSSER: Okay.
I have another general
6 question and I'm not sure who the correct person to respond to
7 this is. We have had a question that asks, in that entire gas
8 cap area, including whatever Lisburne wells, what is the areal
9 spread of oil saturation data in the original gas cap area?
10
MR. JHAVERI: What is the area of.....
11
COMMISSIONER HEUSSER: Yeah, what wells do you have
12 data on in the original gas cap area?
13
MR. JHAVERI: For the oil saturation?
14
COMMISSIONER HEUSSER: Right, in the original.
15
CHAIR TAYLOR: Excuse me, could you just move up to
16 the table so that you're closer to the microphone, so that the
17 court reporter can pick up your voice.
18
MR. JHAVERI: Again, somebody else can help me out
19 here. What I am aware of as far as the original oil
20 saturation in the gas cap is concerned was primarily derived
21
from some of the logged wells. And I think we have a - -
actually, if not constant, we have a sort of a coalition of
oil saturation in the gas cap which averages around 7.69
22
23
24 (indiscernible). But it based on some of the logs, logged
25 wells.
I don't know if anybody else has more information.
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1
UNIDENTIFIED VOICE:
(Indiscernible) . . . . .
2
MR. JHAVERI: Okay, yeah. And -- yeah, all right.
3 And this coalition was actually evaluated with some of the oil
4 based cores from the gas cap.
5
COMMISSIONER HEUSSER: Any idea how many wells you
6 used in order to come up with your data?
7
MR. JHAVERI: Let -- you have more information than
8 (indiscernible). . . . .
9
COMMISSIONER HEUSSER: It doesn't need to be precise,
10 just kind of your best memory, kind of general range of number
11 of wells.
12
MR. SCHNELL: To my recollection, there was a lot of
13 work that was done in conjunction with redetermination of
14 participation in the gas cap oil rim. And this relied very
15 heavily on the number of key wells that were cored, oil base
16 cores, the intent being to get good initial hydrocarbon
17 saturation information. I don't remember the exact number,
18 but I think the technique and all was well described in the
19 literature papers that were written by Ed Holstein (ph), for
20 one, and I think he had an ARCO counterpart that also co-
21 authored some of these papers. But it was a very small number
22 of wells because of the extremely high cost, and this was also
23 state of the art coring at the time. But what they found in
24
general was that immediately above shales they found oil
25
saturations that on the order of 10 percent or thereabouts,
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1 and that as you got away from these shales the oil saturation
2 was less and less.
3
COMMISSIONER HEUSSER: Thank you.
4
CHAIR TAYLOR: Any other questions?
5
COMMISSIONER SEAMOUNT: No.
6
CHAIR TAYLOR: Thank you.
7
MR. BRADY: Thank you.
Perry Richmond will provide a
8 closing statement summarizing the requested changes to
9 Conservation Order 341C.
10
MR. RICHMOND: The presenters have provided summary
11 exhibits at the end of each section of testimony. We hope the
12 Commission finds this helpful when deriving findings and
13
conclusions for the Gas Cap Water Injection project.
14
In closing, I would like to reference our letter
15 submitted September 21, 2001, which contains our requested
16 pool rule changes to Conservation Order 341C.
I will
17 summarize these changes here.
18 Paragraph (d) of Rule 12 provides that the operators
19 are directed to continue to investigate options to mitigate
20 pressure decline and to provide an annual report to the
21 Commission. With the implementation of gas cap water
22 injection, BP and the other owners should not be directed to
23 continue investigating options to mitigate pressure decline
24 and provide an annual report to the Commission on such
25 activity. Therefore, we request that the Commission revoke
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1 paragraph (d) of Rule 12.
2 We also request modification of paragraph (c) in Rule
3 12 which currently provides that the operator maintain a
4 pressure differential of at least 250 psi between the minimum
5 miscibility pressure of the miscible injectant and the
6 prevailing reservoir pressure. Recognizing that gas cap water
injection will mitigate pressure decline, a more appropriate
pressure differential of 100 psi is requested based on
thermodynamic uncertainty only. This change will allow BP to
better optimize both the composition and volume of the
miscible injectant.
Finally, the Commission may wish to consider modifying
Rule 11, which describes the Prudhoe Oil Pool surveillance
report, to include the results of gas cap water injection
surveillance.
This concludes our testimony on the Gas Cap Water
Injection project. Thank You.
CHAIR TAYLOR: We've been going for about an hour and
45 minutes.
I propose a 10 to 15 minute break and we can
regroup, we can gather all our questions, see if there's any
other testimony from other members here in the audience, and
we'll come back.
So help yourself to -- I guess there's some
water here, restrooms are out in the hall.
(Off record - 10:40 a.m.)
(On record - 11:30 a.m.)
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CHAIR TAYLOR: We're back on record. It's
2 approximately 11:30, but really only 15 minutes have passed.
3 Sorry for the delay. Mr. Richmond, I think we'll start with
4 you. Jack Hartz, our senior reservoir engineer, last week
5 forwarded you some questions that a contract expert for the
6 Commission had posed, Frank Leskovich (ph). Did you receive
7 those questions?
8
MR. RICHMOND: Yes.
CHAIR TAYLOR: Did you have a chance to review those?
MR. RICHMOND: Yes, we have reviewed those questions
9
10
11 and we reviewed our prepared testimony to ensure that we've
12 covered those topics that those questions were addressing.
13 CHAIR TAYLOR: And do you feel that the testimony
14 today then addressed all those questions, or were you planning
15
on responding in some other fashion to those?
MR. RICHMOND: Yes, I think it does a good job of
addressing those questions. I did send Jack a note that if
16
17
18 the prepared testimony doesn't do a good job of covering
19 those, that -- to ask any clarification questions at the
20 hearing.
21
CHAIR TAYLOR: Okay, thank you. I think what I'll do
22 right now is turn over questions to Commissioner Heusser.
23
COMMISSIONER HEUSSER: Does Dan want to go first?
24
CHAIR TAYLOR: After you.
25
COMMISSIONER HEUSSER: Okay, let's see. I'm going to
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start basically at the front of the presentation and kind of
2 work my way back some.
Perry, I'm not sure if you're the
3 right person to answer this, so if there is somebody else
4 that's going to respond, would you please come up to the front
5 desk and state your name for our record, please. Okay, I'm
6 looking at section two -- I'm looking at page two, the plot of
7 reservoir pressure of the Prudhoe Bay oil field. And then the
8 text says that currently the reservoir pressure is declining
9 at 25 to 35 psi per year. And I note that this plot
10 represents some sort of averaged reservoir pressure, but what
11 would be useful is this pressure decline plot by major area of
12
the field as gas cap water injection affects it.
For example,
13 you know, how does the pressure in the northwest fault block
14 area respond. You know, how does the gravity drainage area
15 respond. You know, just kind of the individual areas.
16
So you'd like to comment on -- us to
MR. RICHMOND:
17 comment on how the --.....
18
COMMISSIONER HEUSSER: Yes, uh-huh.
19
. . . . . how the individual areas may be
MR. RICHMOND:
20 impacted by the.....
21
COMMISSIONER HEUSSER: Yes, the individual areas, how
22 they may be impacted by gas cap water injection, the
23 pressure.....
24
I can address that. The -- we don't
MR. RICHMOND:
25
have plots of the individual areas such as what you might get
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1 from a full field model, like taking segments out of the full
2 field model and plotting up the pressures. However, I will
3 state that the pressure support from the gas cap water
4 injection we are expecting all regions of the field to benefit
5 from this pressure support. Now the exact magnitude each area
6 will have, we don't have those details to share with you
7 today.
8
COMMISSIONER HEUSSER: Will you have those details to
9 share?
10
MR. RICHMOND: We can provide some additional detail
11 on that.
12
(Indiscernible) . . . . .
UNIDENTIFIED VOICE:
13 MR. RICHMOND: She said will you provide more detail
14 on it. Would you like us to provide that detail?
15
COMMISSIONER HEUSSER: Yes, that would be very useful.
16
UNIDENTIFIED VOICE: What kind of details do you have
17 in mind?
18
COMMISSIONER HEUSSER: A plot of reservoir pressure
19 decline by what I call major field area. You know, northwest
20 fault block, gravity drainage, WPWZ, EPWZ, Flow Station 2, and
21 then a comparison that also includes this kind of average
22 field pressure decline.
23
MR. JHAVERI: I can kind of -- Bharat Jhaveri. I can
24 kind of comment on that.
I think the key thing, this is
25 the pressure decline that we are talking about is the the
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1 weighted hydrocarbon full volume average, weighted pressures.
2 And when we look at the pressure decline in almost all of the
areas of the field, different regions that you just specif- --
you know, just said, like northwest fault block, Flow 2, you
know, updip (indiscernible), downdip (indiscernible), and all
that, what you find is that pretty much all of the areas on
average are declining with time as far as this pressure plot
is concerned.
Key thing to consider here is that there is a
pressure gradient in the field, so in general the areas which
are closer to the gas cap, they are at higher pressure than
compared to the area that is, you know, down deep. You know,
mostly because the pressure in the -- you are injecting gas in
the gas cap, so there is somewhat higher pressure while you
are
your pressures sink in the oil rim.
So as the pressure
sinks, it is (indiscernible) out of the oil rim sometimes at
the lower pressure.
And typically you are looking at the pressure gradient
in the field, from the gas cap to the oil rim, that could be
as much as a few hundred psi (indiscernible).
So what you
will see is a -- you know, in general is the pressure
declining in the field, typically around this block, and this
is an average pressure which is hydrocarbon weighted average
pressure of all these areas. But you'll see a -- you know,
some gradient between the polygons (ph) which are closer to
the gas cap.
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COMMISSIONER HEUSSER: Yes. Okay, thank you.
I am
2 looking at section six, and it's the area of pulsed neutron
3
logging.
It's -- I'm looking at the map here, but I have a
4 general question about the sensitivity of pulsed neutron logs.
5 Jerry, what is the sensitivity spin of measurement of pulsed
6 neutron logs when you go from an environment that's 80 percent
7 gas and, you know, when you inject water it goes to 80 percent
8 water?
9
I can't remember off the top of my head.
MR. BRADY:
10 We did get -- Schlumberger did model their RST in the sigma
11 mode to determine the difference between the gas cap with gas
12 versus with water.
It's significant.
It's greater than what
13 you would certainly see trying to monitor the difference
14 between oil and water.
I'm sorry, I can't remember off the
15 top of my head what those numbers were, but it was several
16 sigma units.
17
COMMISSIONER HEUSSER: Okay.
So when you're doing a
18
comparison
you know, a time lapse comparison, the
19 difference in measurements is so significant that kind of the
20 statistical part of it washes out? I mean, so you will truly
21 see a difference?
22
MR. BRADY: According to their models, we should be
23
able to see a significant change.
It should be greater the
24 oil/water change.
25
COMMISSIONER HEUSSER: Okay.
I believe that when we
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1 asked a question about hydrocarbon saturation in the gas cap,
2 I heard, I think it was Lynn, say that the open hole logs were
3 calibrated to some oil base cores? And are there plans to log
4 these new water injection wells?
5
MR. BRADY: I'm sorry, what was the last part again?
6
COMMISSIONER HEUSSER: Are there plans to log these
7 new water injection wells? Open hole log them?
8
MR. BRADY: Yes, we will
we're planning on open
9 hole logging them, but I'm not sure if we've come up with the
10 actual logging program yet at this time.
11
COMMISSIONER HEUSSER: Okay. And if you're going to
12 do an open hole logging program, are you going to go ahead and
13 see how the results of these open hole logs fit in with that
14 little -- the model that you have that calculates hydrocarbon
15 saturation based on the model developed from the oil base
16 cores and those original logs?
17 MR. BRADY: I'm not sure that we've made plans for
18 that at this point. I don't think we've developed the
19 detailed drilling program and logging program to go into it at
20 this point.
21
COMMISSIONER HEUSSER: There is still some question
22
about what the hydrocarbon saturation is in the eastern part
23
of the gas cap and we were wondering what technique you were
24
going to use in order to, you know, kind of evaluate that and
25
give yourself a starting spot.
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MR. RICHMOND: You're talking about in reference to
2 the current saturation conditions.....
3
COMMISSIONER HEUSSER: Right.
4
.... .In that part of the field?
MR. RICHMOND:
5
COMMISSIONER HEUSSER: Uh-huh.
6
MR. RICHMOND: Yeah, right now we do not have a
7 surveillance plan completed that would include further
8 quantification of the saturations in that part of the field.
9 The sanctioning of the project is based on the confidence that
10 we have in the saturation based on our modeling of that part
11 of the field and our understanding of the
of the general
12 saturation from the cores and the history of how the fluids
13 were initialized in the reserVOlr. And we rely a lot of our
14 anticipated saturations on that historical knowledge.
15
COMMISSIONER HEUSSER: So I -- did I hear you say that
16 you hadn't firmed up your plans or that you didn't intend to
17 take a well or two and look at saturations in that.....
18
MR. RICHMOND: We don't have.....
19
. ... . eastern gas cap area?
COMMISSIONER HEUSSER:
20
MR. RICHMOND: We haven't finalized our plans yet on
21 the wells that we're going to be drilling. The surveillance
22
related to the saturation question that you bring up is still
23
a possibility, but I want to be clear, though, that we don't
24
have any current plans, though, to even include that into the
25
surveillance plans, but it's still a possibility that we could
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1 consider.
2
COMMISSIONER HEUSSER: What kind of time frame are you
3 looking at to firm up your drilling and open hole logging
4 plans?
MR. RICHMOND:
Probably over the next few months. As
we head into next year, we will be trying to firm up our
drilling plans.
COMMISSIONER HEUSSER: Okay.
I've got a question from
our staff.
I understand -- or we understand that the
estimated recovery in the gas cap was on the order of 50
million barrels. And are you able to provide us with
estimated recoveries for residual oil and condensate to help
us put this 50 million barrels in perspective?
MR. JHAVERI: Let me understand the question again.
The net recovery in the gas cap, as I said earlier, was minus
20, which is made up of plus 30 in the non-invaded vapor --
non-water invaded area, and minus 50 in the water invaded
area. Your question is the estimate of this minus 50 in terms
of -- in terms of, you said, relic.....
COMMISSIONER HEUSSER: Right.
