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Conservation Order 114
1.
2.
3.
4.
5.
May 12, 1973
May 19, 1972
June 14, 1984
December 17, 1984
September 9, 1985
Transcript
Marathon Oil Company submittal of information
Amoco's request for a Flare Exception (114.1)
Amoco's request for a Flare Limit Exception (114.2)
Amoco's request for a Flare Limit Exception (114.3)
Conservation Order 114
JIgL1
I . I nve n-¡-ory
2. C. O. fll14
)
))
I~
I NV[r"JTOF~Y
Cm,JSEFN AT I ON Of<!J[f~ // 114
(establishes the size of a
safety flare for Cook Inlet
Platforms and shore faci lities)
3. Affidavit of publication
Marathon Oi I Co.
4. Notice of publication
5. Exhibits I
6. Exhibit 2
7. Exhibit 3
8. Exhibit 4
Union Oi I Co.
9. Exhibit A
10. Exhibit ^
(Exhibit 2 of C. O. #103 - A) Marathon -
Union Gas Gathering system
Dolly Varden Platform
Gas Diagram
Dolly Varden Platform
Trading Bay Production Faci lity
Grayling Platform
Monapod Platform
II.
Exhibit I
Hob i I 0 i I Corporat ion
Granite Point Gas Faci I ity
Granite Point Field - AMOCO Production
12. AM OCO Exhibit Gas Flow Schematic - Platform Anna (G.P.)
13. A~10CO Exhibit 2 Gas Flow Schematic - Platform Bruce (G.P.)
M.G.S. Point Field - AMOCO Production Co.
14. Ar,10CO Exhibit 3 Gas Flow Schematic - Platform Sa ke r (MGS)
15. Ar-.10CO Exhibit <1 Gas Flow Schematic - Platform Dellon Ot1G S )
M. G. S. Field She II
16.
Exhibit I
Simplified flow diagram
:r .¡.~ PV I
)
))
I ìN [NTOr\y
C. o. /'114
Page 2
ARCO
17. Exhibit Locat ion IV1ap
18. Exhibit 2 King Salman Platform schematic diagram
19. [xh i bit 3 King Salmon Platform gas balance
20. Exhibit 4 King Salmon Platform burner tip
Trading Bay Field, Atlantic Richfield Co. , Platform5 A and
Spark platforfl'l
21 .
) 22.
23.
24.
E xh i bit
Exhibit 2
Exhibit 3
Exh i bit 4
Location Map
Platform "AT! Schematic diagram
Platform Spark
Platforms "AI! & Spark Gas Balance
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STATE OF ALASKA
OEPARTtl.~ENT OF NATURAL RESOURCES
DIVISION OF OIL AND GAS
Alaska Oi I and Gas Conservation Committee
3001 Porcupine Drive
Anchorage, Alaska 99504
Re: THE MOTION OF THE ALASKA OIL
AND GAS CONSERVAT ION CQt\1M I TTEE
to hold a hearing to determine
the amount of gas necessary for
safety flares on production
platforms.
Conservation Order No. 114
Granite Point Field
Trading Bay Field
McArthur River Field
Middle Ground Shoal Field
June 9, 1972
IT APPEARING THAT:
I. The Alaska Oi I and Gas Conservation Committee published a notice of
pub I ic hearing in the Anchorage Dai Iy News on Apri I 13, 1972, pursuant
to Title I I, Alaska Administrative Code, Section 2009.
2. A public hearing was held on May 12, 1972 in the City Counci I Chambers
of the Z. J. Loussac Library, 5th Avenue and F Street, Anchorage, Alaska, at
which time operators of the production platforms in the referenced fields
were heard.
3. Conservation Order Nos. 102-B, I03-A, I04-A, and I05-A restrict the
amount of casinghead gas which may be flared from the oi I pools in the
referenced fie I ds to the amount necessary for adequate safety f I ares,
effective at 7:00 A.M., ADST, October 15, 1972, or such later date as
provided in these orders.
FINDINGS:
I. Each of the thirteen oi I-producing platforms in the referenced fields
produces different volumes of oi I, with varying gas-oi I ratios, and necessari Iy
has different oi I and gas production and handling faci lities. Gas flare
booms and burner tips vary in design and number, depending on volumes of
oi I and gas produced, platform and equipment design and other factors.
2. Concentration of producing we I Is and equipment on platforms, necessari Iy
enclosed because of weather conditions, requires adequate safety flares to
avoid the risk of explosion and fire from hydrocarbon accumulation.
3. A safety flare is necessary at onshore production faci lities to avoid
the risk of explosion and fire from hydrocarbon accumulation.
4. The minimum amount of gas necessary to keep a flare burning under
operating conditions has not been determined, but operators estimated
this amount based on limited experience.
T+ # w.- 2..-
,....
~
Conservation Order No. / /4
Page 2
June 9, 1972
CONCLUSIONS:
I. Safety of personnel and property is the paramount consideration; therefore
safety flares on each platform should be of an adequate size to handle both
routine and unexpected gas and liquid volumes.
2. Continued survei I lance of casinghead gas uti lization and flared volumes
from each platform and onshore faci lity is necessary.
3. Pending evidence to the contrary, the operator of each platform and
onshore p I atforrn shou I d be a I lowed to f I are the vo I ume of gas he test if i ed
as being necessary for safety, and gas so flared should not constitute
ItJaste.
4. The Committee should require reports of casinghead gas uti lization by
equipment on each platform and onshore faci lity as wel I as flared volumes,
at frequent intervals.
5. The Committee should retain administrative authority to order an
increase or decrease in the vo I ume of gas a I lowed to be flared for safety
from each platform and onshore faci lity, as additional experience may
indicate.
NOW, THEREFORE, IT IS ORDERED THAT:
I. For each calendar month, the dai Iy average volume of casinghead gas
perm i tted to ma i nta in a safety f I are or f I ares on Mobil platform in the
Granite Point Field shal I be 1000 MCF per day.
2. For each calendar month, the dai Iy average volume of casinghead gas
permitted to maintain a safety flare or flares on Anna platform in the
Granite Point Field shal I be 700 MCF per day.
3. For each calendar month, the dai Iy average volume of casinghead gas
permitted to maintain a safety flare or flares on Bruce platform in the
Granite Point Field shal I be 700 MCF per day.
4. For each calendar month, the dai Iy average volume of casinghead gas
permitted to maintain a safety flare or flares on Monopod platform in
the Trading Bay Field shal I be 2000 MCF per day.
5. For each calendar month, the dai Iy average volume of casinghead gas
permitted to maintain a safety flare or flares on !fAn platform in the
Trading Bay Field shal I be 400 MCF per day.
ó. For each calendar month, the dai Iy average volume of casinghead gas
permitted to maintain a safety flare or flares on Spark platform in the
Trading Bay Field shal I be 600 MCF per day.
"--~
.~
Conservation Order No. 114
Page 3
June 9, 1972
7. For each calendar month, the dai Iy average volume of casinghead gas
permitted to maintain a safety flare or flares on Grayling platform in
the McArthur River Field shal I be 2000 MCF per day.
8. For each calendar month, the dai Iy average volume of casinghead gas
permitted to maintain a safety flare or flares on King Salmon platform
in the McArthur River Field shal I be 800 MCF per day.
9. For each calendar month, the dai Iy average volume of casinghead gas
permitted to maintain a safety flare or flares on Dolly Varden platform
in the McArthur River Field shal I be 1000 MCF per day.
10. For each calendar month, the dai Iy average volume of casinghead gas
permitted to maintain a safety flare or flares on Baker platform in the
Middle Ground Shoal Field shal I be 700 MCF per day.
I I. For each calendar month, the dai Iy average volume of casinghead gas
permitted to maintain a safety flare or flares on Di I Ion platform in the
Middle Ground Shoal Field shal I be 700 MCF per day.
12. For each calendar month, the dai Iy average volume of casinghead gas
permitted to maintain a safety flare or flares on HAl! platform in the
Mi dd I e Ground Shoa I Fi e I d sha II be 700 MCF per day.
13. For each calendar month, the dai Iy average volume of casinghead gas
pe rm i tted to ma i nta in a safety f I are or f I ares on IrCn platform in the
Middle Ground Shoal Field shal I be 700 MCF per day.
14. For each ca~endar month, the dai Iy average volume of casinghead gas
permitted to maintain a safety flare or flares at the West Foreland onshore
production faci lities shal I be 300 MCF per day.
15. For each calendar month, the dai Iy average volume of casinghead gas
permitted to maintain a safety flare or flares at the Granite Point
onshore production faci lities shal I be 100 MCF per day.
16. For each calendar month, the dai Iy average volume of casinghead gas
permitted to maintain a safety flare or flares at the East Foreland onshore
production faci I ities operated by Shel I shal I be 100 MCF per day.
17. For each calendar month, the dai Iy average volume of casinghead gas
permitted to maintain a safety flare or flares at the East Foreland
onshore production faci lities operated by Amoco shal I be 100 MCF oer day.
18. ~·1onth Iy r'eports of gas production, on Form G-7 or 10-407, !!Producers
Report of Gas Producti on ," sha II show va I urnes of gas disposed of in
emer'gencies under the heading "Other Disposition (Detail)."
".....
~
Conservation Order No. 1/4
Page 4
June 9, 1972
19. Fol lowing ten (10) days notice to the operator of any platform or
onshore rroduction faci lity in or serving the referenced fields, the
Comm i ttee, may decrease or increase the vo I ume of gas a I lowed to be f la red
for safety.
DONE at Anchorage, Alaska and dated June 9, 1972.
d¡( 1ft -4/t /
Thomas R. Marshal I, Jr., Executive Secretary
Alaska Oil and Gas Conservation Committee
Concurrence:
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Homer L. Burrell, ~Chairman
Alaska Oi I and Gas Conservation Committee'
------- -
February 26, 1988
Telecopy No.
(907) 276-7542
ADM I N 1ST RAT I V E A P PRO V A L N o. 114.5
',. ~ ..,... - ., L ..... ..~,
Re: Safety flare volume, Dolly Varden platform,
ï-'lcArthur River Field
John Beitia
Operations Superintendent
Unocal Corporation
POBox 190247
Anchorage, AK 99519-0247
Dear Mr Beitia:
\
Since December of 1987 the Dolly Varden platform in Cook Inlet
has been experiencing problems with flare volumes in excess of
the allowable safety flare set by Conservation Order (CO) 114,
item 9. Extensions beyond the 15 day excess flare a.llowable set
by CO 120, Rule 2, have been issued for the last quarter of 1987
and first quarter of 1988. .