MR. JHAVERI:
I'm sorry, you said.....
COMMISSIONER HEUSSER: Basically gas cap liquids, a
total recovery.
MR. JHAVERI: Total -- maybe I'm not quite sure what
you're asking, because the minus 50 represents basically the
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1 total recovery that you would have from this area of the gas
2 cap had you not done the gas cap water injection, which would
3 be a (indiscernible) of total liquids that would have been
4 there at the end of the field life. And then the gas cap
5 water injection scenario would give you a recovery. And the
6 difference between the two in this region, in the water
7
invaded area, is minus 50.
So that is the estimate.
I'm not
8 really clear on what you're.....
9
COMMISSIONER HEUSSER: Okay. You know, I haven't
10 asked the question very well and what I'd like to do is allow
11 one of our staff to ask the question better than I have. Jack
12 Hartz, would you please ask the question?
13
MR. HARTZ: Yeah, Jack Hartz at OAGCC.
14
CHAIR TAYLOR: Would you come to the microphone,
15 please?
16
MR. HARTZ: The question does not
you've
17 characterized the loss of gas cap liquids in your
18 presentation.
I just wanted to see it
or we wanted to see
19 it put in perspective of the estimated recovery of liquids
20
from the gas cap over the life of the field.
I believe
21 there's a component of retrograde condensate as well as
22 vaporized residual oil that are going to be recovered from the
23 gas cap, and just to give us a perspective of that total
24 recovery from gas cap liquids with respect to the projected
25 losses based on the gas cap injection scenario. That's the
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1 question.
2 MR. JHAVERI: Okay, I can answer again, you know, some
3 of that right now. If you were to look at the total recovery
4 from the gas cap in the base case, and again I'm going to talk
5
in terms of order of magnitude.
So, you know, I'm going to
6 quote some numbers, but they are order of magnitude. They are
7 not -- they are out of the top of my head, you know. And we
8 are looking at -- if you didn't do a gas cap water injection,
9 and if you look at all the total liquids that would have been
10 left in the gas cap, that would include vaporization of the
11 original oil saturation which I mentioned earlier, which was
12
7.69 percent on average in the gas cap.
That oil
13 vaporization, plus any original liquids that are held by the
14 gas in the gas cap, altogether within the gas cap in the base
15 case would be of order of -- you know, I'm just going to say a
16 number off the top of my head. Anyone here can correct me.
17 You know, 800 million sort of number I'm looking at.
18 What this means is that when you end up doing the gas
19 cap water injection, from the area which includes both the
20 invade and non-invaded area of the gas cap, you would have
21 about 20 million barrels left, which means it's a very small
22 percentage of the total recovery coming out of the gas cap.
23
MR. HARTZ: Yeah, we wanted that perspective.
24
MR. JHAVERI: Okay, I hope I helped.
25
COMMISSIONER HEUSSER: Bharat, you're probably the
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1 correct person to answer this next question, too. What kind
2 of worst case recoveries did you see?
3
From the model?
MR. JHAVERI:
4
COMMISSIONER HEUSSER: From the model, uh-huh.
5
MR. JHAVERI: The worst case recovery from the model
6 that we have seen are around 150 to 170 million barrels.
Some
7 of the lowest numbers actually were a result of lower than
8 650,000 barrels per day of water injection into the gas cap.
9 For example, if we inject the water for -- as Perry Richmond
10 showed, which is not 650, but it's a ramp up, we can get at
11 less -- as much less as 175 million barrels. And some of the
12 worst case scenario on top of that, we could get as less as
13 100, 150 million barrels out of the full field model.
14
So basically the worst case
COMMISSIONER HEUSSER:
15 scenarios that you've just described are really a function of
16 water injection rate. Did you have any cases where -- did you
17 identify a worst case where perhaps you had non piston-like
18 displacement?
19
MR. JHAVERI: No, in fact, that's a very good
20 question. We must have tried for -- a lot of people over many
21
years tried to come up where you would have a worse than a
piston-like displacement for a variety of reservoir
description sensitivity, and we couldn't. And the reason
22
23
24
being, as we have talked about in the testimony today, that
25
the water displacing gas inherently set up the variable
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1 mobility ratio displacement. That it basically -- the
2 reservoir hydrogeneity (ph) is basically not a parameter.
3 It's not important. So much hydrogeneity you might have. So
4 essentially it dissipates (indiscernible).....
5
COMMISSIONER HEUSSER: Okay. Is -- what triggers in
6 your surveillance operations would cause you to shut off gas
7 cap water injection?
8
MR. RICHMOND: The surveillance data we'll be taking
9 over the years of the project, we'll be continually digesting
10 that information. So anything that we see as it relates to
11 water movement that's different than our expectations, we'll
12 have to study that and adjust to that. And as far as the
13 actions that we would take at that point, I really can't say
14 right now until we see the outcome that would make us want to
15 do a change. One change that would be possibility would be
16 the cumulative water that we would inject into the gas cap.
17 The project that we've shown you today is approximately a 20
18 year project. We'll continue to monitor the project and see
19 if we want to continue on that course as we review the
20 surveillance data.
21
COMMISSIONER HEUSSER: Is there a chance that the
22 project could be shorter lived?
23
MR. RICHMOND: There is that chance.
24
COMMISSIONER HEUSSER: Fifty-fifty? Sixty-forty?
25
Eighty-twenty?
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MR. RICHMOND: And I would -- our 20 year project is
2 what we've, you know, based these benefits on. But when you
3 say 50/50 or some percentage, if you're going to go higher and
4 lower, I think there's a reasonable chance it'd be both longer
5 and shorter. We don't really have a preferred outcome when it
6 comes to any kind of statistical opinion on being longer or
7 shorter.
8
So the modeling and
COMMISSIONER HEUSSER:
9 surveillance that you'll be doing will allow you to -- will it
10 allow you to expeditiously evaluate whether or not this
11 project is proceeding as you expect it?
12
MR. RICHMOND: We are very intent that our
13
surveillance will give us a -- good information for making
14
those decisions, but I can't -- I can't say until we actually
15 see those results how -- how complete the story will be when
16 it comes to -- how every barrel of water we would inject,
17 exactly where its locale is in the reservoir.
So we'll just
18 have to look at those evidence in composite and see where that
19 information leads us.
20
I have a question on -- it's in
COMMISSIONER HEUSSER:
21 your conclusion remarks.
I believe it's paragraph three. One
22 of the things that BP has requested is a -- instead of a 250
23 psi pressure differential, you're requesting 100 psi pressure
24 differential? And we've got some great history here at the
25
Commission, and I didn't understand where the 250 came from,
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1 but I've been told that the 250 psi represents a 30 psi
2 pressure decline plus a residence time of the fluids in the
3
reservoir of five years plus 100 psi buffer.
So if you're
4 asking for 100 psi rather than the 250, what are you basing
5 that on? How did you come up with that number?
6
MR. RICHMOND: Well, the basis for the 250 versus the
7 100 would be, if you stabilize reservoir pressure then you
8 won't have that ongoing decline in reservoir pressure that
9 that residence time, that 150 psi, which is the component that
10 was based on that ongoing decline.
So if you remove that 150
11 psi component out of the composite 250 psi, that's where you
12
end up with the 100 psi.
So that was the basis of settling on
13
the 100 pSl.
14
COMMISSIONER HEUSSER: And you're asking for this from
15 day one of the project? I mean, how long will it take for the
16 pressure decline in the field to kind of stabilize out from
17 the day that you begin water injection?
18
MR. RICHMOND: Yeah, when it comes
when it comes to
19 the length of time, I can't say exactly every point in the
20 reservoir what the time change -- what -- how much time is
21 required for the -- every subsequent year we expect the
22 reservoir pressure, on average, to be at a higher level. So
23 we think this impact will be -- at least in a 12 month period,
24 to be relevant to when it comes to looking at reservoir
25 pressure. The 100 psi that we we're requesting is actually
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1 more of a minimum.
If we see any evidence that we want to be
2 higher than 100 psi, we'd still have that flexibility. But as
3 we look at pressure being stabilized, it also gives us the
4 flexibility to go as low as 100 psi.
5
COMMISSIONER HEUSSER: Thank you.
I have two kind of
6 requests for Dan as to his question. One of the things that
7 would be very useful is what we're calling a desk size map
8 with the entire gas cap area identified, along with the wells
9
including the Lisburne monitoring wells.
Something that would
10 be similar to -- I guess the closest thing is section six,
11 page five. But a presentation that just has those gas cap
12 area wells on it, including AGI, NGI, WGI, the Lisburne
13 monitoring wells.
That would be a useful map to have. Can
14 you provide us with that?
15
MR. RICHMOND: You said desktop size? Is that what
16 you prefer?
17
COMMISSIONER HEUSSER: What's desk -- yeah, so we can
18
okay. And then my last request is
is -- because we're
19 moving into the electronic age here, can you provide us an
20 electronic copy of your presentation today, along with that
21 nice little video presentation, the powerPoint presentation
22 that shows how the fluids are moving through the reservoir?
23 Can you do that?
24
MR. RICHMOND: Yes, we can provide that.
25
COMMISSIONER HEUSSER: Great.
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MR. RICHMOND: In the format for that, we would
2 provide it in a CD. Is that okay? CD form?
COMMISSIONER HEUSSER: Yes, that would be just fine.
Thank you. That's it for me.
CHAIR TAYLOR: Mr. Seamount, do you have any
questions?
COMMISSIONER SEAMOUNT: I have no questions, thank
you.
CHAIR TAYLOR: Is the sign-in sheet someplace out In
the back of the room? Oh, here it is. Are there any
additional folks who have come in since they signed in that
would be interested in testifying this morning or in making a
statement? I see no response to that question. It appears
there's nobody else to provide either additional testimony or
statements. We will make the binders that you provided to us
part of the record.
COMMISSIONER HEUSSER: One more question. I'll nickel
and dime you to death here. This gets back to the list of
questions that -- from Mr. Leskovich that I believe that
you've seen. And it has to do with wetability. And the
question that I have is is that previously we have heard
testimony identifying concern if water was injected into the
gas cap, and I'm just going to pull a few sentences from this
list of questions. But one was -- one of those was that the
gas cap rock tends to be oil wet. Oil wetability at lower
METRO COURT REPORTING, INC.
745 West Fourth Avenue, Suite 425
Anchorage, Alaska 99501
(907) 276-3876
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1 water saturation such as found in the Prudhoe Bay gas cap
2 could present problems. And he goes on to say in an oil
3 reservoir it's normally unadvisable to inject water if the
4 rock is oil wet because of the high residual saturations.
5 What would happen in the Prudhoe Bay gas cap with its relic
6 oil saturation likely to be filling the smaller pore spaces?
7
MR. JHAVERI: Yeah, I can -- likely -- following that
8 question, we actually did modify our attitude thinking of our
9 testimony, and that is that in the way we deal with
this is
10 out in the gas cap, the residual oil that is in the gas cap,
11 is basically immobile, and that it won't move. And the second
12 thing is that the water that is injected into the gas cap does
13
actually trap that oil, and in addition it will also trap gas.
14
So in the base case, you're not
COMMISSIONER HEUSSER:
15 recovering any of this residual gas cap oil?
16
MR. JHAVERI: Even -- that's correct.
Even in the
17 base case, that reliced (ph) oil is not going to be residual
18 oil however we say that.
It's not going to have any recovery
19 by mobility in the oil phase.
In fact, that is one of the
20 reason we are -- the gas injection, that is the only way we
21 can recover any hydrocarbons from this oil is by vaporization.
22
COMMISSIONER HEUSSER: Okay.
I believe that you've
23 answered his question, thank you.
24 CHAIR TAYLOR: Mr. Richmond, with respect to the
25
additional materials that you were going to submit to the
METRO COURT REPORTING, INC.
745 West Fourth Avenue, Suiie 425
Anchorage, Alaska 99501
(907) 276-3876
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1 Commission, I'd like to keep the record open until such time
2 as those materials arrive. Do you have some indication about
3 how long that would be?
4
MR. RICHMOND: We'll try to get you as soon as
5 possible. So if not today, over the next couple of days.
6
CHAIR TAYLOR: Shall we say by next Monday? November
75th?
8
MR. RICHMOND: If you receive -- if you receive it
9 earlier than that, does the record become closed sooner? Or
10 how does that work?
11
CHAIR TAYLOR: I hadn't thought about it. We can
12 treat it as having closed at the time that we get it in,
13 unless we have some additional questions that we would forward
14 to you. So I'll keep the record open until the 5th unless we
15 receive all the information before then.
16
MR. RICHMOND: Sounds good.
17
CHAIR TAYLOR: Okay. Well, thank you very much for an
18 excellent presentation. Thank you all.
I'm sorry that we
19 stretched the 15 minute break out to 45 minutes, but we
20 appreciate your time. Thank you.
21
(END OF PROCEEDING)
22
* * * * * *
23
24
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METRO COURT REPORTING, INC.
745 West Fourth Avenue, Suite 425
Anchorage, Alaska 99501
(907) 276-3876
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C E R T I FIe ATE
2 UNITED STATES OF AMERICA)
)ss.
3 STATE OF ALASKA )
4 I, Cari Ann Ketterling, Notary Public in and for the
5 State of Alaska, and Reporter for Metro Court Reporting, do
6 hereby certify:
7 That the foregoing Alaska Oil & Gas Conservation
8 Public Commission Public Hearing was taken before Julie o.
9 Gonzales on the 30th day of October, 2001, commencing at the
10 hour of 9:04 o'clock a.m., at the offices of Alaska Oil & Gas
11 Conservation Commission, 333 West Seventh Avenue, Suite 100,
12 Anchorage, Alaska¡
13 That the meeting was transcribed by Julie o. Gonzales
14 to the best of her knowledge and ability.
15 IN WITNESS WHEREOF, I have hereto set my hand and
16 affixed my seal this 7th day of November, 2001.
17
18
Notary Public in and for Alaska
My commission expires: 07/19/04
19
20
21
22
23
24
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METRO COURT REPORTING, INC.
745 West Fourth Avenue, Suite 425
Anchorage, Alaska 99501
(907) 276-3876
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Prudhoe Bay GCWI
AOGCC Hearing
Testimony
October 30,2001
.