On February 25, 1988 the Commission met with representatives of
lVIarathon Oil Company. The current flaring situation on the Dolly
Varden was discussed. Efforts to identify and alleviate the .
problems were also discussed.
Per item 19 of Conservation Order 114, the Co~nission hereby
amends item 9 to read:
For each calendar month, a daily average volume of
produced gas permitted to maintain a safety flare or
flares on Dolly Varden platform in the McArthur River
Field shall be 2500 MCF [1000 MCF] per day.
This amen.dment is subject to change upon periodic review of the
situation on the Dolly Varden platform.
'-·---~1
Sincerely, _¡/... //
A , '{:;J</ ' I
¡j/n'1".'VA (; \:J~~::tt
Lonnie C Smith
Commissioner
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Telecopy No.
(907) 276-7542
July 14, 1987
ADM I N 1ST RAT I V E A P PRO V A L N o. 114.4
Re: Establishment of ßafety flare, Steelhead Platform,
McArthur River Field, Trading Bay Unit.
G. A. Graham
District Operations Manager
Alaska District
Unocal Corporation
P. O. Box 190247
Anchorage, AK 99519-0247
Dear Mr. Graham:
By letter dated July 7, 1987 you requested, on behalf ofUnocal,
the establishment of an allowable flare volume for the Steelhead
Platform. The Steelhead Platform will be used to develop the
McArthur River Middle Kenai Gas Pool, the Tyonek G-Zone Oil Pool,
and the West Foreland Oil Pool in the Trading Bay Unit.
The Commission hereby approves, for each calendar month, the
daily average volume of gas permitted to maintain a safety flare
or flares on the Steelhead Platform in the McArthur River Field
shall be 1000MCF per day. All gas flared shall be metered and
reported monthly on the Producer's Report of Gas Disposition
(Form 10-422).
S i~cerely :' [) \
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Lonnie C. Smith
Commissioner
jo/3.AA114
BY ORDER OF THE COMMISSION
be:l.AA 114
Yours very truly,
:::: 7K~/:!J~
Commissioner
Your application, dated December 17, 1984, requesting a flare
limit exception for Platform Anna for the period of January 15,
1985 to September 15, 1985 has been received by the Commission.
The application indicates that the same problems exist that were
presented in your June 14, 1984 application but that with the
installation of a compressor, Union Oil Company of California may
be able to purchase the excess gas and put i~ into the Cook Inlet
Gas System. It is stated that negotiations are underway to sign
a contract to sell the excess gas.
The Alaska Oil and Gas Conservation Commission has reviewed the
data available and finds that, at this time, the flaring of
excess gas on Platform Anna is an operational necessity.
By this letter, Amoco Production Company is hereby permitted to
flare all gas not beneficially used on Platfiom Anna from
January 15, 1985 until September 15, 1985. Amoco Production
Company representatives will meet with the Commission on
September 4, 1985 to present the data pertinent to the disposal
of the excess gas. '
Hr. t~. G . Srot t h
District Manager
Amoco Production Company
P. O. Box 100779
Anchorage, Alaska 99510-0779
Dear Mr. Smith:
Re: The application of M{OCO PRODUCTION COMPA~1Y to flare gas in
a quantity that exceeds the current permitted volume at
Platform Anna, Granite Point Field.
t10. 114.3.
APPROVAL
ADM I N 1ST RAT I V E
December 27, 1984
J
June 19, 1984
ADM I N 1ST R A ~ ~cY ~r-A~? P, R 0 ~.~ L
NO. 114.2
-- ~-
Re: The application of Atl0CO PRODUCTION COt1FAl~ to flare gas in
a quantity that exceeds the current permitted volume at
Platfornl Anna, Granite Point Field.
Hr. W. G. Smith
District Manager
Amoco Production Company
P. O. Box 100779
Anchorage, Alaska 99510-0779
Dear I1r: Smith:
Your application was received on June 18, 1984 requesting
approval to flare gas in excess of the 700 l1CFPD safety flare
volume due to the continued failure of the Granite Point gas
pipeline. It was indicated that pipeline repair costs were such
th~t the repair costs could not be recovered in five years and
that there is no a.ssurance tha.t the repair of tbe four known
leaks would preclude the presence of other leaks in the pipeline.
It was also indicated that other options for the disposition of
the gas are being considered.
The Alaska Oil and Gas Conservation Commission has carefully
reviewed the data available and finds that the flaring of gas on
Platform Anna is an operational necessity.
By this letter, Amoco Production Company 1shereby permitted tó
flare all gas not beneficially used on Platform Anna from July
IS, 1984 until January 15t 1985 with the provision that Amoco
Production Company representatives meet with the Commission at
9:00 am, December 12, 1984 to present the method or methods that
will be used to save the gas.
Yours very truly,
-/ / 'J /J
'Ho-r-rl tJ /[;;-¡-tLí
Harry W. Kugler
Commissioner
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BY ORDER OF THE COMMISSION
Ie
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BY THE ORDER OF THE COMMISSION
Yours very truly,
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Harry U. Kugler
Commiss:f.oner
The Alaska 011 and Gas Conservation Commission has carefully
reviewed the data available and finds that the flaring of -
excess gas on Platform Anna Is an operational necessity.
By th1.s letter, Amoco Production ComJ)any is hereby permitted to
flare all gas not beneficially used on Platform Anna from
January 15, 1984 until July 15, 1984 with the provision that
Amoco Production Company representatives meet with the
Commission at 9:30 AM June 13, 1984 to present the method or
methods they will use to save the gas after July 15t 1984.
Your application was received on December 28, 1984 requesting
approval to flare gas in excess of the 700 MCFPD safety flare
volume due to the failure of the Granite Point gas pipeline.
It was indicated that pipeline repairs are not practical in the
wtnt~r due to ice conditions in Cook Inlet and t1ü~t other
alternatives are under consideration.
Mr. Warren Nielsen
District Superintendent
Amoco Production Company
P. O. Box 100779
Anchorage, Alaska 99510
Dear Mr. Nielsen:
ADM I N 1ST RAT I V E A P PRO V A L NO. ~11~J:~
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Re: The appli.ca,tion of AMOCO PRODUCTIO!t COMPAttY to fltlre gas in
a quantity that exceeds the current permitted volume at
Platform Anna. Granite Point Field.
January 5, 1984
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AMOCO
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Amoco Production Company
Post Office Box 100779
Anchorage. Alaska 99510
907-272-8471
W. G. Smith
District Manager
September 9, 1985
Mr. C.V. Chatterton, Chairman
Alaska Oil and Gas Commission
3001 Porcupine Drive
Anchorage, Alaska 99501
File: TJZ-318-383.3
Dear Sir:
Flare Limit Exception Order, Platform Anna
Reference: Administrative Approval No. 114.3
We understand that our flare limit exception for Platform Anna expires
September 15, 1985. As discussed in the meeting between the AOGCC Commi-
ssioners and Bryan Dotson on September 5, an extension is not needed since
Anna I s fl are has been 1 ess than 700 MCFD for the 1 ast seven months.
Please refer to the attachment for flare volumes for 1985. Furthermore,
we expect Union to complete installation of their compressor at Granite
Point within the next two months. After commissioning, this compressor
will allow sale of excess gas from Anna and Bruce.
Thank you for your previous attention to our flare limit exception.
Please address any questions to Tom Zimmer at 272-8471.
;¡;2Z¿
W.G. Smith
District Manager
BDD/dds
Attachment
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FEB MAR APR MAY JUN JUL
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OCT NOV DEC JAN
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Platform Anna
Daily Flare Gas Volume
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Amoco Production Company
W. G. Smith '
District Manager
Post Office Box 100779
Anchorage, Alaska 99510
i 907 -272-8471
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December 17, 1984
File: TJZ-208-383.3
Mr. C. V. Chatterton, Chairman
Alaska Oil and Gas Commission
3001 Porcupine Drive
Anchorage, Alaska 99501
Dear Sir:
Flare Limit Exception Request, Platform Anna
Reference: Administrative Approval No. 114.2
Please extend our flare limit exception for Platform Anna from the current
January 15, 1985 deadline to September 15, 1985. As discussed in the
meeting between the AOGCC Commissioners and Bryan Dotson of this office on
December 12, 1984, we are making progress in our efforts to obtain an
outlet for Platform Anna's excess gas. In addition, Platform Anna has not
exceeded the flare limit in four of the past 12 months. The deadline
extension will allow Amoco to flare gas in excess of 700 MCFD on Platform
Anna on occasion until a sales connection can be made.
As you are aware, several leaks were found in November, 1983 in our gas
line from Anna to East Forelands. The economics of repairing the line or
installing a compressor at our own expense at Granite Point are prohibi-
tive, as we pointed out in our letter of June 14, 1984. The best prospect
for a sales outlet is the installation, by Union, of a compressor at
Granite Point to boost the gas into their Cook Inlet Gas System (CIGS).
We understand that Union is planning to install a compressor during the
summer of 1985 to handle gas from their own Granite Point platform, as
well as our Anna and Bruce platforms. Currently, we are preparing a
revision to our existing sales contract with Union providing for gas
delivery at Granite Point. We expect to sign the revision in the first
quarter of 1985.
Please note that, recently, we have been flaring somewhat more than the
700 MCFD limit some months and somewhat less than the limit other months.
Included as Attachment One is a plot of Anna's flare gas rates for the
past twelve months.
RECEIVED
DEC 2 it 84
Alaska au & Gas Cons. CommiSSÎon
A__L.._____
· ..
--
~-
Mr. C. V. Chatterton, Chairman
TJZ-208-383.3
December 17, 1984
Page 2
To summarize, we are flaring roughly 700 MCFD off Platform Anna, exceeding
the limit on occasion. We expect to have a sales outlet next summer when
Union installs a compressor at Granite Point. At that time, flare volumes
will be reduced significantly.
Thank you for the opportunity to discuss the disposition of our Granite
Point gas. Please contact Tom Zimmer at 272-8471 if you have any
questions. -------- - ~-- ----.-- -~-.~--'------
Very truly yours,
--;7-- . <'
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W. G. Smith
District Manager
Attachment
BDD/dds
RECEIVED
DEC 24 _
AlaSka Oii &: Gas Cons. CommissIon
Anchorage
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SE:P
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AUG
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JUL
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JUN
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FEB MAR APR MAY
I
JAN
1984
(
DEC
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NOV
200
OCT
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ATTACHMENT ONE
Platform Anna
Daily Flare Gas Volume
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Amoco Production compan'1Ê' 2 F ~:~ -Ä-
Post Office Box 100779 ¡It, I 3 "_
Anchorage, Alaska 99510 '.. ,- ~~;
907 -272-8471 I I ì '-:<:X.-
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AMOCO
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W. G. Smith
District Manager
File: TJZ-048-383.3
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June 14, 1984
Mr. C. V. Chatterton, Chairman
Alaska Oil and Gas Conservation Commission
3001 Porcupine Drive
Anchorage, Alaska 99501
Dear Sir:
~~'Îe
Flare Exception Request, Platform Anna
Please extend our flare\exception request for Platform Anna from our
current July 15, 1984, ~eadline to January 15, 1985, to allow Amoco to
continue gas connect ion I negotiations with Union. This extension was
_~-..L...
discussed during the~ 13, 1984, meeting between the AOGCC
Commissioners and Tom Zimmer of this office. The deadline extension
will allow Amoco to flare gas in excess of our allowable 700 MCFD on
Platform Anna from time to time while the disposition of excess produced
gas is determined since our AnnajEFDF pipeline is shut-in.
The following discussion summarizes Amoco's position on Platform Anna's
produced gas as was detailed by Tom Zimmer:
The current 7¢jMCF gas contract with Unions does not generate
economic cash flows to repair the AnnajEFDF pipeline. The pipeline
was inspected during the week of November 20, 1983, and found to
have four leaks at field welds in an area just east of our Platform
Baker. The engineering estimate to set the break areas on
pedestals, remove the cement sheaths from the weld area and install
repair sleeves is conservatively $250,000. Assuming a five-year
project life, the repair would still be $98,000 in the red after
five years. More importantly, the diving during the leak
identification showed lower volumes at each progressive leak (less
available pressure) further away from Platform Anna. Amoco's
conclusion is that even if the four identified leaks were repaired,
additional problem areas closer to EFDF are likely.
\
RECEIVED
JUN 1 81984
Alaska Oil & Gas Cons. Commission
Anchorage
'-
~
Mr. C. V. Chatterton
TJZ-049-383.3
June 14, 1984
Page 2
A similar cash flow analysis was presented for a $700,000
compressor installation. Again, at 7¢/MCF the project is' $342,000
in the red at the end of a ten-year project life. The cash flow
analysis for the pipeline repair and compressor installation are
attached.
The compressor option could be economic if a reasonable gas price
or operating agreement is negotiated. Again, Amoco is pursuing
this option and initial repsonse from Union is favorable. The
timing to justify our six-month extension is also attached.
Finally, the result of restricting production by limiting the flare
was reviewed. For every 100 MCFD of gas shut-in, at a GOR of 485,
the total State royalty, severence and ad valorem tax loss is
$890/day (loss of 210 BOPD). This analysis is also attached.
In summary, Amoco is pursuing a gas connection for our Granite Point
excess gas and will advise you of our negotiation progress. The flare
limitation exception will permit Amoco to maximize current production,
ultimate recovery and state royalty and tax payments. Amoco's position
is that the conservation of gas will not be achieved by restricting the
flare now since the same volume of gas will ultimately bý-flared over
the life of the project.
Thank you for the opportunity to discuss our Granite Point gas
disposition. Please contact Tom Zimmer if you have any questions.
Very truly yours,
d/Æ~~d'
W. G. Smi th
District Manager
Attachments
TJZ/dds
RECEIVED
JUN 1 81984
Alaska Oil & Gas C. r'f1S Comml's'
Vi, , slon
Anohora;Jö
/.
)
)
PIPELINE REPAIR ANALYSIS
ASSU~'lPT IONS:
1. Pipeline repair will extend life of pipeline five years. This
is optimistic since the Anna-EFDF pipeline has suffered many
failures in the past.
2. 1.0 MMSCFD declining 10 percent per year.
3. Straight line amortization of repair costs.
.
4. Fi fty percent (50%) Federa 1 Tax .
5. Zero percent (0%) Interest Rate.
6. Ten thousand dollars ($10,OOO/yr) operating cost.
7. Seven cents ($.07/MCF) gas sales þrice, no royalty, no severance
tax.
ANNUAL G,AS
PRODUCTION REVENUE AT '"ANNUAL AMORTIZED NET REVENUE'AFTER
YEAR MCF $.07/MCF OPERATING COST REPAIR COST FEDERAL TAX ,
1984
1985
1986
1987
1988
365,0.00 $25,550 '~$10,000 -$50,000 -$17,225
328,500 22,295 - 10,000 - ,50,000 - 18,852
295,650 '20,695 -'10,000 ..,. 50,000 - 19,652
266,085 18,6'26 - 10,000 - 50,000 ~ '20:, 687 :
239,476 16,763 - 10,000 ... 50,000 - 21,618'
Total Net Rè.venue (Loss) ($98,034')'
Even under favorable assumptions, pipeline cannot berepa'ired econo~icðlly
under current gas contract.
RECEIVED
JUN 1 e 1984
Al,aska Oil & GaG C,i:':~ C'11n¡ssiçn
Ar¡"::['J",
/_~A'
)
)
COMPRESSOR INSTALLATION ANALYSIS
ASSUMPTIONS:
1. Ten year compressor life, $700,000 to install.
2. 1.0 MMSCFD declining at 10%/year.
3. Straight-line amortization of compressor.
4. 50% Federal tax
5. 0% interest rate
6. $15.000/year operating cost',
7. $O.07/MCF gas sales pr5ce, no royalty, no'severance tax
.'
.,. AtlNUAL CA$ ANNUAL ' , ,AMORTIzro
PRODUCTIOH REVENUE AT . OPERATING COMPRESSOR NET REVENUE
YEAR MCF $0.07 /è~F " ~.O_S_T_ _~ COST AFTERTAX
- . w _ _ _ ..... .._. - - " - - - .
1984 355,000 $25,550 -$15,000 ~$70, 000·, ~$29,725
1985 328,500 ,22,295 - 15 Þ 000 ' - ,70~OOO - 31,352
1986 295,650 20,695' - 15~OOO,' - 70,000 ' -32, 152
1987 266,085, 18.626 ~, 15, 000 , - '70,000 '- 33,187
1988 239,476 16,.763 -, 15,000 ' - 70 _ 000, - '34 'I 118
1989 215,528 15,087 - 15,000 - 70,000 ~34,956
1990 193,976 13, 578 . - 15,000 -',70,000 -:- 35, 711
1991 174,578 12,220 15,000 - 70,000 - 36,390
1992 157,120 10,998 - 15,000 - 70,000 - 37,001
1993 14 1, 408 9i898 - 15,000 - 70,000 -37,551
Total Net Revenue (Loss) (S 342, 145)
RECEIVED
JUN 1 81984
Alaska Oil, & _ ßaß, COfU)! CQmm.lS!tOlt _
Anchorage
I "'r !,j ~
')
RESULTS OF RESTRICTING GAS FLARE/OIL PRODUCTION
PLATFORM ANNA
Oil Production Loss/laD MCFO gas shut ih:
100 [v1CFO =
485 GOR (5-84)
210 BOPO
State Revenue Loss/IOO MCFO gas shut in:
State Royalty = 210 BOPO x $3.25/BBL = $680/0ay
State Severance and
Ad Valorem Taxes = 210 s~po x $l/BBL = $210/day
Total Loss
= $890/day
NOTE: Conservation of gas will not be achieved because the same volume of
gas will be flared over the ,life of the project.
.'
R E eEl V ED
JUN 1 e 1984
Alaska Oil & Gas Cons. Commission
Anchorage
Gran~te Poir~tGas D,ispo'sitiori
, ,
Negoc!ùte w/Union Orden
- Co n~ D re 5 ~ 0 r & -Comprouor
Sales Contract If Economical
Co'mprassor
Delivery ,
Install
Compressor
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Legend
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MARATHON
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MARATHON OIL COMPANY
PRODUCTION-UNITED STATES AND CANADA
ANCHORAGE DIVISION
-- I
P.O. SOX 23S0 I DIR Þ
ANCHORAGE, AI rSKA .51. _.9-' .'
C. GtOL ~,
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Hay 19, 1972 . I '!'_ENG,~
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CONFER:
FlLE:(,O/1 t.(
P¡,L/,\ ~ ,/-L
Attached are four copies of Exhibit 1. TŸI0 are for the
Mr. O. K. Gilbreth
Alaska Oil and Gas Conservation committee
3001 Porcupine Drive
Anchorage, Alaska
Attention:
Gentlemen:
Safety pilot Hearing, Dolly Varden Platform, and two are for
the Safety Pilot Hearing, Trading Bay Production Facility.
Yours very truly,
i!~r~
JRB:dp
Attachments
l0J~OWlœ~\
~ W ~ ' !j
fIAV/) Jt
~'i}ì f CJ 2 1972 ~
DIV/SION OF OIL
,,"'.1 ANt> 01~-
P"II~Q.fQ~OH '''s', ,
EXHIBIT 1
u SUBMARINE TRENCH
C. o. I' <..( 0 f.( I ( ~ f i ( ll.-
)
\
SCALE: 1": 4000'
EXISTING PIPELINES
COMPLETED GAS GATHERING SYSTEM
PIPELINES UNDER CONSTRUCTION
LEX PLANT - COMPRESSOR STATION
SAND & GRAVEL DUNES < 10'
" " "> 10 '
(-)
COLLIER CARBON
6 CHEMICAL CO,
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W£ST
FOR£LANO
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MARATHON - UNION
GAS GATHERING SYSTEM
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AMOCO
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PROD~ION' fÄCILlTY ./"'"
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R Be R COURT REPORTERS
825 WEST EIGHTH AVENUE-SUITE 5
277-4713
ANCHORAGE,ALASKA 99~OI
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23
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19
18
17 THOMAS R. MARSHALL, Member and Executive Secretary
16 O. K. GILBRETH, JR., Member
..
HOMER BURRELL, Chairman
15
14 APPEARANCES:
13
},I
12
11
10
9
8
May 12, 1972
7
HEARING ON CONSERVATION FILE NO. 114
6
5
TRANSCRIPT OF PROCEEDINGS
4
3
OIL AND GAS CONSERVATION COMMITTEE
2
)
BEFORE THE STATE OF ALASKA DIVISION OF OIL AND GAS
1
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R 8c R COURT REPORTERS
825 WEST EIGHTH AVENUE-SUITE 5
277·4713
ANCHORAGE, ALASKA g9501
ADDENDA: ~ rt' Ct" t (,...o J,
,TESTIMONY OF R. C. KELLER RE. GRAYLING PLATFORM
TESTIMONY OF R. C. KELLER RE. MONOPOD PLATFORM
TESTIMONY OF B. C. ANDERSON RE. PLATFORM 'A' AND SPARK
TESTIMONY OF MAX BEAZLEY RE. GRANITE POINT SHORESITE
PAGE NO.