1. Introduction
2. Overview
3. Benefits
4. Water Movement
a. Water displacing oil movie
b. Water displacing gas movie
5. Major Gas Sales Relationship
6. Surveillance
7. Conclusion
. AOGCC Hearing - GCWI
October 30, 2001
e
e
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Prudhoe Bay GCWI
AOGCC Hearing
October 30,2001
1. Introduction
Perry Richmond
BPX (Alaska) Inc.
October 30, 2001
Introduction Exhibit 1
.
Good morning, my name is Perry Richmond. I am the East/W est Prudhoe
Bay Waterflood Resource Manager for BP Exploration (Alaska) Inc. BP is
the Operator of the Prudhoe Bay Unit.
This hearing has been scheduled to consider information supporting the
modification of pool rules for implementation of Gas Cap Water Injection in
the Prudhoe Bay Oil Pool. The Gas Cap Water Injection project is a result of
studies to mitigate reservoir pressure decline for the Prudhoe Bay Oil Pool.
It is a new element in the depletion strategy of the Prudhoe Oil Pool and will
Improve recovery.
BP has previously submitted a request for revision to the pool rules in
correspondence to the Commission dated September 21,2001.
.
Page 1
·
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I would now like to give to the Commission a copy of the Testimony and Exhibits we will be
presenting today. We will use a projector to display the exhibits as we read our prepared
testimony.
[Introduce Evidence]
The testimony we are presenting will be given by representatives of the Owners, BP,
ExxonMobil and Phillips and is divided into seven parts. I will provide an overview of the Gas
Cap Water Injection project and a summary of other pressure support options that were
considered. I will also give a closing statement summarizing requested changes to
Conservation Order 341 C. Bharat Jhaveri will testify about recovery benefits, Matt Maguire
about water movement, Lynn Schnell about the relationship to major gas sales and Jerry Brady
about surveillance.
A few notes about acronyms. We may occasionally use the letters GCWI to refer to the Gas
Cap Water Injection Project. You may also hear GD which refers to the Gravity Drainage area
of the field and GDWFI which identifies that part of the field where Gravity Drainage and
Water flood Interact. We will keep these terms to a minimum.
We are asking that each witness be qualified as an expert, and each of us is prepared to respond
to questions concerning our testimony and related exhibits.
Page 2
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Prudhoe Bay GCWI
AOGCC Hearing
October 30, 2001
2. Overview
Perry Richmond
BPX (Alaska) Inc.
October 30. 2001
Overview Exhibit 1
·
I'd now like to be sworn and qualified as an expert witness.
[Administration of Oath)
My name is Perry Richmond. I am a Resource Manager for BP, currently responsible
for managing the Prudhoe Bay water flood in the Northwest Fault Block and Flow
Station 2 areas. Technical staff in my group will be responsible for implementing
and monitoring the Gas Cap Water Injection project. I received a Bachelor of
Science Degree in Petroleum Engineering from Texas A&M University. I was
employed by ARCO in 1982 and have worked on numerous engineering projects in
Texas, Alaska, and overseas. I have worked on the Prudhoe Bay Field since January,
1998. I have been employed by BP since July, 2000.
[Acceptance as Expert Witness)
I will now provide an over view of the project.
Since field startup in 1977, cumulative production from the Prudhoe Bay Oil Pool is
now over 10 billion barrels. This surpasses the original estimate of9.6 billion
barrels. This excellent performance has resulted from optimizing total recovery by
progressively using multiple recovery mechanisms, such as gravity drainage, gas
cycling, oil vaporization, waterflooding, and miscible flooding. These same recovery
mechanisms, particularly gravity drainage and gas cycling, result in liquid
hydrocarbon and gas voidage from the reservoir, leading to a steady decline of
reservOIr pressure.
·
Page 1
Reservoir Pressure - Prudhoe Bay on Pool
0)
"'-
~
III
III
~
D.
ø
0) 3000
lIS
"'-
ø
~ 2500
October 30, 2001
Overview Exhibit 2
Exhibit 2 shows the history and forecast of reservoir pressure under the
existing recovery mechanisms. Currently, reservoir pressure is declining at
25 to 35 psi/year. The Working Interest Owners have studied options to
mitigate pressure decline and have reported annually the progress of these
studies to the Commission. As a culmination of these studies, the Working
Interest Owners sanctioned the Gas Cap Water Injection project in June,
2001. This project represents a new element in the depletion strategy of the
Prudhoe Bay Oil Pool and will mitigate reservoir pressure decline and
improve recovery.
Gas Cap Water Injection Project
· Ramp up to 650 mbd seawater into
eastern gas cap area
· Mid 2002 project start-up
· 150-200 mmbl gross reserves
700
Ii! 600
:::¡¡ 500
i
.S! 400
Ü
.!. 300
.5
! 200
~100
o
2000
2005
2010
2015
2020
2025
East Dock Injection
October 30,2001
Overview Exhibit 3
The project scope calls for ramping up to 650,000 barrels per day of
seawater into the eastern portion of the gas cap trom an injection site loc.ated
at the East Dock Staging Pad. As shown by the chart, injection increases
over time. This is caused by the availability of more seawater as demand
decreases in other projects, such as the Flow Station 2 and Point McIntyre
water floods and Grind and Inject.
Facility construction is planned for this winter, followed by start-up of
injection in mid 2002. Water injection is anticipated to continue for twenty
years, with a final injected water volume near four billion barrels. The
increase in hydrocarbon liquid recovery is expected to be 150 to 200 million
barrels.
Page
Gas Cap Water Injection - Facilities Scope
· New SWI Line, FS2
to East Dock
· STP/ESIP Upgrades
· East Dock Injection
Facility
· 5-7 Injection Wells
SiP
-~¡),,;¢¡,;
Sto__
AGI
Prudhoi!
Bay
NWGI
October 30, 2001
Overview Exhibit 4
To implement the Gas Cap Water Injection project, a new seawater pipeline
from Flow Station 2 to the East Dock Staging Pad will be constructed. The
new line will have a 32" diameter and a total length of approximately
18,000 feet. It will tie-in to the existing 32"seawater line running from the
Eastern Seawater Injection Plant to Flow Station 2.
Upgrades to pumps, piping, filters and plant control systems are required at
the Seawater Treatment Plant to accommodate the seawater demand. For
the Eastern Seawater Injection Plant, waste heat louvers will be upgraded.
A heated pig receiver/manifold module and well houses will be installed at
the East Dock Staging Pad to accommodate five to seven new injection
wells.
October 30, 2001
Overview Exhibit 5
wells.
areas
e
e
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Gas Cap Water Injection - Well Completion Plan
"",·WCIW
WElllE~D:., or.- .~..
13 :uaw TAM Port Collar _1000'
7" SCSSay ·1800'
13 3/8",... Surface CIg -.UO· SS TYD
15/8" 29.7', ST.....IPC !njullon TubinG w17~
ICC...ort..
1-5/S" . 7"lnjectlon Packe,
7" Profil.. (2)
TOL line' Hano.rl Packer -8150' S8 TVD
'-51S", 4ft I"honudlst. Cso -8210' SS TYD
7" 29. injection l.lne, -8580' as TVD
Det. Rev 8
Commenw
Oa. Cap Wet., In}ectlon
Generic Completion Design
BP Alu.8 Drilling & Wella
October 30, 2001
OvelView Exhibit 6
.
Exhibit 6 shows a representative well completion plan. Each completion
will include 13 3/8" surface casing cemented to surface, 9 5/8"
intermediate casing with cement brought to 1000' above the shoe, and a
fully cemented 7" injection liner. The tubing will be 7 5/8" and will
include a 7" subsurface safety valve and two 7" profiles. The tubing is
large to accommodate the high volume of water to be injected. The
tubing will also be plastic coated to help minimize the friction losses.
Average surface pressure for these new injection wells will be
approximately 2700 psi. Maximum injection pressure is expected to be
approximately 3100 psi.
This concludes the project overview. I will now begin my testimony on
the other pressure support options that were considered.
.
Page 6
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Gas Cap Water Injection Project
Pressure Support Options
October 30. 2001
Overview Exhibit 7
·
The Owners formed a multi-company, Pressure Studies Initiative (PSI)
Team in 1991 to evaluate pressure mitigation options for the Prudhoe
Bay Oil Pool. Prior to the PSI Team's focus on Gas Cap Water Injection,
several pressure support options were screened. These options included
supplemental hydrocarbon gas injection, nitrogen or flue gas injection,
fuel gas alternatives, additional water injection in oil rim areas, and gas
cap water injection.
·
Page 7
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Pressure Support Options Considered
Supplemental Hydrocarbon Gas Injection
c Limited sources, high cost
Nitrogen or Flue Gas Injection
c Expensive to implement
c Hurts vaporization relative to lean gas
c Contaminates gas stream
Fuel Gas Options (Import gas, oil as fuel, import electricity, gas
hydrates)
c High Cost
c Results in immediate Field Gas Offtake reduction, not attractive
October 30.2001
Overview Exhibit 8
·
Many of the options considered were not viable, primarily due to high capital costs
and/or recovery benefits limitations. These projects are summarized on Exhibit 8.
For supplemental hydrocarbon gas injection, limited gas sources exist. A Point
Thomson type source was evaluated in the screening study; however, high capital
costs associated with development, distribution, and compression facilities makes this
option unattractive.
Nitrogen or flue gas injection are also unattractive since these options would require
high capital costs for compression or air separation, result in reduced vaporization
efficiency compared to lean hydrocarbon gas, and contaminate the reservoir gas.
Options to replace the fuel gas used by Prudhoe facilities, and thereby reduce
reservoir voidage, were also screened. Fuel gas options included importing gas, using
oil as fuel, importing electricity, or developing gas hydrates. The fuel gas options are
unattractive due to high capital costs, unproven technology, and the fact that replacing
the fuel gas causes a reduction in field gas off-take, resulting in an immediate
decrease in oil rate.
·
Page 8
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Pressure Support Options Being Implemented
Oil Rim Water Injection
D Justify by overall recovery benefits of each project
D EWE waterflood, Updip Zone 4, and Updip Victor WAG currently
being implemented
D Limited pressure support potential compared to gas cap water
injection
Gas Cap Water Injection
D Low cost / high benefit potential
D Recommended for detailed study by PSI Team
October 30, 2001
Overview Exhibit 9
.
Exhibit 9 shows projects that have been identified as viable and are now in various
stages of implementation.
Projects that increase water injection into the Oil Rim areas have been justified based on
overall recovery benefits, rather than just pressure support benefits. Eileen West End
Waterflood, Updip Zone 4 Water/Miscible Injection, and Flow Station 2 Updip Victor
WAG Injection are being implemented as projects with related pressure support benefits.
However, they have limited pressure support potential when compared to gas cap water
injection.
Gas cap water injection was screened and found to have significant recovery benefits
with reasonable capital cost requirements. The PSI Team thought this option was
potentially attractive to very attractive. The PSI Team recommended gas cap water
injection be their focus for more detailed study.
This concludes my prepared testimony. Are there any questions?
Thank you. The next four presentations will describe key results from the detailed
studies of Gas Cap Water Injection. First, Bharat Jhaveri will review benefits.
.
Page 9
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Prudhoe Bay GCWI
AOGCC Hearing
October 30, 2001
3. Benefits
Bharat s. Jhaveri
BPX (Alaska) Inc.
October 30, 2001
Benefits Exhibit 1
.
Good morning. My name is Bharat S. Jhaveri. I'd now like to be sworn
and qualified as an expert witness.
[Administration of Oath)
I am a Consulting Reservoir Engineer with BP Exploration (Alaska)
Inc. since 1995. I received a PhD in Chemical Engineering from
Stanford University in 1979. I have been involved with the
development and reservoir management of the Prudhoe Bay field for
over twenty years, from 1981-1994 at ARCO and since 1995 at BP.
[Acceptance as Expert Witness)
I will now testify about the recovery benefits of the Gas Cap Water
Injection Project.
.
Page 1
4000
3500
3000
l 2500
l!f 2000
;:¡
If
~ 1500
CI.. 1000
500
o
1985 1990 1995 2000 2005 2010 2015 2020 2025 2030
..... r"" .- '" i
- ~--ww -
-. ·r····~." ,L
. . -without GCWI
-with GCWI
i
October 30,2001 Benefits Exhibit 2
e
October 30, 2001
Benefits Exhibit 3
Ii
s
October 30,2001
Benefits Exhibit 4
I now
II!
s
October 30,2001
Benefits Exhibit 5
IS
IS a
I now
III
s
October 30, 2001
Benefits Exhibit 6
As
IS more
more
I
now
/
N
s
October 30.2001
Benefits Exhibit 7
are
s
October 30,2001
Benefits Exhibit 8
e
e
.
Summary - Benefits
· GCWI arrests pressure decline
· Increased pressure improves oil recovery mechanisms
+ Vaporization
+ Gravity Drainage
+ Waterflood
+ EOR
· GCWI provides 150-200 MMB of liquid reserves
October 30, 2001
Benefits Exhibit 9
.
In summary, the gas cap water injection project outlined here arrests
pressure decline in the field and increases recovery.
All recovery mechanisms benefit from the higher pressure:
vaporization, gravity drainage, waterflood and EOR.
Total incremental liquid recovery ranges from 150-200 MMB. The
range reflects modeling uncertainties and the availability of sea water.
This concludes my prepared testimony. Are there any questions?
Thank you. Next Matt Maguire will review water movement.
.
Page 9
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Prudhoe Bay GCWI
AOGCC Hearing
October 30, 2001
4. Water Movement
Matt Maguire
Phillips Alaska Inc.
October 30,2001
Water Movement Exhibit 1
·
Good morning. My name is Matt Maguire. I'd now like to be sworn and
qualified as an expert witness.
[Administration of Oath)
I am a Senior Reservoir Engineer with Phillips Alaska, Inc., currently
assigned to the Greater Prudhoe Area Team. In 1988, I received a
Bachelor of Science Degree in Petroleum Engineering from the
University of Alaska-Fairbanks. I started working for ARCO Alaska out
of college and am currently in my 14th year of working Prudhoe Bay
engineering projects.
[Acceptance as Expert Witness)
I will now testify about water movement.