S
26
51
78
90
107
III
113
119
A. O. P. CASPARIAN
MILLARD OWENS, &~OCO PRODUCTION COMPANY
BART GILES, AMOCO PRODUCTION COMPANY
MILLARD OWENS, AMOCO PRODUCTION COMPANY
MAX BEAZLEY, MOBIL OIL CORPORATION
JOHN. R. BARBER, MARATHON OIL COMPANY
B. C. ANDERSON, ATLANTIC RICHFIELD COMPANY
'R. C. KELLER, UNION OIL COMPANY
JOHN R. BARBER, MARATHON OIL COMPANY
1 WITNESS
TABLE OF CONTENTS
Page 2
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25
24
23
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22
21
20
19
18
17
16
15
14
13
12
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8
7
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1
PRO C EE DIN G S
2
MR. BURRELL: Good morning, ladies and
3 gentlemen. This is a hearing of the Alaska oil and Gas Conser-
4
vation Committee. My name is Homer Burrell; I'm Chairman. To
5
my right is Mr.,O. K. Gilbreth, Jr., member of the Committee;
to my left is Mr. Thomas R. Marshall, Jr. who's a member of the
6
7
Committee and Executive Secretary of the Committee. I'll read
8
the notice of this hearing. Notice of Ptiblic Hearing, Alaska
9
Oil & Gas Conservation Committee, Conservation File; No. 114,
Subject: Granite Point Field, Trading Bay Field, McArthur
River Field, and Middleground Shoal Field. . The Alaska Oil &
Gas Conservation Committee will holding a hearing pursuant to
Title XI, Alaska Administrative Code, Section 2Q09, to consider
the amount of gas necessary for'adequate safety flares on pro-
duction platforms in the referenced fields'as required in
Conservation Orders No.. 102, 103, 104, and 105. The hearing
will be held at 9:00 o'clock a.m. May 12, 1972 in the City
Council Chambers of the Z. J. Loussac Library, Fifth Avenue and
F Street, Anchorage, Alaska, at which time operators of the
oil pools within the referenced fields and affected and interested
parties will be heard. Signed by Thomas R. Marshall, Jr.,
Executive Secretary, published in the Anchorage Daily News on
April 13, 1972.
Mr. Marshall will swear any witnesses; those who have not
previously qualified as experts will be requested to do 50.
R '& R COURT REPORTERS
825 WEST EIGHTH AVENUE-SUITE S
277·4713
ANCHORAGE. ALASKA 99501
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MR. ANDERSON: Mr. Chairman, members of the
Committee. My name is Robert H. Anderson, Attorney for Marathon
Oil Company, at Anchorage. As you have just recited, the Corn-
mittee's notice of hearing has stated the purpose to bs to
consid,sr the amount of gas necessary for adequate safety flares,
and though the notice does not so state, we believe this tarm
could be changed or also referred to as a safety pilot for the
platforms for the four ailfields in Cook Inlet, as required by
the Conservation Orders 102 through 105.
MR. BURRELL: All right, Mr. Anderson, we
have no objection to your change in the terminology, and we
would expand the hearing unless there's obj'8ction to inclucla
safety pilots at any other location in connection with the oil
, production from the, referenced oil pools.
HR. ANDERSON: There would be no objection.
MR. BURRELL: If anybody doss at anyt.ime
in the context of the testimony, they may feel free to do so
since we did not expand the Order to include the onshore pro-
duction facilitiss or other locations where ~h$re ara flares.
I might also point out we have U.s. G~ological Survey repra-
sentativas here today, and they are frse to ask questions at
anytime and will b2 invited to do so as they have a concern in
this matter not only in Alaska .but in other areas in which th3Y
have the regulatory responsibility.
MR. .ANDERSON: Proceeding on then, for
R 8c R COURT REPORTERS
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1 convenience and orderly presentation, since the notics does
2
specify platforms, we will present a witness for the operators
3
for eachµatform. I'll introduce the witnesses for the McArthur
4 River Field, the Trading Bay Field, and the Trading Bay Field
5 Northeast oil Pools. Perhaps it's appropriate at this point to
6 briefly outline a summary of the presentations and request that
7 this order of presentation be approved by the Committee.
8 Referring to the map that was ussd yesterday which shows
9 the platforms, Mr. Ed MacFarland will point out the platforms,
10
11
we'll start with the Dolly Varden platform, Harathon Oil
Company operators, Hr. John R. Barber. We will then proceed to
the Grayling platform, Hr. R. E. Keller of Union Oil COr.lpany,
12
13
operators of Grayling. Then in order to complete Mr. Keller's
14
, testimony, we will skip to the Monopod platform of the Trading
15
Bay Field, and then we'll come back to the King Salmon platform,
16
McArthur River Field, with Mr. B. C. Anderson of Atlantic
17
Richfield Company t·estifying. Mr. Anderson will also then
testify with respect to the Platform A and the Platform Spark.
18
19
And in view of the change hars on the onshore designation, we
20
will then re-pres8nt Mr. Barber at that time concerning the
21
safety pilot at the Trading Bay Production Facility since four
22
of thoss platforms do go into the Trading Bay Production Facility.
23
After that then we will go to th.e Mobil Number One platform,
24
and Mr. M. E. Beazley of Mobil Oil Corporation will testify, and
25
at that time Mr. Rish Thornton and Mr. ~i. R. Harrison, Attorneys
R Be R COURT REPORTERS
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1 for Mobil Oil Corporation, will take over with respect to the
Mobil platform. After that time we will then go over to the
2
3
Anna and ,Bruce platforms, Granite Point Field, and Mr. M. E.
\ 4 Owens of AMOCO Production Company will testify, and Mr. Ralph G.
5 Crews, Attorney for AMOCO, will present Mr. Ownens. In order
6
to complete his testimony then we will go on down to the Middle-
ground Shoal Field and the Dillon and Baker platforms that will
.':")1 .
7
8 be testified to with respect to Mr. Owens. And than finally the
9 Shell A and Shell C platforms in the Middleground Shoal Field
10
will ba completed by testimony with
from Mr. A. O~ P.
11 Casparian of Shell Oil Company, and Mr. Joseph Rudd, Attorney
12 for Shell Oil Company will present Mr. Casparian.
13
These witnesses will generally explain and give a das-
14 cription of the gas handling process facilities and concarning
'15 the size of an adequate safety pilot. Does this order of pra-
16 sentation meet with the committee's approval?
17
MR. BURRELL: No objaction at all, Mr.
18 And'erson.
19
MR. MARSHALL: I have one small question
20 here. You referred to the facility on West Foreland as the
21 Trading Bay Production Facili~y. I noticed yesterday this was
22 r~fsrred to as the West Foreland Facility. We should cl~rify
)
23
what we're going to call it for .the purposes of the hearing here.
24
MR. ANDERSON: Well, since we've used the
25 phrase West Foralands yssterday, then we will use the sam9 here,
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the 'vest Foreland Production Facility, although it is also known
2
as the Trading Bay Production Facility. That way we won't havs
3
'(unintelligible.)
4
MR. BURRELL: For the purposa of clarificatio~,
5
ths ~';¡est Foreland or Trading Bay
6
MR. ANDERSON: All right, fine.
7
,HR. BURRELL: --- since it serves both th:e
8
Trad~ng Bay,Field and the 11cArthur River Field or Trading Bay,
9
is that corrsct?
MR. ANDERSON: That's correct.
MR.. CRE\vS (?): I'll give you an affidavit
of idantity,!Hr. Commissioner. They're onß in tHe same.
MR. BURRELL: You're qualified as an expert.
MR. ANDERSON: FOllowing the procedure
that was established yesterdaý and' for convenience, we request
that all the witnssses which I've just nam'ed be s~vorn in at
once at this time,'if that's satisfactory.
MR. BURRELL: It is.
MR. ANDERSON: All right, would Mr. Bob ---
MR. CRENS: Bob, just a minute. In addition
to Hr. Owens for MI0CO, Hr. Bart Giles \..,i1l also testify.
HR. BURRELL: Thank you.
MR. ANDERSON: All right, Mr. Barber, Hr.
Keller, Mr. Anderson, Mr. Beazley, Mr. Casparian, Mr. Giles. I
think that covers evaryone.
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82.5 WEST EIGHTH AVENUE-SUITE S
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ANCHORAGE, ALASKA 99~OI
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MR. BURRELL: Mr. Marshall, would you swear
the witnesses.
MR. MARSHALL: Please raise your right hands.
In the matter now appearing, do you swear to tell the truth,
the whole truth, and nothing but the truth, so help you God.
(Witnesses'answer in the affirmative.)
MR. ANDERSON: We will now call our first
witness, Mr. J. R. Barber, Marathon Oil Company, operator of
the Dolly Varden platform. Mr. Barber has not been qualified
or testified before this Committee before, and I'll ask Mr.
Barber to state his qualifications for acceptance by the
Comrnitbee.
MR. BARBER: My name is John Barber. I
graduated from Texas A & I University in 1954 with a B.S.
degree in PetroletL'1\ Engineering. I joined Marathqn Oil
Company that same year. I worked in various fields and
New
'capacities inA1exico, West Texas, advancing to Area Engineer
in 1963. In 1967 I was transferred to the Los Angeles Division
Engineering Staff. Early in 1968 I was transferred to Anchorage,
Alaska as Area Production Superintendent and have served in
this capacity since that time.
MR. BURRELL: Without obj ~ction, w,e' 11
accept Mr. Barber's qualifications.
MR. BARBER: Marathon Oil Company is a
suboperator in the 'McArthur, River Field, Trading Bay unit. As
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8211 WEST EIGHTH AVENUE-SUITE !S
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1 a suboperator, Marathon's responsibilities include the operation
2
of the Dolly Varden platform. As indicated on my exhibit #1,
which is 'the Pipeline Exhibit #2 from yesterday's testimony,
4
the Dolly Varden platform is the southernmost platform in the
McArthur River Field.
5
6
The primary operations on this platform include oil and
7
gas production, gas compress'ion, and water injection. Currently,
the oil production rate is in excess of 44,000 barrels per day.
8
9
This oil is being produced from an average vertical depth of
approximately 9500 feet, utilizing high pressure casinghead gas
10
11
injected into ,the tubing string as the artificial lift machanism.