·
Page 1
October 30, 2001
Water Movement Exhibit 2
lam
water movement
cap. I
moves once it is
objectives GCWI
IS
I will correct here
area are at
we want to
can we
is to
an
Flood Front Examples
· Piston-like Flood Front
I Injection ~
"
c'"
0'1;.c~
'9 '---
'V ,,?oÇJ
.. Channeling Type Flood Front
I Injection ~
"
c'"
0'1;·c~
'9 ~
'V ,,?oÇJ
October 30, 2001
Water Movement Exhibit 3
This slide shows two flood fronts that are relevant to the discussion of this
project. Each ofthese is pictured in a 2-D cross-section.
Our preference is the piston-like flood front. This is characterized by
efficient and unifonn displacement as opposed to having channels
develop. Here, the front is stable, moves slowly, and as a result takes
much longer for water to breakthrough.
With a channeling front, it is easy to see how water breakthrough would
occur earlier. As you can imagine, this type of behavior within the GCWI
project is not desirable.
For gas cap water injection, the displacement of gas by water is very
efficient, and essentially piston-like. This is because gas is 100 times
more mobile than the water that displaces it. I will now demonstrate this
for you with a flow model.
Homogeneous Model with 5 Darcy Thief
Grid Size: 1 ac x 2 ft,
Dimensions: 42xlx50
October 30.2001
WatBr Movement Exhibit 4
1 have two reservoir simulations to show you. Each uses the reservoir description shown on this slide. The model
is 2-D cross-sectional in nature with an injector on the left and a producer on the right. The cells are 208 feet
square and 2 feet thick. The green cells have 500 md permeability and the orange ceHs 5000 md. The orange cells
represent a 20-foot thick thief zone in the middle of the model.
The main difference in the model runs will be the fluid within it. In one simulation the model contains oil; and
the other, gas. In each simulation we wil1 inject water. The purpose of these comparison cases is to show how a
high permeability zone has little effect when water displaces gas.
<Testimony just before running the water displacing oil "video">
This first simulation is of water displacing oil. Here we would expect the permeabilities to playa major role.
<Run water displacing oil video>
<Testimony during water displacing oil "video" at breakthrough point>
Note at this point that breakthrough has occurred at the producer.
<Testimony during water displacing oil "video" at the end>
This is the end of the run. Let me run this one more time.
<Run water displacing oil video second time, no comments>
As you have seen the thief zone caused early water breakthrough and channeling of the water.
Page 4
Homogeneous Model with 5 Darcy Thief
Grid Size: I ac x 2 ft,
Dimensions: 42xlx50
October 30,2001
Water Movement Exhibit 5
<Testimony just before running the water displacing gas "video">
Now let's take a look at the same simulation, however this time the model
will be loaded with gas instead of oil. So, this simulation is of water
displacing gas. Keep in mind the thief zone is in the middle of the model.
<Run water displacing gas video>
<Testimony during water displacing gas "video" at the end>
This is the end of the run. Let me run this one more time.
<Run water displacing gas video second time, no comments>
As you have seen, even a high permeability thief like this one is
significantly dampened by such a favorable displacement process.
5
Comparison of Displacements
in Thief Model
.. Water Displacing Oil .. Water Displacing Gas
- Thief causes Channeling - Effect of Thief Dampened
M>t>ot_',,,,,,.~'j....t',to_~'f:OJ!'
October 30,2001
MItØ'llW'._o'O_._'":þ$.8!
Water Movement Exhibit 6
I have one comparison slide to summarize what we just viewed. The
water displacing oil case shows the water moving significantly faster
through the high penneability channel leading to early water breakthrough.
In the water displacing gas case, the thief has little effect on the flood
front, such that the displacement is nearly piston-like. The water doesn't
channel through the gas. This is because the gas is approximately 100
times more mobile than the water. As a result, this displacement process
dampens the effect of geologically reasonable variations in reservoir
penneability.
Page 6
a
to
to
producers are
areas.
the
11/1/2010 1
GCWI Injectors
October 30,2001
Water Movement Exhibit 8
This shows the continued growth ofthe water at 2010, or after
approximately 8 years of injection.
Page 8
1111120151
GCWI Injectors
October 30,2001
Water Movement Exhibit 9
This shows the continued growth ofthe water at 2015, which is
approximately 13 years of injection.
Page 9
11/1/2020 I
GCWI Injectors
And 2020, which is approximately 18 years of injection.
Page 10
GCWI Injectors
October 30,2001
Water Movement Exhibit 11
And this is 2031. Water injection was stopped in 2022. Due to it's low
mobility the water moves very little between 2022 and 2031. So, a
picture at 2031 is almost the same as a picture at 2022.
As you can see water eventually reaches the closest gas injectors and
some oil producers at drill sites 4, 11, and 18. Let me show you the
effect on these three areas on the next three slides.
Page 11
Minimal Impact on Gas Injection
8.0
e
IJ.. 7.0
0
IQ
G) 6.0
..
(\
n:: 5.0
!: 4.0
0
.-
...
y 3.0
@
..... 2.0
!:
If¡ 1.0
(\
CD 0.0
2000 2005 2010
October 30,2001
with GCWI
2015
2020
2025
2030
Water Movement Exhibit 12
First, GCWI has a small impact on gas injection. It occurs primarily
late in field life when the gas oil ratios are higher. This impact is
incorporated into the benefits analysis.
Page 12
Q 600
11II
I 550
is 500
i
u
450
October 30, 2001
GCWI Complements Waterflood Area
DS4 <IDS 0811 Cum 011 Production
650
400
20002005 2010 2015 2020 2025 2œ0 2035
Water Movement Exhibit 13
Second, this plot shows cumulative oil production for drill sites 4
and 11 with and without GCWI. As you can see, oil recovery is
slightly higher with GCWI. is because the additional water from
GCWI drives updip oil towards the drill site 4 and 11 producers.
Page 13
GCWI Preserves Gravity Drainage Recovery
DS18 Cum Oil PrøWction
160
140
o
I:I! 120
I 100
80
Õ 60
§ 40
u 20
o
2000 2005 2010 2015 2020 2025 2030 2035
October 30, 2001
Water Movement Exhibit 14
And finally this plot shows cumulative oil production for drill site 18
with and without GCWI. Oil recovery is slightly higher with GCWI
because the water limits encroachment and displaces some updip oil.
This concludes my prepared testimony. Are there any questions?
Thank you for your time. The next section, Major Gas Sale Relationship,
will be presented by Lynn Schnell.
Page 14
.
.
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e
Water Displacing Oil in a X-Section with 5 Darcy Streak
Gtj~Síz<, 1..~2ft.
DÍIII<J"j"H" 42xlx50
......nr.....u-.'...·....
Water Displacing Oil in a X-Section with 5 Darcy Streak
GrKlSiz<;hex2f<.
f)o,,<n,ion,,41:<b5ü
................'J_..........,
Water Displacing Oil in aX-Section with 5 Darcy Streak
~~;~~:~~~:~o
......~,..,<...".....,"_.,.._.,
Water Displacing Oil in a X-Section with 5 Darcy Streak
GridSiz.,¡.<x2ft,
Dim<Il<;ons;42xb5ü
............,...'0...<._">0..,
Water Displacing Oil in a X-Section wjth 5 Darcy Streak
GridSi", 1~<, 2 fl.
Dim<n"m,,~2,]ÜO
M....~'"'."'.~...._._...U,
Ii
Water Displacing Oil in a X-5.x:tion with 5 Darcy Streak
GridSÍZ<>: lac, 2 f~
D."",,,,,,,,, 42xl<50
...........,...",....._.".'"
e
Water Displacing Oil in a X-Section with 5 Darcy Streak
addS;"., 1.o~ 2 ft.
Dim",..ion.,42.b50
_........._~....._..D.O,
Water Displacing Oil in a X~Section with 5 Darcy Streak
"...,......,...."'..".-......,
1'""'-='
'~1 ~
:.<t:
ii:m:;
Water Displacing Oil in a X~SectÎon with 5 Darcy Streak
QidS¡z."lo<x 2 ft,
Ðmen''''n'' 42xlxSû
......·rw,._"....._·...-"1
1
.
.
.
e
Water Displacing Oil in a X-Section with 5 Darcy Streak
Grid Slz~: 1acx 2 f~
Dim"",,,,,,,, ~2'1,.\O
"'....~w'.'...."....._n~.·:m."
Water Displacing Oil in a X-Section with 5 Darcy Streak
~"j:<;~:::~:2'x;:;'o
......~,........".....,_._."
Water Displacing Oil in a X-Section with 5 Darcy Streak
GridS;z"oj"O,2f1,
D;",,,",¡()];;,~2,Lt5U
......~........".....,';_._.Oi
Water Displacing Oil in a X~Section with:; Darcy Stn:ak
."'..'OW'.,..."..........._.."
Water Displacing ûil in a X-Section with 5 Darcy Streak
QridSÍ7.<:1"",2fi,
DÍII,,,,,,,ioll,,-1.hh50
".,.._.._"'....._."....,
1·';~..',1......,...,.
¡Ii
Water Displacing Oil in a X-Section with 5 Darcy Streak
C".¡,¡Siz,o 1"",2 fi,
Di>"<!"jon,,~2x],50
............<-".....,_.._...
e
I..·,·'.,...'.·.'..·.'.·..'.·.·,..i
"'-"'!
'I ~
Water Displacing Oil in a X-Section with:; Dan:y Streak
GrjdSiz<:I,,,,2fi,
DÌlne".;on,,~lxlx50
_...IW"....."'.O<._.....,
Water Displacing Oil in a X-Section with 5 Darcy Streak
GrjdSl<e:boxlfi,
DUneru;k",,,~1xlx50
".........,.....,....._._..,
Water Displacing Oil in a X-Section with 5 Darcy Streak
Grj,Sizool""xlfi.
Di","",j",,,, ~2xlx~O
-...""....."'-<......."..
2
·
·
·
e
I.',.'·"··,~·,·~··",··,
:'----j
; <
Water Displacing Oil in a X-Section with 5 Darcy Streak
GridS¡",: l"e, 2~.
D"I<II,jo",:42,1,50
................""*"',_.....01
Water Displacing on in a X-Section with 5 Darcy Streak
Ori,jSÍl~: 1.<x2 ft,
D."<".;o,,,,4;"1.50
................."...~,".........t
I';-.··.·,~.·,···'¡
-~""'
Water Displacing Oil in a X-Section with 5 Darcy Streak
~:~~:,~~:~~x~o
......_',m.""'...,._.....01
Water Displacing Oil in a X-Section with 5 Darcy Streak
". .n"'......,·_<,'_·""'~1
Water Displacing Oil in a X-Section with 5 Darcy Streak
OridSize:lacx2ft,
Di",,,,,,ion,,42x1x50
"........,......-:_,_._~1
Water Displacing Oil in a X-Section with 5 Darcy Streak
Grid Si"" ]~ox2ft.
Dimc'n5~Jns;42x¡x50
......-,'..."......-.,..""
e
Water Displacing Oil in a X-Seçtion with 5 Darcy Streak
_...IW".,_"'....._....'"
Water Displacing Oil in a X-Seclion with 5 Darcy Streak
GridSiz.,h<x2f1.
Dim<",i",,,;42>oIx5ü
......'...."...',...,..........,.,
Water Displacing Oil in a X-Section with 5 Darcy Streak
GridSi>;<:t"cx2f1,
D'n<",jon",¡:;x1x50
.....·....,<...".....,_·....b'
3
·
·
·
e
Water Displacing Oil in a X-St:<.:tion with 5 Darcy Streak
Or¡<¡S¡z."jacx2ft.
Dirncn,jo",,4:!xlx.lO
......~..-."..."..,...~_....,"
Water Displacing Oil in a X-Section with 5 Darcy Streak
r"idSiu,!.cx2 f"
D¡""'r",".,,, 42x!xSü
M....~...."..~.._....,.'
Water Displacing Oil in a X-Section with 5 Darcy Streak
......'SW'.....-::"...._.-...
!I'·'·'·'··¡¡¡
!:. ~;::::- ~
!-._".....~:.;
il
Waler Disp!acing Oil in a X-Section with 5 Darcy Streak
GrÚISiz<:].cx2f,.
Dimc",;ons:42xl.SO
"......"'.,...~-,_....~,
1·"··11
-:-
I'.,....'
I ~~---: i
Water Displacing Oil in a X-Section with 5 Darcy Streak
~::;~:':,;~~~~x~o
......~..."...",....,'...·_~1
I'···,·,·,·,···.·".··.··..··.'.....'".......,...'
""",,=1
-,
Water Displacing Oil in a X-Section with 5 Darcy Streak
......_.....-::......._·"'x.-'"
e
Water Displacing on in a X-Sectíon with 5 Darcy Streak
Gr.ISiz"lacx2ft,
Dirncn.¡""., 42x!x50
_............'[J_<._..."..,
Water Displacing Oil in a X-Section with 5 Darcy Streak
......~\O'".....'attiO".~_._..,
Water Displacing Oil in a X-Section with 5 Darcy Streak
"'...._.....~.~_·'....01
4
·
·
·
e
I·"'·········.··.··.'···.'·'.·····.·
¡' ~
i; ~-i
I_of';::
ilii.
Water Displacing Oil in a X-Section with 5 Darcy Streak
_".........."0>....,....·'000..'
Water Displacing Oil in a X-Section with 5 Darcy Streak
_"sw.....'C.......m.·'.n...
1'··'····-···...···.···.·.···.
».
. ,
Water Displacing Oil in a X-Section with 5 Darcy Streak
GridS".ol.oxlft,
Dim",,<j(m,,~2,1x50
...."..........-:¡".........,-"
Water Displacing Oil in a X-Section with 5 Darcy Streak
...........,....",.........·"".01
Water Displacing Oil in aX-Section with 5 Darcy Streak
OridSiz.,1.cx2n,
Oim.nsionsc42xlx50
......_,....'1:,..........'''''''..,
Waler Displacing Oil jn a X-Seçtion with 5 Darcy Streak
................':]".........,......,
e
Water Displacing Oil in a X-Section wi!h 5 Darcy Streak
"'...._.....~_._."..,-'>1
Water Displacing Oil in a X-Section with 5 Darcy Streak
...........-....."...........","'-,,,
Water Displacing OJ] in a X-Section with 5 Darcy Streak
.........,...,....-;:.....,U...·'»OM
5
·
·
·
e
Water DispJacing Oil in a X-Section with 5 Darcy Streak
......_.....""....."·'300,"
Water Displacing Oil in a X-Section with 5 Darcy Streak
......_.....U...'.....='_.01
Waler Displacing Oil in a X-Section with5 Darcy Streak
~;:;~~~:~~;,;:~'o
......no.....""........·,_."
e
Water Displacing on in a X-Section with 5 Darcy Streak
...p..-....."'...........,.,""
6
·
·
·
Water Displacing Gas in a X~Section with 5 Darcy Streak
Gti<1 SÌl<e]",,' 2 fl.
Dim"".ion,,~1,1,50
-"'.....,....~..,,'._..,"
Water Displacing Gas in a X-Section with 5 Darcy Streak
~~~C;'~:'~:;~;' ~,~o
_.._.....'G,_._....~,
Water Displacing Gas in a X-Section with 5 Darcy Streak
.,..........,..."'...~._.,""..,
e
Water Displacing Gas in a X-Section with 5 Darcy Streak
~~:e~'~;:':":~, ~ :.~o
......_.....~"',_.->...,
Water Displacing Gas in a X-Section with 5 Darcy Streak
_............'0...<._."'''...
Water Displacing Gas in a X-Section with 5 Darcy Streak
~~.:';~~~:~;,~'o
-..-....."'"<,......".,
e
Water Displacing Gas in a X-Section with 5 Darcy Streak
g~..
::1 ~
....':
gr:,~~;:,:;:;,~:.~o
...".....,...."................
Water Displacing Gas in a X-Section with 5 Darcy Streak
I···¡
'..'.',' J
......_.....D.........·".'"
Waler DispJacing Gas in a X-Seçtion with 5 Darcy Streak
Ii
......"........"................
·
·
·
Water Displacing Gas in a X-Section with 5 Darcy Streak
_"'SW'.,..."_._.",,,..,
Water Displacing Gas in a X-Section with 5 Darcy Streak
_of..........m.or,_·""'..,
Water Displacing Gas in a X-Section with 5 Darcy Streak
~~.~~~~~~~,~x~o
-............"'.....-......,
e
Water Displacing Gas in a X-Section with 5 Darcy Streak
-.......,...."..........--'"
Water Displacing Gas in a X-Section with 5 Darcy Streak
~~.~,~~;,~~:; ~:.~'O
_..,."......m.or,_.·_-"'
Water Displacing Gas in a X-Section wilh 5 Darcy Streak
-..-.-."................
e
Waler Displacing Gas in a X-Section with 5 Darcy Streak
·I!E-
. .-.
1ã¡
_"_.'...0.......,.·""'...
Water Displacing Gas in a X-Sectîon with 5 Darcy Streak
-,,-.....""'.........-...-"'
Water Displacing Gas in a X-Section with 5 Darcy Streak
1······.·.·.·.-·.··..·..··.······.......
r------"~¡¡}
:~;
,'" ;;;
......-....."...........,....
2
·
·
·
Water Displaçing Gas in a X-Section with 5 Darcy Streak
I..····'..·.·.·.·..····'·······
".
',,-,'- Ii
.................-0.....,.........,
Water Displacing Gas in a X-Section with 5 Darcy Streak
"'.....iW'......,...<._....,..,
Wat<:r Displacing Gas ill a X-Section with 5 Darcy Streak
.........,.,...O::....._·T20b'
e
Water Displacing Gas in a X-Section with:; Darcy Streak
I'····.·'·.i~...·...................'.
~:~
'\ - .: i
-".........."..".......".,
Water Displacing Gas in a X-Section with 5 Darcy Streak
·I···~··.···.·...··.···..·..··.'··.··..·.........................
:'~"
_........,...~.."....·..oøt
Water Displacing Gas in a X-Srxtion with 5 Darcy Streak
......,,.........,,_.......,.....,
e
Water Displacing Gas in a X-Section with 5 Darcy Streak
................ú.........·_'"
Water Displacing Gas in aX-Section with 5 Darcy Streak
-............"'...............
Water Displacing Gas in a X-Section with 5 Darcy Streak
1.··..-·······'·······'··.'
......"" ,
-..-....."..........,.....,
3
.
.
.
Water Displadng Gas in a X-Seçtion with 5 Darcy Streak
-........,...""....-..,.'"
Water Displadng Gas in a X-Section with 5 Darcy Streak
_"'iW".,...~....._._-'I1
e
Water Displacing Gas in a X-Section with 5 Darcy Streak
_ot..........,,_.....·_.,
Water Displacing Gas in a X-Section with 5 Darcy Streak
_".....,_"..........-»0.0'
e
Water Displacing Gas ín a X-Section with 5 Darcy Streak
....".........."............,...,
4
e
e
.
Prudhoe Bay GCWI
AOGCC Hearing
October 30, 2001
5. Major Gas Sale Relationship
Lynn W. Schnell
ExxonMobil Production Co.
October 30. 2001
MGS Relationship Exhibit 1
.
Good morning. My name is Lynn W. Schnell. I'd now like to be
sworn and qualified as an expert witness.
[Administration of Oath)
I've been employed by ExxonMobil Production Company and its
predecessors since graduating from Washington State University in
1965 with a BSEE. I have been involved with the development and
reservoir management of the Prudhoe Bay Field almost continuously
since June, 1968.
[Acceptance as Expert Witness)
I will now testify about the relationship of a major gas sale to the Gas
Cap Water Injection Project.
.
Page 1
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e
.
GCWllnteraction with Major Gas Sales
· Focus is on the impact of
¡.. Gas sales on GCWI recovery benefits
¡.. GCWI on gas recovery
· Reservoir pressure maintained at higher level
· MGS reduces GCWI oil recovery estimate
· Gas recovery is preserved
October 30, 2001
MGS Relationship Exhibit 2
.
The purpose of this presentation is to address the interaction of the Gas
Cap Water Injection project with a potential major gas sale. The
primary focus will be on how a gas sale would impact the estimated
benefits of the project. The secondary focus will be on how gas cap
water injection is expected to impact ultimate gas recovery.
Since the timing and rate of a gas sale have yet to be determined, a gas
sale will be addressed broadly. As such I will focus on the mechanisms
involved, and will not try to quantify these factors.
In general, the water injection project will maintain reservoir pressure at
a higher level under any currently foreseeable gas sales scenario.
A gas sale will reduce the incremental oil recovery from gas cap water
injection. This will be shown and explained.
Finally, the impact of the project on ultimate gas recovery will be
addressed. I will show that gas recovery potential is virtually unchanged
when compared to a no gas cap water injection case.
.
Page 2
Higher Pressure Maintained by GCWI
5000
1000
,ii
~ 3000
2!
::¡
<II
~ 2000
0..
o
2010
2020
2030
2040
2050
Year
October 30. 2001
MGS Relationship Exhibit 3
This chart represents the average reservoir pressure as predícted by the BP
fun field model. It shows that gas cap water injection results in a
uniformly higher reservoir pressure with a major gas sales; this case,
approximately 140 psi.
The blue dashed curve shows the pressure declining at until
a 4 Bcf/d gas sale in 2008, at which time the pressure drops at about
135 psi/year through 2025. The rate of pressure decline is proportional to
the gas sales decline moderates later years as
gas sale rate pressure depletion.
The solid green same gas sales scenario; but with gas cap
water injection. reservoir pressure remains essentially constant
until the start in 2008. . At that time the pressure parallels the
case without relationship is characteristic of other gas
sales rates and
The
the oil recovery
depicted in the next chart.
the project means that even with a
will operate more efficiently.
GCWI Recovery Reduced by MGS
250
CD
~ 200
.
è:'
~ 150
o
u
&!.
¡¡¡ 1 00
ë
CD
E
I!! 50
u
.E
o
2000
2005
2010
2015
2020
2025
2030
October 30, 2001
MGS Relationship Exhibit 4
This graph shows the cumulative incremental oil recovery due to gas cap
through 2030. While the gas sale reduces the recovery, the incremental
significant; and the project remains viable.
The upper dashed blue curve represents the 200 MMB shown in Bharat
presentation. The solid green curve represents the 135 MMb incremental oil recovery
with a 4 Bcf/d gas sale starting in 2008.
This reduction in recovery is caused by
First, with a major volume
meet the gas sale oil is
vaporization cap water injection.
Secondly, the ability of the injected gas to vaporize the oil it contacts
lower reservoir pressure.
Finally,with the lower pressure due to a gas sale the oil becomes more viscous. It drains
more slowly and
With this MGS impacts GCWI, I would now like to address how
gas cap water injection would impact a major gas sale.
mechanisms.
available for injection is reduced in order to
by injected gas. This reduces
Gas Recov~ry Maintained with GCWI
30000
~ 25000
I~
v, 20000
.i
~ 15000
tlI
«I
C) 10000
E
c3 5000
o
2000
2010
2020
2030
2040
2050
October 30. 2001
MGS Relationship Exhibit 5
This chart is a plot of cumulative gas sales with time through 2050 as
forecasted by the BP full field model. It shows that ultimate gas recovery
win be essentially unchanged by gas cap water injection. The primary
reason for this is that similar abandonment pressures can be realized with
and without the project. This requires a large water free area from which
to produce the gas.
During the final stages of field life after the recoverable liquids have been
produced, the operating objective will be to maximize gas recovery. This
is accomplished by "blowing down" the reservoir pressure with the
remaining wells. These will likely be former oil wells that have been
recompleted the expanded and original gas cap. As you
know there are many candidate wens in the gravity drainage area.
Gas wen producing capacity is a strong function of both reservoir pressure
and water production. Without water a gas well can flow at economic
rates with relatively low reservoir pressure. However, is produced
along with the a much higher reservoir pressure is needed to sustain
production.
Consequently a large water free area must remain in the reservoir late in
field life. As shown on the next slide the water injected into the cap
remains highly localized.
Page 5
Water Free Area Remains for Slowdown
October 30. 2001
MGS Relationship Exhib.it 6
This chart shows the water and hydrocarbon saturation predicted by the BP
full field model in the high permeability Zone 3 at 2035. Blue represents
high water saturation; red represents the high gas saturation in the original
gas cap. The orange area is where gravity drainage and vaporization have
been responsible for oil recovery.
The water injected into the gas cap is readily apparent. water remains
relatively close to where it was injected because of its low mobility
compared to the gas it displaces. The blue area around the lower edge is the
aquifer.
Although not apparent in this chart, most ofthe red and orange
been penetrated by many wells on approximately 80 acre spacing. It
through these wells that the bulk of the late life gas reserves will be
produced.
Within the red and orange area the gas recovery mechanism will be simple
pressure depletion.
Because of this large water free area, gas cap water injection will not
materially impact the final reservoir pressure as shown on the next chart.
Similar Late Life Pressures
5000
1000
4000
¡¡¡
';- 3000"
:!!
:::¡
If¡
~ 2000
0...
o
2000
2010
2020
2030
Year
October 30, 2001
MGS Relationship Exhibit 7
This is the same chart shown earlier. Notice how close the pressures are
the end.
The next chart will illustrate how reservoir pressure depletion impacts gas
recovery.
Page 7
'Gas Recovery by Pressure Depletion
100%
90%
CI. 80%
¡:;
o 70%
"¡ft
. 60%
~ 50%
~
_ 40%
~
30%
:3
CJ 20%
10%
0%
Reservoir Pressure - psi
October 30, 2001
MGS Relationship Exhibit 8
This chart shows gas recovery by pressure depletion as a percent of
original gas in Gas recovery varies inversely with pressure. Notice
that recovery exceeds 80% when the pressure is reduced from the original
4400 psi to about 850 psi.
This is representative of what happens in the absence of water in the
original gas cap and throughout much of the gravity drainage area.
The next chart shows what happens when water is injected into the gas
cap.
PageS
Gas Recovery by Displacement
100%
90%
0. 80%
¡;
0 70%
'#-
. 60%
~ 50%
<I>
~ 40%
~ 30%
'"
«I 20%
CI
10%
0%
0
500 1000 1500 2000 2500 3000 3500 4000 4500 5000
Reservoir Pressure· psi
October 30, 2001
MGS Relationship Exhibit 9
The solid green lìne in this chart depicts gas recovery the case
has been injected into the gas cap after the reservoir pressure has dropped from
the original4400 psi to 3500 psi. For reference the pressure depletion
ITom the previous chart is also shown.
When water is injected it displaces most In this example,
saturation reduced from an original 90% PV to a trapped saturationof2~%
PV. Just as water is unable to displace the oil a waterflood, it is also
unable to displace all the in the gas cap.
The solid green curve shows that prior to injection, about
original gas volume had been recovered (expanded down
drainage area) by depletion.
When water is
removed from the
subsequently
again becomes
Notice that at a the water
invaded area is 90%. realize
depletion alone pressure has to be blown down to 500 psi.
Thus it can recovery ITom the gas cap where water is injected
may exceed that from the rest of the gas cap and gravity drainage area.
Now to summarize..
e
e
.
Interactions with Major Gas Sales
· GCWI yields higher pressure throughout remaining oil
producing life regardless of MGS rate & timing
· MGS slightly reduces GCWI incremental oil recovery
» Less gas cycled
" Lower vaporization efficiency
" Less Gravity Drainage
· Gas recovery is virtually unchanged
" Water free GD area is preserved for final blowdown
» Abandonment pressure only slightly increased
October 30, 2001
MGS Relationship Exhibit 10
.
In conclusion, gas cap water injection has been shown to yield higher
reservoir pressure with and without a major gas sale. Any water injected
serves to reduce total net voidage and thus maintain a higher pressure.
The gas sale does, however, reduce the incremental oil recovery due to
gas cap water injection for three reasons. First it reduces the volume of
vaporized oil because less gas is injected into the gas cap. Second, the
ability of the injected gas to vaporize residual oil is somewhat lower at
the lower reservoir pressure associated with the gas sale. Finally, gravity
drainage is reduced.
Gas recovery will be virtually unchanged by gas cap water injection.
This is because the large water free area that remains during late field life
enables effective pressure depletion with only a slightly higher final
pressure. Also it is likely the gas recovery from the water invaded area
will be somewhat increased.
This concludes my prepared testimony. Are there any questions?