12
Approximately 45,000 MCFPD of gas is being compressed on the
13
platform each day. Of this volums, 30,000 MCF is compressed to
14
1250 psig and utilized as gas lift gas in the oil production
15
process. The remaining 15,000 ~1CFPD is compressed to 250 psig
16
and either utilized as fuel gas, transported to the Trading Bay
17
Production Facility ,for processing through the low temperatures
18
liquid extraction plant, or part is used to maintain a safety
19
pilot. Water injection operations include processing and injscti~g
20
approxim~tsly 60,000 barrels of deaerat~d wa~er per dêY at 3500
21
psig into the H~~lo~k ~eservoir for pressure maint~nance purposss.
22
It is the cont-ention of Marathon Oil Company that the size
23
of a safety pilot required to maintain safe opsrations on the
24
platform is not only r,=lated to such factors as weather conditions
25 .
and flare stack configuration, but is also directly r~lated to
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1 the type of production operations, particularly the gas handling
2
proc9Ss, being conduct~d. For this reason, we feel it is very
3 p~rtinant to this hearing that you, th'; Oil and Gas Cormnittee,
4 fully unders~and the gas systzm on the 'Dolly Varden platform.
5 To aid in explaining this system, Exhibit #2, a basic schematic
6 flow diagram depicting the g2.S flow on the platform, has been
7 prepar'ed.
8 At this time, utilizing the flow schematic, I will trace
9 the gas flo\1}' beginning with the producing wells going through the
10 production separators, gas compressors, and returning to the
II producing walls. Crude oil and associated solution gas produced
12
from a tot~l of sightaen oil wells on the platform are gathersd
13 into one of five production separators. In each of these vessels,
14 the gas is separated from the crude oil and is gathered into a
15 co~~on manifold directsd to the suction scrubber of sither of two
16 compressor packages. These packages are identical with each unit
17 containing one 3,000 horsepower reciprocating compressor and
18 associ'ated equipm·snt. Since these units are identical, flo\'1 will
19
only b9 traced through one unit. Gas enters the suction scrubbsr
20
from ~he production separators at 90 psig. From this'ærubbsr,
21
the gas goes ~hrough the first stag~ of compression where it is
22
compressed from 90 to 250 psig. This gas is then cooled and
23
scrubbed to remove any sntrainad liquids.
24
Downstre~ of the first intsrstage scrubber, the gas flow
25
is split into two separate streams, one going to ~1e second stage
~1
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of compression and ths other going to the West Foreland Pro-
2
duction Facility for processing. The gas baing sent to the
3
West Foreland Production Facility comprises what we refer to as
4
the 'gas to shore' system. Following this system through on the
5
diagram, notice that both compressor units contribute to the
6
total gas to shore volume. Also, as shown on the diagram, the
7
platform fuel gas requirements are satisfied with gas from the
8
gas to shore system. This system supplies fuel gas to the Solar
9
10
turbines and boilers as well as supplying the deaerator with its
11
required gas volume. All casinghead gas in excess of these
12
requirements and safety pilot requirements is transported to
13
the west sids of Cook Inlet·for processing through the LEX
Unit.
14
15
Returning to the portion of the gas stream going to th~
second stage of compression, we will continue to follow the gas
flow through the compressor unit. In the second stage of
compression, th~ gas is compressed from 250 psig to 480 psig and
is compressed to 1250 psig in the third and final stage of
compression. Third 'stage gas from both compressor units is then
combingd.
This high pressure gas is piped to the individual wellhead
rooms where it is injected down the tubing casing annulus of
each of the oil walls on the platform. The gas enters the
tubing through specially designed valves and lifts the cruda oil
to tha surface.
This gas lift gas returns to the surface with
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1 the crude oil where it is recompressed.
2
For the sake of simplicity, the safety pressure relief
system was not shown en this diagram. However, I would like to
3
4
point out that this relief system is piped into the flare system
5
downstream of the flare valve. The discharge side of the safety
6
relief valves installed on all of the coded hydrocarbon pressure
7
vessels are piped into this systam. We have thirty coded ves~
8
sels on the platform. Should the pressure in any of these ves-
9
sels exceed the set pressure of its relief valve, the value auto-
10
matically opens and relieves pressure by venting gas into tha
11
flare system.
12
As previously mention·ed, the amount of gas requirad to
13
maintain a reliable safety pilot is directly relatsd to the
14
production operations. Now that the gas flow has besn explained,
15
I would like to point out some op~rating conditions under which
16
the safaty and the wellbeing of all personnel and equipment
located on the platform d~pends upon a relia.bl,e saf,~ty pilot
18
and ths burning of vented gas.
19
As mentioned earli~r, approximately 45,000 MCF of gas
20
is being compr9ss9d on the platform each day. If for. any r~ason
both:compressor units were to shut down simultaneously, the
21
22
flare valve shown in the flow diagram would ~h=n automatically
23
open and gas would be vented until conditions on tha platform
24
stabilizad. Tha flare rate during the firs~ few mom~n~s of th9
25
shutdown would be approximatsly 90,000 to 95,000 MCF per day.
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1 The additional flare rate above the 45,000 MCF per day that is
2
continually being producsd is the result of an automatic safety
3
system built into each compressor unit whereby the suction
4
bottles, su~tion- and interstage scrubbers, discharge bottles,
and all associated piping is depressured immediat~ly upon a
5
6
compressor shutdown.
7
This 90,000 to 95,000 MCF per day gas rate may last for
8
only a short time; however, the safety pilot must be sufficiantly
9
stable to withstand this high rate without being extinguished.
10
If the safety pilot is extinguished, then the platform could be
11
exposed to hydrocarbon vapors and possible ignition. Under
12
normal operating conditions, both compressors do not shut down
13
simultaneously; however, there are certain safety alarms and
14
, oper~tional functions ~hich would require a simultaneous shutdown
15
of both compressor units. These conditions include platform
16
electrical failures, excessive pressure in tha production
17
separators, occurrence of hydrocarbon vapors, excessive plat-
18
form vibration as a result of an earthquake or other outside
19
forces.
20
Other operating conditions where lesser flare rates occur
21
but yet where an adequate safsty pilot is required to proparly
22
dispose of the venting gas include compr-sssor shutdovlns involving
23
only one unit, excessive pressure in process vessels resulting
24
in venting gas through ths safety relief sys~em, equipment
25
failures requiring equipment to be de-pressured through the
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1 flare syst9m, and so forth.
2
To further amplify how the safety of the platform depends
3 on an adequately lighted safety pilot, I direct your attention
4 to Exhibit #3, which is an expanded view of the Dolly Varden
5 platform. This platform consists of three decks. The sub deck
6
contains the platform heating equipment and the shipping pumps
7
utilized to ship oil to the West Foreland Production Facility.
8
The production deck houses the wellheads, production vessels,
9
electrical power generation facilities, as well as a portion of
10
the water injection facilities and gas compression equipment.
11
The'top deck, referred to as tha drilling deck, contains two
12
workover rigs and associated equipment, the 'remainder of the
13
gas compression, water injection facilities, and living faci-
14
litie~ for approximately seventy men. All of this equipment is
15
contained in an area of approximately 27,000 square feet on
16
three decks, or approximately six-tenths of an acre.
17
The flare boom extends from the southwest corner of the
18
production deck at an angle of eighteen degrees above the hori-
19
zontal. This boom is approximately 100 feet long. It is readily
20
apparent that should the pilot light be :extinguished for whatever
21
reason and natural gas he vented out the flare boom, a v,ery
critical condition could develop. As indicated on the drawing,
23
the area, between the drilling and production decks and between
24
the production deck and sub deck is completely enclos'ed to pro-
25
t.ect the equipment against the cold weather conditions. Th,g
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1 enclosed areas containing sources of ignition, such as the
2
generator room, are continually purged with outside air to
3 prevent any hydrocarbon vapor accumulation. However, if natural
4 gas at increased rates is allowed to escap~ unburnad from the
5 nearby flare boom, the wind conditions could be such that the
6 purge fans would pick up the gas and gas vapors could be intro-
7
duced inside the platform. Also, gas vapors could migrate to
8
outside work areas. It is apparent from this drawing that if
9
the gas vapors reached an explosion limit with ignition sourcas
10
present, an explosion could occur.
11
In view of the operating conditions of the Dolly Varden
12
platform, the weather conditions in the Cook Inlet area, and
13
the damage that could occur if an adequata safety pilot is not
14
inaintained,Marathon submits that the Cornmitbee should find that
15
a volume up to 1,000 HCF is required for an ad-equate safety
16
pilot. This volume is based on field observations of ths volume
17
required to maintain a light~d safety pilot under adverse
'18
conditions.
19
That concludes my prepared testimony on the Dolly Varden
20
platform. I'll be happy to try and answ,er any questions at this
21
time.
22
MR. BURRELL: Thank you, Hr. Barber. r--lr.
23,
Barber, what we're going to do here is we'll ask any questions
24
that come to mind as a result of~ur testimony, but we will ask
25
you and all the othar witnesses to remain availa.bl,e for qU9stions
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1
in the event w's hav,e - I shouldn't sayconflic't:ing tsstimony --
2
but different testimony with respact to the various platforms.
3
We want to try and see comparisons, why ana may require mora than
4
another, for instance. Do you have some questions, Mr. Gilbreth?
5
MR. GILBRETH: Mr. Barber, this one million
6
a day, one million cubic feet a day that you mentionad here, you
7
said that this was based on your observations and,experisnce?
8
MR. BARBER: Observations in the fisld, yes.
9
MR. GILBRETH: Would the volume that's
10
necessary depend on the burner design, for exampl,e?
11
MR. BARBER: Possibly so. I would think
12
that the equipment that is ti~d to that flare would havs a great
13
bearing on the volums r~quired.
14
MR. GILBRETH: Is it nec:essary to flare the
15
--- this volume continuously at all times for emergency then, or
16
is it just certain times you'd need this largs a volume?
17
MR. BARBER: We think up to this volume.
18
19
We don't think that it would be necessary to flare one million
20
every day of the month.
21
MR. GILBRETH: Well, under what conditions
22
would it not be necessary and under what conditions would it
23
be necessary? How would you foretell these occurrences and how
24
much you would need?
25
MR. BARBER: Weather conditions would have
a strong bearing on the volume we would think would be required.
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MR. GILBRETH: Would that be tha ---
MR. BARBER: The direction of the wind, the
velocity; things of this nature. And maybe we would only have
one compressor running instead of two, so the potential for a
large release would not be as great if you only had one com-
pressor running, and the other one happened to be down for
maintenance.