Thank you. Next Jerry Brady will describe the surveillance program.
.
Page 10
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Prudhoe Bay GCWI
AOGCC Hearing
October 30, 2001
6. Surveillance
Jerry Brady
BPX (Alaska) Inc.
October 30, 2001
Surveillance Exhibit 1
·
Good morning. My name is Jerry Brady. I'd now like to be sworn and
qualified as an expert witness.
[Administration of Oath]
I am a Staff Engineer for BP Alaska currently working as a Production
Engineer on the Gas Cap Water Injection Project. I received a Bachelor of
Science Degree in Petroleum Engineering from Montana Tech in 1980. I
began my career with ARC a International in 1981 and moved to Alaska in
1984 for ARCa Alaska. Since then I have worked on a variety of
Production Engineering projects in Alaska. I began working on the GCWI
surveillance plan in 1993.
[Acceptance as Expert Witness]
I will now testify about surveillance for the Gas Cap Water Injection
Project.
·
Page 1
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Objectives of Surveillance Plan
· Injection Wells
- Injection Conformance
· Water Movement
- General Water Movement
- Leading Edge Detection
· Reservoir Pressure Monitoring
- Current Reporting Requirements
October 30, 2001
Surveillance Exhibit 2
·
Lets begin with the objectives of the GCWI surveillance plan. The
objectives are to monitor project performance and ensure that the injection
project is performing as expected. Critical elements of the plan are the
monitoring of injection well conformance, water movement and reservoir
pressure. Injection well monitoring ensures that the water injection is
contained in the desired reservoir interval. Water movement monitoring is
assuring that the water moves in the reservoir as expected. General
waterflood movement will be monitored using 4-D surface gravity and
downhole pulsed neutron logs in offset wells. The leading edge of the
waterflood will be detected primarily with pulsed neutron logs. Reservoir
pressure will be obtained from the current pressure reporting requirements
for the Prudhoe Bay oil pool.
·
Page 2
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GCWI Surveillance Plan
!.ojection Wells
· Surface Injection Measurements
- Temperature
- Pressure
- Rate
· Downhole Measurements
- Temperature, pressure & spinner surveys
· Injection profile analysis
· Hydraulics (correct surface calculations)
Pressure Falloffs
October 30,2001
Surveillance Exhibit 3
·
The first component of the GCWI surveillance plan is water injection well
monitoring. The injection wells will be monitored with surface measured
temperature, pressure and injection rate. These measurements will be
similar to other injection wells within the Prudhoe Bay pool. With these
measurements it is possible to monitor injection characteristics,
particularly changes in the injectivity indices. The injectivity indices
provide direct evidence of changes in well performance.
Downhole measurements will provide confirmation of the surface
measurements and will also help describe reservoir properties and
hydraulic performance. Downhole temperature logs will provide
verification of injection conformance and confirm that fracture height
growth is confined within the Ivishak. Downhole pressure measurements
will be used to determine tubular pressure drops and hydraulic
performance. Pressure falloff tests will be undertaken to determine
reservoir properties and wellbore skin.
·
Page 3
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GCWI Surveillance Plan
Water Movement
· General Waterflood Movement
- Pulsed Neutron Logging of wells
· Downhole zonal information
· Regional water movement
- 4-D surface gravity survey
· Regional water movement
October 30, 2001
Surveillance Exhibit 4
·
Water movement is monitored to make sure it remains in zone and it
moves as expected. Two techniques will be utilized to provide
information on the water movement. They are pulsed neutron logging in
offset wells and 4D surface gravity survey. The pulsed neutron logging
will provide the downhole information on which zones are being
flooded along with regional information on where the water is moving.
4D gravity will augment the pulsed neutron logging by providing
general water movement information.
·
Page 4
Area of Pulsed Neutron Logging
October 30,2001
Surveillance Exhibit 5
The next major component of the surveillance plan is the pulsed neutron
logging. This slide highlights the approximate area of interest for the
early time pulsed neutron logging program.
The light blue region surrounded by the heavy dashed line is the area of
primary interest. In the center of the blue region is a smaller dashed line
that shows the proposed location ofthe water injection wells. The wells
to be logged will be selected from the suite of wells shown as green dots.
These wells are primarily Lisburne producing wells, none of which have
known cement problems that would prevent confinement of injection to
the Ivishak.
Pulsed neutron logs, specifically the RST logs, were chosen because they
can be run in Lisburne wells completed with 2 7/8 inch tubing. Also, they
can be run in two modes to collect data for discerning a major change in
fluids (sigma & Carbon/Oxygen). The RSTs will help locate the leading
edge of the waterflood. It will also provide data in determining the
regional waterflood coverage.
4..D Gravit Station Grid
o.
o'M!lii¡~t
--===-
·t·
eN m
..
.......
iJU· .
...
_t4 ~
~-'~
...
--.'··1""""~-----r"""""~·-·"~·C~."·i,~nn,--,-_--_··--c1"".:C--·'--··'=-".~,.~.._m.'~~~r~.--r'.-~.
.tlœfI!).....~-.~ IìIIþ- 4IIOIiQO.... 1óOIII» 'IœfO/I '1fIIØO& 1flIII» 12ØIÞ ~ ~
EeoiI!Iø(j)
October 30.2001
Surveillance Exhibit 6
The 4D Gravity technique utilizes very sensitive surface gravity
measurements taken periodically. The method measures small changes in
gravity as the low density gas is replaced with the higher density water.
Baseline measurements will be taken prior to water injection. Subsequent
measurements will be made at discrete time intervals and compared to the
baseline measurements. An increase in the density of the fluids in the gas cap
indicates the presence of water.
This slide shows the area for gravity monitoring which covers the area of
expected water movement. The gravity stations are shown by red dots. The
center portion ofthe gravity grid is the most important region and it is setup
on a 2500 ft grid spacing. The center is also overlain with a few more closely
spaced gravity lines to improve the lateral sensitivity of the gravity
processing. Finally, the outer portion ofthe gravity grid is setup on a station
spacing of 5000 ft.
The 4D Gravity technique will enable us to map general water movement,
detennine an average watert100d front, and provide a means to perfonn a
mass balance ofthe injected water. The major limitations ofthe 4D gravity
technique is that it cannot detect horizontal or vertical flood fronts and
it cannot provide any downhole zonal infonnation.
Page 6
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GCWI Surveillance Plan
Summary
1. Injection wells will be monitored as other
water injection wells within the Prudhoe Bay
pool.
2. PNLs in existing wells will provide downhole
and regional data on the water movement.
3. 4-0 gravity will provide a general view of
water movement.
4. Reservoir pressure monitoring will be done
according to Prudhoe Bay pool rules.
October 30,2001
Surveillance Exhibit 7
·
In summary,
The major components of the GCWI surveillance plan are:
1) Injection wells will be monitored as other water injection wells
within the Prudhoe Bay pool.
2) PNLs in existing wells will provide downhole and regional data on
the water movement.
3) 4-D gravity will provide a general view of water movement.
4) Reservoir pressure monitoring will be done according to Prudhoe
Bay pool rules.
This concludes my prepared testimony. Are there any questions?
Thank you. Next Perry Richmond will provide a closing statement
summarizing requested changes to Conservation Order 341 C.
·
Page 7
e
e
.
Prudhoe Bay GCWI
AOGCC Hearing
October 30, 2001
7. Conclusion
Perry Richmond
BPX (Alaska) Inc.
October 30. 2001
Conclusion Exhibit I
.
The presenters have provided summary exhibits at the end of each
section of testimony. We hope the Commission finds this helpful when
deriving findings and conclusions for the Gas Cap Water Injection
project.
.
Page 1
.
.
.
e
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Conservation Order 341 C
Reauest:
Rule 12
paragraph (d) - revoke requirement to investigate and
report pressure mitigation options
Paragraph (c) - modify the pressure differential between
minimum miscibility pressure and reservoir pressure from
250psi to 100psi.
Consider:
Rule 11
add requirement to report on surveillance of GCWI
October 3D, 200l
Conclusion Exhibit 2
In closing, I would like to reference our letter submitted September 21, 2001 which contains our
requested pool rule changes to Conservation Order 341 C. I will summarize these changes here.
Paragraph (d) of Rule 12 provides that "The Operators are directed to continue to investigate
options to mitigate pressure decline and to provide an annual report to the Commission". With
the implementation of Gas Cap Water Injection, BP and the other owners should not be directed
to continue investigating options to mitigate pressure decline and provide an annual report to the
Commission on such activity. Therefore, we request that the Commission revoke paragraph (d)
of Rule 12.
We also request modification of Paragraph (c) in Rule 12 which currently provides that the
Operator maintain a pressure differential of at least 250 psi between the minimum miscibility
pressure of the miscible injectant and the prevailing reservoir pressure. Recognizing that GCWI
will mitigate pressure decline, a more appropriate pressure differential of 100 psi is requested
based on thermodynamic uncertainty only. This change will allow BP to better optimize both
the composition and volume of the miscible injectant.
Finally, the Commission may wish to consider modifying Rule 11, which describes the Prudhoe
Oil Pool surveillance report, to include the results of Gas Cap Water Injection surveillance.
This concludes our testimony on the Gas Cap Water Injection project. Thank You.
Page 2
GCWI testimony
.
.
Subject: GCWI testimony
Date: Thu, 01 Nov 2001 16:21:42 -0900
From: Jane Williamson <Jane_ Williamson@admin.state.ak.us>
Organization: Alaska Oil & Gas Conservation Commission
To: Daniel T Seamount JR <dan_seamount@admin.state.ak.us>,
Camille 0 Taylor <cammy _ taylor@admin.state.ak.us>,
John D Hartz <jack_hartz@admin.state.ak.us>,
Robert P Crandall <bob _ crandall@admin.state.ak.us>,
Robert E Mintz <robert mintz@law.state.ak.us>,
Stephen F Davies <steve _ davies@admin.state.ak.us>,
Thomas E Maunder <tom_maunder@admin.state.ak.us>,
Julie M Heusser <julie_heusser@admin.state.ak.us>,
Jody J Colombie <jody_colombie@admin.state.ak.us>
Perry brought by the CD containing their testimony, hard copies of the 8 1/2 x 11 slides we requested, a
desk size map showing the GCWI surveillance area. They also brought plots which show pressure over
time by area (23 separate areas of the field) with and without GCWI. In addition, Perry and Bahradt
hopefully will provide us with slices of the model (showing water saturations) which will help answer
questions concerning water movement after GCWI is shut-in and impact upon the gravity drainage area.
Jack and I will be discussing with Perry and Bahradt data and information which could better alleviate
concerns as to loss of gas cap liquids, particularly in the eastern area, and to fill in gaps, if any, on
information in that area. Additionally, we will discuss further with them the request to lower the MMP
to 100 psi above the prevailing pressure, to better understand the impact (may free up additional MI for
injection to other areas).
The individual exhibits and testimony are provided on the M drive. Steve Davies copied the pressure
plots to the M drive as well. The are in //MI/gcwi testimony/ The slides are in JPEG format, and I cant
directly read, as I don't have comparable software (might be a discussion item). I will later put in
powerpoint (not fully understanding why they couldn't use that but there was some legal reason).
However, if you also don't have the appropriate software, you can open power point, click insert, picture,
from file, then point to the M drive, gcwi testimony, and the particular slide you want to view.
Further update after tomorrow's meeting.
Jane
1 of 1
11/2/01 5:28 AM
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STATE OF ALASKA
OIL AND GAS CONSERVATION COMMISSION
GAS CAP WATER INJECTION PROJECT
NAME - AFFILIATION
October 30. 2001 9:00 am
ADDRESS/PHONE NUMBER
TESTIFY (Yes or No)
(PLEASE PRINT)
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STATE OF ALASKA
OIL AND GAS CONSERVATION COMMISSION
GAS CAP WATER INJECTION PROJECT
October 30. 20019:00 am
NAME - AFFILIATION
ADDRESSIPHONE NUMBER
TESTIFY (Yes or No)
(PLEASE PRINT\
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October 18,2001
To: Jack Hartz
Alaska Oil and Gas Conservation Commission
From: Frank Blaskovich
Blaskovich Services, Inc.
Re: GCWI Questions
I have reviewed the GCWI presentation materials provided at our 9/19 meeting with the
WIOs. This is a wealth of good information and has really helped me to understand the
reasoning behind starting a water injection project in the gas cap at Prudhoe Bay. The
Owners have done a great deal of work over the years and the model results seem
consistent in their support of the project. In fact, this has made my job somewhat harder.
I have tried to look beyond the WIO materials to find anything that hasn't been addressed
that might still be a factor in the decision to go ahead.
The following is a small set of questions that emerged from my investigations. I am
confident that the Owners will be able to quickly address these issues and that their
omission has either been an oversight or because they were not considered important.
As always, thanks for your patience and cooperation.
Very best regards,
Frank Blaskovich
Vice-President
Blaskovich Services, Inc.
e
e
GCWI Project Review Questions
The following is a series of questions derived from studying the 9/18/01 GCWI Project
Meeting notes and other documents. They are designed to clarify a few issues that
surfaced after the meeting and any remaining risk factors not fully discussed to date.
Wettability
During the MIINGL hearings in 1995, Arco's Dr. SimonI listed several reasons for
concern if water was inj ected in the gas cap. One of those was that the gas cap rock tends
to be oil-wet. Oil wettability at low water saturations, such as found in the Prudhoe Bay
gas cap, was also discussed by Jerauld and Rathmell2 in 1997. In an oil reservoir, it is
normally unadvisable to inject water if the rock is oil-wet, because of high residual
saturations. What would happen in the Prudhoe Bay gas cap with its relict oil saturation
likely to fill the smaller pores? Has the relict saturation in the cap been modeled as a
residual oil saturation to water displacement? Does some of the retrograde remain behind
the water front as part of the residual saturation? Has this issue been considered or
addressed as a risk factor?
Water Movement
After examining the model water saturation maps and profiles provided, it seems clear
that water continues to migrate downdip after water injection stops in 2020. I assume
that this is due to a combination of the natural gravity forces and the flow field created by
the continuing movement of fluids from the updip gas injectors to the downdip oil
producers. I understand your plans for surveillance and think they have merit. However,
what are your plans for controlling the water movement? It seems that the water will not
stay in place just by shutting in the water injection. Based on recent estimates3, Prudhoe
Bay could still be producing nearly 200,000 stbld by 2030 and I suspect most of it will be
from the gravity drainage area. Are these reserves at risk due to invasion? Do any model
results show this invasion of the oil column? Or do they indicate that the water gets to
the oil column so late that it doesn't appreciably impact oil recovery?
Trapped Gas Recovery
I understand that all trapped gas is now expected to be recoverable during blowdown.
Virtually all of this gas can be remobilized according to recent lab experiments. (A paper
by Ancell4 also supports this argument, although that process involved producing at high
water-cuts.) This appears to be part of your justification for claiming that no gas reserves
will be lost due to the GCWI project. Where will this gas be produced? Will GCWI
injectors be turned around or will this gas migrate over several miles to the NGI/WGI or
AGI injectors? Could it somehow move downdip to be produced from the oil column?
Well Locations
It would have been better to show more results from the final East Dock Water Injection
Case rather than the older Apex Water Injection Case. The latter has a different
relationship with the NGI/WGI gas injectors and appears to water out several of these
wells - based on materials presented on 9/18/01. High volume gas injection (~5 mmrb/d)
directly downdip from the apex water injection probably tends to slow down and stabilize
e
e
.
the movement of the water front. Water literally has to push past this gas somehow to get
further downdip. In the East Dock case, this seems much less likely to happen. Water
should have an easier time moving downdip and may even be pushed along by the
western and apex gas injection. I expected to see the water front being pushed from a
radial into a more elongated front (north to south) by the presence of the gas injection.
This could be a good thing because it may prevent the water from reaching the gravity
drainage area in the western half of the field. However, it may result in water reaching
the oil column in the eastern half of the field more quickly. Are there any simulation
results that show this?
Model Calibration and Gas Sweep Efficiency
While all of your model studies tend to show similar results, I am still concerned about
the accuracy of predictions based on very limited data. It appears that there is little if any
hard data to define the rock or fluid properties in the East Dock area at this time. Less is
known about it than any other part of the field and now we are planning to introduce an
entirely new, untested process as well. How confident are you that the gas liquids
(condensate and relict oil) have been efficiently swept in the eastern gas cap? Are there
any measurements that you have matched with the models to confirm good sweep
efficiency? From your model work, is it possible to see a simulator map (from 3D-View)
of current gas cap liquid saturations and an idea of current gas yields? Adding a few
"dummy gas producers" around the gas cap, running the PBU FFM for one timestep at
the end of history, and tabulating the results could generate these yields. My
understanding is that you have not taken this possibility into account ill your gas cap
liquids calculations.
1 MIINGL Hearing Minutes, May 1995, p. 645
2 Jerauld, G.R. and Rathmell, J.J.: "Wettability and Relative Permeability of
Prudhoe Bay: A Case Study of Mixed-Wet Reservoirs, SPERE, February 1997.
3 2000 Annual Report, Department of Natural Resources, Division of Oil and Gas.
4 Ancell, K.L. and Trousil, P.M.: "Remobilization of Natural Gas Trapped by
Encroaching Water", SPE 20753 presented at the 65th Annual SPE Technical
Conference and Exhibition, New Orleans, La., September 1990.
[Fwd: GCWI Questions]
e
--
Subject: [Fwd: GCWI Questions]
Date: Tue, 23 Oct 2001 17:33:47 -0800
From: Jack Hartz <jack_hartz@admin.state.ak.us>
Organization: AOGCC
To: Jody Colombie <jody _ colombie@admin.state.ak.us>
Jody,
Could you please print the email and attached document and add to the
record file for the BPX - Prudhoe Bay Oil Pool - Modification 341C.
Thanks,
Jack
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Subject: GCWI Questions
Date: Tue, 23 Oct 2001 17:08:37 -0800
From: Jack Hartz <jack_hartz@admin.state.ak.us>
Organization: AOGCC
To: "Richmond, Perry" <richmopl@bp.com>
Perry,
First - Frank Blaskovich forwarded several questions to us based on the
review of 9/18/01. I have reviewed the questions and think they are
appropriate for us to consider in the context of the project. He has
taken care to set the question is a context that helps explain his
thinking and what he is after. We'd appreciate if you can address the
questions during the course of the hearing.
Let me know if there are any problems.
Second - I mentioned to the Commission that testimony may not be ready
to pre file before the hearing. In that case, you'd be expected to
present the testimony so the Commissioners and all could hear it and
formulate questions. If the testimony is timely pre filed, then a
summary is ok. The pre filing has to give the Commission and staff
enough time to review the testimony and consider it before the hearing.
Jack Hartz
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Name: GCWI Questions.doc
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Encoding: base64
Jack Hartz <iack hartz(ll),admin.state.ak.us>
Sr. Petroleum Reservoir Engineer
Alaska Oil & Gas Conservation Commission
lof2
10/24/01 11 :40 AM
*2
STATE OF ALASKA
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e
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Notice of Public Hearing
STATE OF ALASKA
Alaska Oil and Gas Conservation Commission
Re: Prudhoe Oil Pool- Modification to Pool Rules - Conservation Order 341 C
By letter dated September 21, 2001, BP Exploration (Alaska), Inc. on behalf of
the working interest owners of the Initial Participating Areas of the Prudhoe Bay Unit has
applied for a modification of certain Rules of Conservation Order 341 C in conjunction
with a proposed project named the Gas Cap Water Injection Project.
A person may submit written comments regarding this application no later than
4:30 pm on October 30,2001 to the Alaska Oil and Gas Conservation Commission at 333
West 7th Avenue, Suite 100, 'Anchorage, Alaska 99501. In addition, the Commission has
tentatively set a public hearing on October 30, 2001 at 9:00 am at the Alaska Oil and Gas
Conservation Commission at 333 West ih Avenue, Suite 100, Anchorage, Alaska 99501.
A person may request that the tentatively scheduled hearing be held by filing a written
request with the Commission no later than 4:30 pm on October 15, 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 public
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 a public hearing, please contact Jody Colombie at 793-1221
before October 23,2001.
(ß~ [l¿¿~ ~
Cammy dechsli Taylor
Chair
Published September 29,200 I
ADN AO# 02214009
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STATE OF ALASKA
Alaska Oil and Gas
Conservalion Commission
Re:Prodhoe Oil Pool -
Modification 10 Pool
::"1~lè Conser\lQllon Or"
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A "ers()nm(\'.~requesl
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~1:Iedu.1!td ~i'!9:~ fteld
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quest witlt IlteCommis-
sion nø ia~ fflcÎII4:30 pm
0",qc~r~5.290J.
If a requesltar a hearing
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To learn if tlte Cammis:
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CTR
POBOX 87703
CHICAGO, IL 60680-0703
ALFRED JAMES III
107 N MARKET STE 1000
WICHITA, KS 67202-1811
10GCC,
POBOX 53127
OKLAHOMA CITY, OK 73152-3127
GAFFNEY, CLINE & ASSOC., INC.,
LIBRARY
16775 ADDISON RD, STE 400
ADDISON, TX 75001
DEGOL YER & MACNAUGHTON,
MIDCONTINENT DIVISION
ONE ENERGY SQ, STE 400
4925 GREENVILLE AVE
DALLAS, TX 75206-4083
SHELL WESTERN E&P INC,
G.S. NADY
POBOX 576
HOUSTON, TX 77001-0574
RAY TYSON
2016 MAIN #1415
HOUSTON, TX 77002-8844
CHEVRON,
PAUL WALKER
1301 MCKINNEY RM 1750
HOUSTON. TX 77010
MURPHY EXPLORATION &
PRODUCTION CO.,
BOB SAWYER
550 WESTLAKE PARK BLVD STE 1000
HOUSTON, TX 77079
UNOCAL, REVENUE ACCOUNTING
PO BOX 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
TESORO PETR CORP,
LOIS DOWNS
300 CONCORD PLAZA DRIVE
SAN ANTONIO, TX 78216-6999
ROBERT G GRAVELY
7681 S KIT CARSON DR
LITTLETON, CO 80122
US GEOLOGICAL SURVEY, LIBRARY
BOX 25046 MS 914
DENVER, CO 80225-0046
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OIL & GAS JOURNAL,
BOB WILLIAMS
1700 W LOOP SOUTH STE 1000
HOUSTON, TX 77027
MARK ALEXANDER
7502 ALCOMITA
HOUSTON, TX 77083
EXXON EXPLORATION CO.,
T E ALFORD
POBOX 4778
HOUSTON, TX 77210-4778
PETR INFO,
DAVID PHILLIPS
POBOX 1702
HOUSTON, TX 77251-1702
EXXON MOBIL PRODUCTION
COMPANY,
J W KIKER ROOM 2086
POBOX 2180
HOUSTON, TX 77252-2180
CHEVRON CHEM CO, LIBRARY & INFO
CTR
POBOX 2100
HOUSTON, TX 77252-9987
TEXACO INC,
R Ewing Clemons
POBOX 430
BELLAIRE, TX 77402-0430
INTL OIL SCOUTS,
MASON MAP SERV INC
POBOX 338
AUSTIN, TX 78767
DIANE SUCHOMEL
105070 W MAPLEWOOD DR
LITTLETON, CO 80127
C & R INDUSTRIES, INC."
KURT SAL TSGAVER
7500 W MISSISSIPPI AVE STE C4
LAKEWOOD, CO 80226-4541
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PETRAL CONSULTING CO,
DANIEL L LIPPE
9800 RICHMOND STE 505
HOUSTON, TX 77042
MARATHON OIL CO,
GEORGE ROTHSCHILD JR RM 2537
POBOX 4813
HOUSTON, TX 77210
EXXON EXPLOR CO,
LAND/REGULATORY AFFAIRS RM 301
POBOX 4778
HOUSTON, TX 77210-4778
PHILLIPS PETROLEUM COMPANY,
W ALLEN HUCKABAY
PO BOX 1967
HOUSTON, TX 77251-1967
EXXONMOBIL PRODUCTION
COMPANY,
GARY M ROBERTS RM 3039
POBOX 2180
HOUSTON, TX 77252-2180
MARATHON,
Ms. Norma L. Calvert
POBOX 3128, Ste 3915
HOUSTON, TX 77253-3128
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
JERRY HODGDEN GEOL
408 18TH ST
GOLDEN, CO 80401
NRG ASSOC,
RICHARD NEHRING
POBOX 1655
COLORADO SPRINGS, CO 80901-
1655
TAHOMA RESOURCES,
GARY PLAYER
1671 WEST 546 S
CEDER CITY, UT 84720
LA PUBLIC LIBRARY, SERIALS DIV
630 W 5TH ST
LOS ANGELES, CA 90071
ORO NEGRO, INC.,
9321 MELVIN AVE
NORTHRIDGE, CA 91324-2410
SHIELDS LIBRARY, GOVT DOCS DEPT
UNIV OF CALIF
DAVIS, CA 95616
US EPA REGION 10,
THOR CUTLER OW-137
1200 SIXTH AVE
SEATTLE, WA 98101
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
DEPT OF REVENUE,
CHUCK LOGSTON
550 W 7TH AVE, SUITE 500
ANCHORAGE, AK 99501
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RUBICON PETROLEUM, LLC,
BRUCE I CLARDY
SIX PINE ROAD
COLORADO SPRINGS, CO 80906
US GEOLOGICAL SURVEY, LIBRARY
2255 N GEMINI DR
FLAGSTAFF, AZ 86001-1698
BABSON & SHEPPARD,
JOHN F BERGQUIST
POBOX 8279 VIKING STN
LONG BEACH, CA 90808-0279
TEXACO INC, Portfolio Team Manager
R W HILL
POBOX 5197x
Bakersfield, CA 93388
H L WANGENHEIM
5430 SAWMILL RD SP 11
PARADISE, CA 95969-5969
MARPLES BUSINESS NEWSLETTER,
MICHAEL J PARKS
117 W MERCER ST STE 200
SEATTLE, WA 98119-3960
FAIRWEATHER E&P SERV INC,
JESSE MOHRBACHER
7151ST #4
ANCHORAGE, AK 99501
TRUSTEES FOR ALASKA,
1026 W. 4th Ave, Ste 201
ANCHORAGE, AK 99501
DEPT OF REVENUE,
DAN DICKINSON, DIRECTOR
550 W 7TH AVE, SUITE 500
ANCHORAGE, AK 99501
DEPT OF ENVIRON CONSERVATION,
DIV OF ENVIRONMENTAL HEALTH
JANICE ADAIR
555 CORDOVA STREET
ANCHORAGE, AK 99501
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JOHN A LEVORSEN
200 N 3RD ST #1202
BOISE,ID 83702
MUNGER OIL INFOR SERV INC,
POBOX 45738
LOS ANGELES, CA 90045-0738
ANTONIO MADRID
POBOX 94625
PASADENA, CA 91109
US GEOLOGICAL SURVEY,
KEN BIRD
345 MIDDLEFIELD RD MS 999
MENLO PARK, CA 94025
ECONOMIC INSIGHT INC,
SAM VAN VACTOR
PO BOX 683
PORTLAND, OR 97207
DEPT OF REVENUE,
BEVERLY MARQUART
550 W 7TH A V STE 570
ANCHORAGE, AK 99501
GUESS & RUDD,
GEORGE LYLE
510 L ST, STE 700
ANCHORAGE, AK 99501
DUSTY RHODES
229 WHITNEY RD
ANCHORAGE, AK 99501
FOREST OIL,
JIM ARLINGTON
310 K STREET STE 700
ANCHORAGE, AK 99501
YUKON PACIFIC CORP,
JOHN HORN VICE CHM
1049 W 5TH AV
ANCHORAGE, AK 99501-1930
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
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
OIL & GAS
WILLIAM VAN DYKE
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
ANADARKO,
MARK HANLEY
3201 C STREET STE 603
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
TRADING BAY ENERGY CORP,
PAUL CRAIG
5432 NORTHERN LIGHTS BLVD
ANCHORAGE, AK 99508
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ALASKA DEPT OF LAW,
ROBERT E MINTZ ASST ATTY 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
DEPT OF NATURAL RESOURCES, DIV
OF OIL & GAS
BRUCE WEBB
550 W 7TH AVE, SUITE 800
ANCHORAGE, AK 99501-3560
BAKER OIL TOOLS, ALASKA AREA
MGR
4710 BUS PK BLVD STE 36
ANCHORAGE, AK 99503
N-I TUBULARS INC,
3301 C Street Ste 209
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
THOMAS R MARSHALL JR
1569 BIRCHWOOD ST
ANCHORAGE, AK 99508
UOA/ ANCHORAGE, INST OF SOCIAL
& ECON RESEARCH
TERESA HULL
3211 PROVIDENCE DR
ANCHORAGE, AK 99508
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GAFO,GREENPEACE
PAMELA MILLER
125 CHRISTENSEN DR. #2
ANCHORAGE, AK 99501-2101
AK JOURNAL OF COMMERCE, OIL &
INDUSTRY NEWS
ROSE RAGSDALE
4220 B Street Ste #210
ANCHORAGE, AK 99501-3560
DEPT OF NATURAL RESOURCES, DIV
OF OIL & GAS
JIM STOUFFER
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
HDRALASKA INC,
MARK DALTON
2525 C ST STE 305
ANCHORAGE, AK 99503
ALASKA OIL & GAS ASSOC,
JUDY BRADY
121 W FIREWEED LN 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
VECO ALASKA INC.,
CHUCK O'DONNELL
949 EAST 36TH AVENUE
ANCHORAGE, AK 99508
US BLM AK DIST OFC, GEOLOGIST
ARTHUR BANET
949 EAST 36TH AVE STE 308
ANCHORAGE, AK 99508
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, RESOURCE
EVAL
JIM SCHERR
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
GERALD GANOPOLE CONSULT GEOL
2536 ARLINGTON
ANCHORAGE, AK 99517-1303
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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