MR. GILBRETH: I see. Based on your
observations then and operation on a platform, about what par
cent of the time does your experience indicate that it would be
n~cess'ary to flare or have your pilot at this maximum volume?
MR. BARBER: I don't have that data, Mr.
Gilbr'eth,.
MR. GILBRETH: In some fields does this
occur half the time or a tenth of the tim~ or a less amount of
time?
MR. BARBER: Perhaps half. I would not
MR. GILBRETH: I see. I'm not exactly
familiar'witll just how the pilot is incorporated into your
flare boom. Does the flare from the pilot extend directly
into the path of the gas that is expelled through the flare
boom, or does it sit to the side?
it's
MR. BARBER: The ---jactually burning out
the same flare, our pil~t is. It utilizes the same flare.
MR. GILBRETH: It's not just a separate
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1 pilot ---
2
MR. BARBER: Not ---
3
'MR. GILBRETH: --- itself?
4
No. It is not. It's not like
HR. BARBER:
a pilot light feeding a boom.
MR. GILBRETH:
MR. BURRELL:
MR. MARSHALL:
I'm --- I don't quite under-
5
6
That's all I have.
7
Mr. Marshall?
8
9
stand the arrangement on the flare boom. Is the,.'flare gas
10
introduced at the base of the boom, and then' it burns through
the same orifice as the main safety escape for the gas would be
of course
in case of emergency? Both gasBs/burn through the same orifice
11
12
13
at the tip of the boom, but the pilot gas is introduced at the
14
base of the 'same boom as the other gas?
15
MR. BARBER: We don't really have an orifice
at the tip of our boom. We have more or less a pipe. It has a
16
17
flare tip on it, but it's not, you know, it's not an orifice
18
or anything, and the gas that is burned for the safety pilot
19
is introduc,ed back .at the platform and goes out that on:e --- the
20
one flare pipe.
21
HR. MARSHALL: But it's not in a sleparate
22
piping system?
23
MR. BARBER: Not in a separate pipe.
MR. MARSHALL: Just --- it's in the larger
24
25
pipe?
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MR. BARBER: Right.
MR. MARSHÞ..LL : I see.
MR. BARBER: Right.
MR. HARSHALL: What is th€re any baffling
2
3
4
5 or other arrangements to prevent blowing out by \'l'eather of the
6 pilot flare?
7
HR. BARBER: I don't believe so.
8
MR. MARSIßLL: In othsr words, it's mars or
9 less just a pipe? We've seen some rather ornata safety flare'
10
arrangemants which were dssignedto minimiz:a the effect of the
11
weatha~ on the flare. I'm curious if you've considered any of
12
thesa arrangements?
13
MR. BARBER: We have a different flare tip
14
we have not installed on the platform, but it's similar to qna
15
we have at ~'h~st Foreland. 'But as far as I know, it does not have
16
any baffles that would protect it against wind conditions.
17
MR. MARSHALL: That's all the questions I
18
have.
19
MR. BURRELL: Mr. Barber, I have a couple of
20
questions here. It's my understanding some of the platforms
21
'at least may have two flares; why do you only hav'e on,a?
22
MR. BARBER: One is ---
23
MR. BURRELL: Why do you think two might be
24
n'eces s ary?
25
MR. BARBER: One is adequate for our operatio:!
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2
MR. BURRELL: For your op8ra~icn ---
3
MR. BARBER: Yes.
4
MR. BURRELL: as based on what, throughput
5 volume of gas?
6
MR. BARBER: On the dièmeter of our flare
7 and the gas we handle. '
8
MR. BURRELL: You may have --- for instance,
9
somebody that may have two flares may hav8 smaller diameter
10
flares?
11
MR. BARBER: Possibly so. I don't know.
12
MR. BURRELL: But in your case, the diameter
13
of your flare is such that one is adequate?
14
MR. BARBER: That's correct.
15
MR. BURRELL: Okay. Next question, as I
16
understand it, the main factors relating to size of your flare
17
are, one, weather, w:eather and wind, if you will, second, your
18
gas handling equipment:, gas handling process equipment; is that
19
essentially it, or is there any other basis?
20
MR. BARBER: The sudden
well, the sudden
21
release of gas should both units go down.
22
MR. BURRELL: Right, and in the~ent ana of
23
the compressors goes down.
24
MR. BARBER: One or both, right.
25 '
MR. BURRELL: One or both.
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MR. BARBER: Right.
2
MR. BURRELL: So those three factors
3
essentially would be the major factors in determining the size
4
of your --- the safety pilot requirements, right?
5
MR. BARBER: I would ,say so.
MR. BURRELL: You also indicated that the
6
7
one million cubic feet per day which you are requesting us to
8
authorize for a safety flare would probably be adequate for the
9
worst day?
10
MR. BARBER: We think so, yes.
11
MR. BURRELL: Like the day both compressors
12
are down, the day the wind is just wrong,
13
MR. BARBER: Yes.
HR. BURRELL: a day like that?
MR. BARBER: Yes, it. would be adequa t'6 .
HR. BURRELL: What do you think about a
14
15
16
17
monthly average for flare size which would be something less than
18
thirty times a million per month.
19
MR. BARBER: Yes.
20
MR. BURRELL: Do you think an appropriate
21
it would be appropriate to enter an order which would not allow
22
you a million per day every day, but a monthly average, or do you
think there should be just some discretion, should it be with
23
24
the Committee, should it be with the platform. supervisor, or
25
what's your thought? In other words, you've already indicated
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as I underst~nd your testimony th~t you don't need a million
(
2
per day avary d~y, that's the worst situation?
3
MR. BARBER: Ne don' t n~,ed a million. Yes.
4
We feel like th~t would bs the worst.
5
MR. 'BURRELL: Right.
6
MR. BARBER: Thirty million a month, we
7 would suspect that we will have less than thirty million a month,
8 but if \"9 sayan average of so much a month, ---
9
MR. BURRELL: If it's a windy month and ths
10 compressors are down all month, you 'v,s got a problem, right?
11
MR. BARBER: We sure could have, right.
12
MR. BURRELL: Yeah.
(
13
MR. BARBER: I'd hate to prophasizs on what
14 that would av'srage a month.
15
MR. BURRELL: All right. We'd hate to
16 proph~siz'ê th~ wind or the st~~tus of the compressors.
17
MR. BARBER: Right.
18
MR. BURRELL: Hmm, that's interesting. Should
19 we --- what about an order that is less than a million, say
,20 a thirty day average but with the usual escape clause for an
21 em~rgency situation when th~re would be a compressor down, one
22 or two down, or both?
(
23
'MR. BARBER: Hell,
MR. BURRELL: What could you liva with is
I'm going to ask this of ,every other --- (thope.
24
25 my question.
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MR. BARBER: Ysah.
2
MR. BURRELL: Just b8causa you'ra tha first
3 don't think I'm picking on you.
4
HR. BARBER: ~V'ell, I think that W'ê:. could
5 live wi t.'1 somsthing l,sss tha.n thirty mill~on a month. Trying to
6 pin that number down~ I'm afr2id I couldn't do right now ---
7
MR. BURRELL: Sure.
8
MR. BARBER: --- without time trial involved.
9
MR. BURRELL: Now, that leavss anoth~r
10
alternative 6f course is to look for a little experience. Give
11
a temporary order and look for a littl's experience and than
12
write a final order after that. I'll want to ,explor,e this more
13
after I think about that. .
14
MR. GILBRETH: I'm sure the nature of this
15
so-called emergency flaring that we're talking about is such
16
that it would be almost impossible to measure the amount of gas,
17
wouldn't it, I mean in such a surg,e?
18
MR. BARBER: Yes, sir, it would, Mr. Gilbrsth.
19
MR. GILBRETH: What about measurin~ th6 mnount
~hat you hava just for the safety pilot, is this practical or
20
21
feasible?
22
MR. BARBER: Not in our installation. I
23
couldn't ' answer for the other platforms, but for,Qurs it's not.
24
MR. GILBRETH: You're not tied in in such a
25
manner that it could be measured?
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1
MR. BARBER: No, sir, we're not. That's
(
2
right.
3
MR. GILBRETH: In other words, anything W~
4 come up 'with is going to be an estimate and it's going to depend
5 on the man looking at the size of the flame out there, isn't it?
6
MR. BARBER: Well, not really. We run a gas
7 balance on our platform. We measure through the system, and then
, 8 the difference would be the safety pilot, under normal operating
9 conditions.
10
, MR. GILBRETH: That's all I have at this
11 tim'e .
12
MR. BURRELL: Mr. Marshall? I guess that's
(
13
all we have for you now, Mr. Barber. Thank you. You will bs
14
availabl1e, sir?
15
MR. BARBER: Yes.
16
MR. ANDERSON: Mr. Barber, were your exhibits
17
one, two, and three for the Dolly Varden platform prepared by
18
you or under your supervision?
19
MR. BARBER: Exhibit #1 was prepared under
20
someone else's supervision for yesterday's testimony. Two and
21
Three under mine for today.
22
(
23
MR. ANDERSON: You approved Exhibit #1 as
part of your testimony?
MR. BARBER: Yes.
24
25
MR. ANDERSON: We ask that these be accepted
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1
as part of tbe record.
MR. BURRELL: Vary good. Did we identify
them as ..--
MR. ANDERSON: Dolly Varden #1, 2 ---
MR. BURRELL: Dolly Varden #1, 2 and 3.
MR. ANDERSON: Yes. And ~..,e' 11
MR. BURRELL: Dolly Varden #1 is ---
MR. ANDERSON: Is Exhibit #2 from
MR. BURRELL: Pipeline ---
MR. ANDERSON: --- Pipeline ---
MR. BURRELL: --- Exhibit ---
MR. ANDERSON: --- Exhibit #2
! MR. BURRELL: --- #2 from yesterday.
MR. ANDERSON: --- from yesterday, and we
2
3
4
5
6
7
8
9
10
11
12
13
14
15
will furnish you smaller copies of that as we premised yesterday.
16
MR. BURRELL: Thank you, Mr. Anderson.
MR. ANDERSON: Mr. Barber will remain sworn
17
18
for later testimony on the West Foreland Production Facility.
19
MR. BURRELL: Thank you.
20
MR. ANDERSON: Our next witness is Mr. R. C.
21
Keller of Union Oil Company who will present testimony on th,e
22
Grayling platform, McArthur Rivar Field, and ths Monopod plat-
23
form, Trading Bay Field. Mr. Keller was qualified at yesterday's
Committee hearing, and. we ask that his qualifications be accepted
24
25
for the purpose of today.
.
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1
MR. BURRELL: They are.