US MIN MGMT SERV,
FRANK MILLER
949 E 36TH A V STE 603
ANCHORAGE, AK 99508-4363
CIRI, LAND DEPT
POBOX 93330
ANCHORAGE, AK 99509-3330
PHILLIPS ALASKA,
JOANN GRUBER ATO 712
POBOX 100360
ANCHORAGE, AK 99510-0360
PHILLIPS ALASKA,
MARK MAJOR ATO 1968
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 A V #13
ANCHORAGE, AK 99513-7599
JWL ENGINEERING,
JEFF LIPSCOMB
9921 MAIN TREE DR.
ANCHORAGE, AK 99516-6510
DAVID CUSATO
600 W 76TH A V #508
ANCHORAGE, AK 99518
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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, LIBRARY
949 E 36TH A V RM 603
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, LEGAL DEPT
MARK P WORCESTER
POBOX 100360
ANCHORAGE, AK 99510-0360
PHILLIPS ALASKA, LAND DEPT
JAMES WINEGARNER
POBOX 10036
ANCHORAGE, AK 99510-0360
AL YESKA PIPELINE SERV CO,
PERRY A MARKLEY
1835 SBRAGAW - MS 575
ANCHORAGE, AK 99512
ANCHORAGE DAILY NEWS,
EDITORIAL PG EDTR
MICHAEL CAREY
POBOX 149001
ANCHORAGE, AK 99514
NORTHERN CONSULTING GROUP,
ROBERT BRITCH, P.E.
2454 TELEQUANA DR.
ANCHORAGE, AK 99517
ASRC,
CONRAD BAGNE
301 ARCTIC SLOPE AV STE 300
ANCHORAGE, AK 99518
ARMAND SPIELMAN
651 HILANDER CIRCLE
ANCHORAGE, AK 99518
TESORO ALASKA COMPANY,
PO BOX 196272
ANCHORAGE, AK 99519
MARATHON OIL CO, LAND
BROCK RIDDLE
POBOX 196168
ANCHORAGE, AK 99519-6168
UNOCAL,
KEVIN TABLER
POBOX 196247
ANCHORAGE, AK 99519-6247
BP EXPLORATION (ALASKA) INC, INFO
RESOURCE CTR MB 3-2
POBOX 196612
ANCHORAGE, AK 99519-6612
BP EXPLORATION (ALASKA) INC,
MR. DAVIS, ESQ
POBOX 196612 MB 13-5
ANCHORAGE, AK 99519-6612
D A PLATT & ASSOC,
9852 LITTLE DIOMEDE CIR
EAGLE RIVER, AK 99577
DEPT OF NATURAL RESOURCES,
DGGS
JOHN REEDER
POBOX 772805
EAGLE RIVER, AK 99577-2805
RON DOLCHOK
POBOX 83
KENAI, AK 99611
NANCY LORD
PO BOX 558
HOMER, AK 99623
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HALLIBURTON ENERGY SERV,
MARK WEDMAN
6900 ARCTIC BLVD
ANCHORAGE, AK 99518-2146
JACK 0 HAKKILA
POBOX 190083
ANCHORAGE, AK 99519-0083
MARATHON OIL CO, OPERATIONS
SUPT
W.C. BARRON
POBOX 196168
ANCHORAGE, AK 99519-6168
EXXONMOBIL 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
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
COOK INLET KEEPER,
BOB SHAVELSON
PO BOX 3269
HOMER, AK 99603
DOCUMENT SERVICE CO,
JOHN PARKER
POBOX 1468
KENAI,AK 99611-1468
PENNY VADLA
POBOX 467
NINILCHIK, AK 99639
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OPST AD & ASSOC,
ERIK A OPSTAD PROF GEOL
POBOX 190754
ANCHORAGE, AK 99519
ENSTAR NATURAL GAS CO,
PRESIDENT
TONY IZZO
POBOX 190288
ANCHORAGE, AK 99519-0288
UNOCAL,
POBOX 196247
ANCHORAGE, AK 99519-6247
BP EXPLORATION (ALASKA) INC,
PETE ZSELECZKY LAND MGR
POBOX 196612
ANCHORAGE, AK 99519-6612
BP EXPLORATION (ALASKA) INC,
SUE MILLER
POBOX 196612 M/S LR2-3
ANCHORAGE, AK 99519-6612
PINNACLE,
STEVE TYLER
20231 REVERE CIRCLE
EAGLE RIVER, AK 99577
JAMES RODERICK
PO BOX 770471
EAGLE RIVER, AK 99577-0471
PHILLIPS PETROLEUM CO, ALASKA
OPERATIONS MANAGER
J W KONST
P 0 DRAWER 66
KENAI, AK 99611
KENAI PENINSULA BOROUGH,
ECONOMIC DEVEL DISTR
STAN STEADMAN
POBOX 3029
KENAI, AK 99611-3029
BELOWICH,
MICHAEL A BELOWICH
1125 SNOW HILL AVE
WASILLA, AK 99654-5751
JAMES GIBBS
POBOX 1597
SOLDOTNA, AK 99669
AL YESKA PIPELINE SERVICE CO,
VALDEZ CORP AFFAIRS
SANDY MCCLINTOCK
POBOX 300 MS/701
VALDEZ, AK 99686
NICK STEPOVICH
543 2ND AVE
FAIRBANKS, AK 99701
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
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PACE,
SHEILA DICKSON
PO BOX2018
SOLDOTNA, AK 99669
VALDEZ PIONEER,
POBOX 367
VALDEZ, AK 99686
UNIV OF ALASKA FAIRBANKS, PETR
DEVEL LAB
DR V A KAMATH
427 DUCKERING
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 BOX416
ESTER, AK 99725
SENATOR LOREN LEMAN
STATE CAPITOL RM 113
JUNEAU, AK 99801-1182
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KENAI NATL WILDLIFE REFUGE,
REFUGE MGR
POBOX 2139
SOLDOTNA, AK 99669-2139
VALDEZ VANGUARD, EDITOR
POBOX 98
VALDEZ, AK 99686-0098
COOK AND HAUGEBERG,
JAMES DIERINGER, JR.
119 NORTH CUSHMAN, STE 300
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
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BP Exploration (Alaska) Inc.
900 East Benson Boulevard
P.O. Box 196612
Anchorage, Alaska 99519-6612
(907) 561·5111
September 21, 2001
Commissioners
Alaska Oil and Gas Conservation Commission
333 W. 7th Ave. Suite 100
Anchorage, Alaska 99501
Re: Prudhoe Oil Pool- Gas Cap Water Injection Project
Dear Commission~rs,
The Working Interest Owners of the Initial Participating Areas (IP A) of the Prudhoe Bay
Unit have studied options to mitigate pressure decline in the Prudhoe Oil Pool. The
progress of these studies has been reported annually to the Commission as provided in
Rule 12 of Conservation Order 341C. As a culmination of these studies, the IPA Owners
recently sanctioned the Gas Cap Water Injection (GCWI) project. This project represents
a new element in the depletion strategy of the Prudhoe Oil Pool and should mitigate
reservoir pressure decline and improve recovery from the Prudhoe Oil Pool. Facility
construction is planned for this winter, followed by start-up of injection in 2Q 2002.
BP Exploration (Alaska) Inc. (BPXA), as Operator of the Prudhoe Bay Unit, has
previously provided information to the Commission on the GCWI project on an informal
basis, and is proceeding with technical reviews for your staff. From these interactions and
correspondence received from the Commission, we understand that the Commission
intends to publish notice regarding the GCWI project (and schedule a public hearing). In
addition, although we believe that GCWI operations will be consistent with Area
Injection Order 4C, some modifications to the pool rules for the Prudhoe Oil Pool
(Conservation Order 341C) are appropriate.
The first section of this letter provides a description of the GCWI project. This is
followed by a section that describes certain specific changes to Conservation Order 341 C
that would be appropriate in conjunction with the GCWI project. Please consider this
letter as an application for revisions to the pool rules to the extent requested herein.
.... .
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Gas Cap Water Iniection Proiect
Scope of Operations
The Gas Cap Water Injection project involves installation of 5 to 7 new injection wells at
the East Dock pad. The proposed location of these wells is shown in Attachment 1. The
wells are planned to begin injection of seawater in the gas cap of the Ivishak formation in
2Q 2002. The seawater injection rates for these wells are expected to ramp up to
approximately 650,000 BWPD. A pipeline to supply the water will be built from the
seawater injection line at Flow Station 2 to the East Dock pad as shown in Attachment 2.
Injection Wells
The gas cap water injection wells will differ from typical injection wells in that the tubing
will be larger (7-5/8") to accommodate the high volume of water to be injected. The
tubing will be plastic coated to help minimize the friction losses and maximize rate. A
representative well completion diagram is shown in Attachment 3. Average design
wellhead pressure for these new injection wells is approximately 2700 psi. Maximum
injection pressure is expected to be approximately 3100 psi.
Surveillance
Surveillance will playa key role in monitoring the performance of the injection wells,
movement of injected water in the reservoir, and the overall effectiveness of the project.
Plans include monitoring surface injection rate, temperature, and pressure on each of the
injection wells. Temperature logs and pressure surveys will be run on the injectors as
well. Offset wells accessing the Lisburne formation will be used to monitor movement of
the water by means of cased hole logs, such as the Reservoir Saturation Tool. 4D Gravity
surveys also are planned to periodically monitor the overall movement of injected water.
Recovery Benefits
The objective of the GCWI project is to mitigate pressure decline and enhance production
performance. Increased reservoir pressure should affect recovery in several ways. First,
pressure support increases reservoir energy, which improves well inflow performance.
Second, pressure maintenance improves oil fluid properties by decreasing viscosity and
reducing shrinkage. Third, pressure support allows dilution of MI (higher MMP)
increasing MI supply and improving EOR recovery. Finally, vaporization of residual oil
by lean injected gas is more efficient at higher pressure. The expected incremental
increase in hydrocarbon liquid recovery for this project is estimated to be 150 - 200
million barrels.
..
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Modifications to Conservation Order 341 C
Paragraph (d) of Rule 12 of Conservation Order 341C provides that "The operators are
directed to continue investigating options to mitigate pressure decline and to provide an
annual progress report to the Commission." With implementation of GCWI, BPXA and
the other owners should not be directed to continue investigating options to mitigate
pressure decline and provide an annual report to the Commission on such activity.
Therefore, we request that the Commission revoke paragraph (d) ofRu1e 12.
We also request modification of paragraph (c) in Rule 12. Paragraph (c) currently
provides:
( c) The operator will maintain a pressure differential of at least 250 psi between
the minimum miscibility pressure (MMP) of the MI and the prevailing
reservoir pressure at the time of injection. This differential is based on a
projected prevailing reservoir pressure decline of no more than 30 psi/year
over the life of the project. (Source: C.O. 290, Rule 4)
We request (c) be modified as follows:
( c) The operator will maintain a pressure differential of at least 100 psi between
the minimum miscibility pressure (MMP) of the MI and the prevailing
reservoir pressure at the time of injection.
The 250 psi pressure differential is based on the existence of a prevailing reservoir
pressure decline of approximately 30 psi/year and thermodynamic uncertainty.
Recognizing that GCWI should mitigate pressure decline, a more appropriate pressure
differential of 100 psi is requested based on thermodynamic uncertainty only. This
change will allow BPXA to better optimize both the composition and volume of miscible
injectant.
The Commission also may wish to consider modifying Rule 11, which describes the
Prudhoe Oil Pool surveillance report, which is submitted annually to the Commission. To
accommodate surveillance activity associated with the GCWI project, the Commission
could add the following requirement:
6. Results of surveillance of injected water volumes into the gas cap of the pool.
We believe that the injection operations associated with the GCWI project can be carried
out consistent with provisions of Area Injection Order No. 4C. Therefore, no change in
the Order is requested by BPXA .
<.
e
e
We hope that this information provides the Commission with enough information to
publish the notice and schedule a public hearing. If this is not the case, please contact me
at your earliest convenience.
We look forward to working with the Commission in moving forward with the GCWI
Project. If you have any questions, please give me a call at (907) 345-6811 or email me at
RichmoPL@BP.com.
Respectfully,
æ/!;/
p~hmond
Manager, EastJWest Group
Greater Prudhoe Bay
BP Exploration (Alaska) Inc.
Enclosures (3)
..
.
1
Attachment 2
Prudhoe
Bay
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Date
8-29-00
3290
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4100
44I!4
9803
5051
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5$86
6415
660$
6$01
7<131
7674
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8267
$267
$267
$267
$26$
8270
8297
$56$
$584
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Attachment 3
Proposed Generic Design
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