MR. KELLER: Ny name is Richard Keller, and
2
3
I'm c~~rently ARaa Engineer with Union Oil Company, Anchorage
4 District, Alaska. My purpose here today is to describa the
gas procassing system and the need for safety pilots and to
5
6
recommend safety pilot sizes for the Grayling platform.
(M 11" h d h· b . """ h· . ,
r. Ke er s test~mony "attac e as an ex ~ ~ t ,-0 t ~s transcr~pt.
7
8
MR. BURRELL: Were you going to testify on
9 the Monopod or ---
10
MR. KELLER: Yes.,
11
MR. BURRELL: Now or later?
12
MR. KELLE R: Y:es, now.
MR. BURRELL: Now.
MR. KELLER: Unl·es s you'd like to ask
13
14
15 questions now.
16
MR. BURRELL: List's just cover this now
17 before you continue.
18
MR. KELLER: Okay.
19
HR. BURRELL: If that's okay with you, Hr.
20 Kell~r?
21
MR. KELLER: It's fine.
22
MR. GILBRETH: Mr. Keller, just looking at
23
the lexhibi ts that you've had a.nd thos,e that Hr. Barber presented'l
I
I
I
I
24
there ',5 not a great deal of diff,erence in the amount of pro-
25 duction, amount of gas production. You have two flares; they
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1 hav9 one on the Dolly Varden. This million cubic f:st a day
(
2
per flare you" re talking a.bout, since you ha.ve the two flaras,
3 is it necsss~ry that thay both go a~ th2 maximum at all timss,
4 or when you hav,= maximum ccndi ticns, is it necessary that th-:y
5 both be at maximum than?
6
HR. KELLER: Yes, sir, we feel it is. Our
7 reli·ef systam ties into both of these flares simultaneously,
8 and. like I sa.y, we hava two flares to dissipate the heat that's
9 evolved. und<:;r thosa conditions, and our experience has shown
.10 that it takes that much to keap th·e flar.es lit under thoss
11 conditions.
12
MR. GILBRETH: Well, now if I understood the
(
13
testimony, this would dspend on the production and the wind and
14 'weather conditions and so forth?
15
MR. KELLER: Yes, sir.
16
HR. GILBRETH: In your opinion, is this
17
18·
million per day that I guess w:e can call a m~ximum amount tha.t
is
would be absolutely necessary,/that necessary then regardless
19
of the amount of gas that you expect to expel in emergency
20
conditions?
21
22
MR. KELLER: I'm sorry, I --- '
MR. GILBRETH: Is itd~pendent entirely on
(
23
the wind, let's put it that way?
24
MR. KELLER: The wind and the shutdown
25 '
condition whera we vent a large amount of gas.
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1
MR; GILBRETH: Well, what I'm trying to under-
2
stand, Mr. Barbsr indicated that he's going to put out twice as
3 much in öne of his flares as you do in yours, and it takes a
4 million a day to kesp his burning, and the only comparison I
5 can see batwaen the two would be wind,
6
MR. KELLER: Yes, primarily.
7
MR. GILBRETH: --- that if there's a wind
8
condition, why you'd both need the same, but if it's the opera-
9
ting conditions, why then theoretically \-lhy it should take much
10
more than half bur~ing to go into your flare.
11
MR. KELLER: All I can say is this is what
12
our experienc:e has found. We --- if the wind is blowing a
13
c:ertain dir:ection, the discharge will put out one b~g flænê,
14
and in order to keep the heat to a minimum on this platform, we
15
do havs. the two flê.res, and primarily it's the wind that will
16
blow thesa flares out, but a combination of the two is our worst
17
possible condition.
18
MR. GILBRETH: I see. \Vhat about the con-
19
struction of your flares, do you actually have a pilot --- a
20
separate pilot, or is it just incorporated into the flare boom? '
21
MR. KELLER: It's incorporated into the
22
flare boom. \ve do have
we did have --- or I should say wa de
23
have igniters on the flares that are a --- also serve as a pilot,
24
but they've never b~en satisfactory and are now disconnected on
25
the platform.
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Page 29
3
HR. GILBRETH: That's all I have.
MR. BURRELL: Hr. Marshall?
MR. MARS HALL: Are your igniters ,electrical
1
(
2
4 igniters?
5
MR. KELLER: Like I say, they're not in
6 operation now. Thsy ware, yes. They mix gas and air together
7 and a spark ignites the flame front which goes up a separate
8 pipe and ignites th9 flare.
9
MR.HARSHALL: Is the igniter at the burner
10 tip of the flare?
11
MR. KELLER: Yes.
12
MR. MARSHALL: Do you have any wind baffling
'(
13
arrangaments around your flares?
14
MR. KELLER: Yes, sir, we do.
15
MR. HARSHALL: Would you describe that
16
briefly?
17
MR. KELLER: Oh, it's a --- it amounts to a
18
shield.
19
MR. MARSHALL: On the off platform side of
20
the ---
21
MR. KELLER: Yes.
22
MR. MARSHALL:
flare? It's just a flat
(
23
shield, is it, or does it surround the entire flare?
24
,MR. ~~RSHALL: Yes. It's just a metal shield.
25
We have
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HR. MARS HALL: Is it tubular, or is ". flat?
J.~
MR. KELLER: I'm not surs.
MR. MARSHALL: ~'Jell , both the witnesses this
2
3
4
morning have mentioned the wind problem and ths weather problem,
5
and I really hav'~n 't h'eard anything much about the dssign which
6
could possibly b9 made to minimize the flar~ because of the
7
weather situation.
8
MR. KELLER: We have yet to find any dasign
9
that will allo,.¡ us to protect the flare. ~'Je also 'have a problem
10
kgeping the flare small.
11
MR. MARSHALL: You still have a wind deflecto=
12
on your flare now; apparently it has some value?
13
MR. KELLER: It has some value. We may ---
14
, actually it --- ac~ually it would flare more if it weren't for
15
the baffling.
16
MR. MARSHALL: Thank you.
MR. BURRELL: Mr. Barber, I have a coupl'e
I'm sorry, !-1r. Keller. Haybe if I --- Mr.
17
18
of questions here.
19
Keller, I have a coupls of questions. ~fu,endid you put two
flares on? Did you start out with two flare booms on that, or
20
21
was the second flare boom installed at a later date?
22
,MR. KELLER: The second flare boom was
23
installed at a later date after we ~dded mors compression
24
equipment. They we:r;:s on when I was' trans f,erred up here; I don I t I
25
know exact dates.
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Pag,a 31
1
HR. BURRELL: Initially there was on'e flar-e
(
2
on,th3 beom on th~ pla~form, or I should say one pilot boom,
3 whatav,er on the plat.form, and then ther~ ''las another ons a.dded
4 later a~ som~ subsequ9nt date.
5
MR. KELLER: Yes.
6
MR. BURRELL: \~= 1 re talking a.bout a sub-
7 stantial diffsrence here, and it bothsrs me. Mr. Barber testified
8
that the Dolly Varden platform was producing 45 mcf of gas per
9
day; you testified that the Grayling platform is producing
10
just slightly oyer --- just over 55 mef per day; yet you want
11
twic'e the flare. Why --.... I don I t --- why can I t you run that
12 through ona flare boom at a higher rate, answer that?
(
13
MR. KELLER: Wall, all I can say is that we
14 . are responsible for the safety of our peopl,a on the platforms
15 and
16
~lR. BURRELL: So is Hr. Barber on his pIa t- ,
17
form. Are you insinuating he I s lesssaf:e?
18
MR. KELLER: No, sir. I just feel that ~--
19
this is what we feel is nesdedto he safe on the platform at
20
this tim'8.
21
MR. BURRELL: Can you give me any r'sason why
22
the diff,erenc,e in what each of you fs,sl is· nec·eSSê.ry to bs saf:a?
(
23
MR. KELLER: One of the things we do have
24
ar's compressors spread out over a greabsr distance.
Like I say 'I
Thsy're
25
w'enow have nine compressors, and we will have ten.
~1
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Page 32
1 spread out over a larger area of tha platform. This may ba ana
2
r'sason for it.
3
MR. BURRELL: But couldn't ---
4
MR. KELLER: To ke~p the flares closer to
5
the compressors ---
6
MR. BURRELL: --- that all ba gath'arad
7
together?
8
MR. KELLER: --- where each flara is closer
9
to the compr9ssors where thay're operating.
10
MR. BURRELL: But couldn't that all be
gathered in one boom?
MR. KELLER: It could be.
MR. BURRELL: Well, we. really would like to
11
12
13
14
know why the second boom is being used?
15
MR. KELLER: Well, all I can say is that
16
this is what we fe'el is safe.
17
MR. BURRELL: Well, of course it'd be safer,'
18
I suppose, if you had two more booms.
19
MR. KEELER: I ---
20
MR.' BURRELL: I'm unable to find a rsason
21
why you set your boom --- why a slight difference in gas pro-
22
duction, about a twenty per cent diffarence in gas production,
23
why you need twice the flare? Could you help me on that?
MR. KELLER: Only,the fact that there are two'
24
25
flares in approximately the same location.
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1
MR. BURRELL: Well, but if thare wera four
2
flares, then you'd w~nt four million a day?
3
MR. KELLER: Probably ha.ve to have four to
4
maintain the flares.
5
MR. BURRELL: What about six flaras, six
6
million a day?
7
HR. KELLER: But we fael that two is
8
adequate for safety.
9
MR. BURRELL: But how come one is adequate
10
for safety on 45 million dubic feet of gas?
11
MR. KELLER: I can It answer that. This is
12
an ---
13
MR. BURRELL: Why can't you answer that?
14
MR. KELLER: --- engine~ring difference in
15
philosophy, I suppose.
16
MR. BURRELL: I can't answer it sither.
17
Mr. Gilbreth?
18
MR. GILBRETH: Mr. Keller, could you giva
19
me again the figure that you gave as an instantaneous discharga
rate in the event of emsrgency?
MR. KELLER: We calculate 110,000 mcf per
22
day, approximately 'two and a half s,econds after a total shutdown.
23
MR. GILBRETH: The piping on your platform,
is it such that the flare volume could be maasured?
MR. KELLER: Not dir~ctly. It's obtained
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Page 34
1
by differenca. ~v'e have a total of our produced gas, a total
of what we: send to shore, what our fuel requirements are, and
th·8 differ~nce is what we flare.
2
3
4
MR. GILBRETH: In other words, it'd ba just
5 the estimated diff~rence?
6
MR. KELLER: Yes, the calculated diffêr€nc~.
7
MR. GILBRETH: Is there anything in the
8
design of the flare boom i tselftha.t would make a differenc9 Sè~Y
9
between your platform and any of the other platforms on the
10
vOlum'ê of gas that. might be needÐd?
11
MR. KELLER: I don't know how all the,rest
12
of the flares are designed., I expect that most of them are very
13 similar.
14
MR. GILBRETH: Just for t.he racord, could yo~
15 give us an idea of the length and the diameter of your 'flare
16 boom?
17
MR. KELLER: There are two eight inch
18
relief lines in each flare, and thaflaras are approximately
19
a. hundred fe!et long; they may be somewhat. shorter.
20
MR. GILBRETH: All right, that's all Ih~vs,
21
thank you.
22
MR. BURRELL: Hell, I have another one. Nr.
23
Keller, ~.¡hat would you think a.bout a monthly av·eraga? If one
24
million per flare which you1va requestad per day is the worst
25
condi tions, compressors down, th,e wind blowing the 'Vlrong dirsctio::1,
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1 everything ---
f
4
MR. KELLER: Yes.
MR. BURRELL: going to ble.zas , right?
HR. KELLER: Right.
HR. BURRELL: ~vha t do you think about a
2
3
5
6 monthly averags? Something l,ess than th2.t, does that sound
7 r'easonabl,e? Just philosophically speaking, \..¡ithout naming
8 numbers right now?
9
MR. KELLER: v-rell, I feel that safely wa ca.n
10 live with a thousand a day avsrage for the month and possibly
11 less.
12
r·1R. DURRELL: H;ell, that's worst conditions
'(
13
t.hat ---
14
MR. KELLER: That's worst conditions.
15
MR. BURRELL: --- that you've found, that's
16 worst conditions?
17
MR. KELLER: Right.
18
t-1H. BURRELL: So you know you can live with
19
less unless things go wrong, right?
20
21
MR. KELLER: Correct.
MR. BURRELL: Okay. lih at would you think
about a trial period to see what the actual performancs is?
22
<.
23
MR. IELLER: I think this\..¡ould be ---
24
MR. BURRELL: With an emergency escape clause,
25
you understand, of course.
~1
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22
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Page 36
1
MR. KELLER: Yes. I think this comes under
it.
2
MR. BURRELL: In casa something goes wrong,
3 you understand that. We don!t want to endanger ~nybody's lif~
4
at all, but I'm un~ble to grasp mentally why you nged ~wice the
5
flare for twenty par cent more gas.
6
MR. ANDERSON: Mr. Chairman?
MR. BURRELL: Yes, sir.
MR. ANDERSON: For ths sake of tim9, may we
7
8
9
go on to the Honopod platform?
MR. BURRELL: Certainly, if everybody's
through aSking qU'~stions.
MR. ANDERSON: Excuse me.
MR. BURRELL: Mr. Marshall, do you have
anymore? Hr. Gilbreth? Okay. Excuse m'e, 1-1r'.Andsrson, would
you like thesa exhibits to be introduced for the Grayling?
l'-1R. ANDERSON: Yes, at this time I'd like
to ask Mr. Keller on Grayling ,Exhibit A, was that prepared by
you or under your supervision?
MR.KELLER: Yes, under my direction.
MR. ANDERSON: We ask that it ba entered
into the record.
~lR. BURRELL: Ne'll accept the eight by
t~n copy as Grayling Exhibit A.
MR. ANDERSON: Grayling Exhibit A, all
right. Mr. Chairman, we broke at ten yestarday¡ would the
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1
Committee entertain a coffee break at this time. Just a sUggastirn.
MR. BURRELL: Good idea. Weill take a fifteen
2
3 minute br·eak.
4 (OFF THE RECORD)
5 (ON THE RECORD)
6
MR. BURRELL: Walll reconvene the hearing
7 now. Mr. Kellar.
8
MR. KELLER: My name is Richard Keller, and
9
I am Area Enginaer for Union oil Company, Anchorage ,District,
10
Alaska.
11
MR. BURRELL: Excuse me, Mr. Keller, can I
12
interrupt~ Welve all been guilty of this I hear from the back
of the room, if we could speak a little louder. Some of th~
13
14
people in the back at least say that it seems as though we're
15
talking to each other, so I for one shall make an effort to
16
speak a little louder. ,Maybe if we all could do that, it'd be
17
helpful. Thank you.
18
MR. KELLER: My purpose here today is to
19
de;scribe the gas processing system and the need for safety pilots
20
and to recommend safety pilot sizes for the Monopodplatform.
21
I have testified previously a.s·to why sàfety'pilbts are
22
required on, Cook Inlet platforms and will now discuss only the
23
Monopod. I wish to have my previous general comrnents regarding
24
ths Grayling platform incorporated into this testimony.
25
MR. BURRELL: They are so-incorporated.
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1
MR. KELLER:
(Mr. Keller's testimony is
2
attached as an exhibit to this transcript.)
3
MR. BURRELL: Thank you, Mr. Keller. Mr.
4 Gilbreth?
5
MR. GILBRETH: Mr. Keller, in your Exhibit A
6 you show eight inch flare lines and ten inch flare lines. Are
7 these the sizes of the booms themselves, or are thsse just the
8 platform pilot lights?
9
MR. KELLER: Those are the size of the flares
10 themsel vas.
11
HR. GILBRETH: They are. Her,e ag ain, i s th:~
12 piping such that' the gas VOlUffi8 can be m::~asured going to t.h'9
13
14
flars boom?
MR. KELLER: No, sir. It's obtained by
15 differenc:e of our sUImning up our total produc,ed gas' and sub-
16 tracting the gas we use fot f~el and ship to shore.
18
17 MR. GILBRETH: In your schematic here, where
would the pilot gas
what would be the source of pilot gas
20
19 . for the flare booms?
21
22
23
24
25
~1
MR. KELLER: The --- on the upper flare that
you see, the pi~ot gas is obtained from the lower eight inch
flare lin·s.
MR. GILBRETH: I know, but ---
MR. KELLER: ,And the lower ---
t-1R . GILBRETH: --- trying to· trace the flow
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(
1 back from that point.
2
MR. KELLER: Yaah, it's obtainad off of the
3 main header m~nifold there where you see the old pre-comprsssor
4 scrubbsr just to ths right there of the --- that's the on9, just
5 to the right of the separators. The other ons's obtainêd off the
6
number one gross separator. That maintains the oth'ar flare.
7
l-lR. GILBRETH : There 's nowhere in your whole
system then for provision for metering of the let's cali it
8
9
pilot gas?
10
MR. KELLE R : No, there isn't.
HR. GILBRETH: Could it be incorpora t·ed?
MR. KELLER: I don't believe it could he
11
12
13
safely incorporatèd. The purpose of the relief lins is to ---
14
a minimum of back pressure, in fact no back pressure to speak
15
of, and installing a meter in the line would form a back prassure
16
under discharge conditions.
MR. GILBRETH: I can understand that so far
17
18
as the safety phase is. concerned for relief purposes, but what
19
about the' --- just the piloted fire, that's what I'm referring
20
to?
21
MR. KELLER: It is possible, I believe, that
22
that probably could be used.
23
MR. GILBRETH: I --- the thought occurrad to
24
me, consideririg your ear¡ier testimony, nobody really seems to
25
know what these things require. I'm just· wondering if it'd be
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1 possible to rig up any sort of a test hook-up through axisting
(
2
aquipment that it ,could b~ measured against somehow?
3
MR. KELLER: There's a problem that it's
4 vary, very low pressure gas which is extremely difficult to
5 msasure. It does vary greatly, and orifice meters, to my
6 knowledge, ,ha~e approximately a five to one ratio of being able
7 to measure gas in that particular line. I don't believe that I
8
would recommend it, simply because of this problam of when we havs
9
to have an instantaneous release, we can't live with a mater in
10
that line.
, 11
MR. GILBRETH: Well, I realize that. But
12
apparently you have some restriction of the line right now going
'(
13
to the pilot ---
14
MR. KELLER: The control valve.
15
MR. GILBRETH: --- or will have to control
16
the pilot itself.
17
MR. KELLER: A control valve, yes, which
18
is a pull open tYP8 valve.
19
MR. GILBRETH: And I'm talking about mebering
20
upstream ,of that control valve.
21
MR. KELLER: Well, this becomes a problem,
22
you put a restriction then ahead of the control valve, and it
(
23
would be the same thing as putting a meter downstrleam of the
24
control valve,: either place would present a back pressure
25 '
condition where you want to instantaneously release this in an
~1
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1 emergency. I know of no way that we could safely ---
2
MR. GILBRETH: I'm not understanding your
3 testimony at all then. I understood that the one million a day
4
was to provids for all necessary contingencies and the pilot
5
light.
6
MR. KELLER: That's correct.
7
MR. GILBRETH: Now, if you wers metering
8
one million a day through there, why would this restrict your
9
flow for safety ,purposes then?
10
MR. KELLER: Because this is ths. SaID·9 lin~9
that a 'release, when it occurs, if we have a shutdown, the prsssurz
12
in that line is r9leased through that valve.
13
M~. GILBRETH: ~lliat happens to your control
14
valve? Does ---
15
MR. KELLER: It opens up. The control valve
16
then opens up and releases the gas until the pressure goes down,
17
so this is the line
one of the lines that relieves.
18
MR. GILBRETH: Under the worst conditions,
19
as I understand your t·sstimony, you think that you'd need a
20
million a day. What is your best ,estimate at this time under
21
ideal conditions that you'd need? Is it still a million a day
22
or half a million?
23
MR. KELLER: Something less than a million,
24
¥'es.
25
MR. GILBRETH: You just don't have any idea
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1 how much less?
2
MR. KELLER: On the M~nopod platform, waive
:3
been, una.ble t.o draw the fl2.r::s dO\Vl1, sae i we haV3 to base our
4
expsrienc= ~n the Gr~yling at this tim2 until W9 gat our sys~2m
5
opera~icnal. 1~9 can only estimate from what we're using on tha
6
Grayling.
7
~m.GILBRETH: The --- your testimony here
8
for th~ Honopod ~nd also for tha Grayling is that. the pilot gas
9
goes do\~ the lin~ ~nd you just kaep the flare boom lit at all
10
tims;s?
11
MR. KELLER: Yss, sir.
12
HR. GILBRETH: Is it feasible to install a
13
separate pilot line?"
14
a
MR. KELLER: We have installed/separate
15
pilot line: we haven't had ,good experience with it. That's our
16
main problem.
17
~ffi. GILBRETH: I see. What problems have
18
you had with thase?
19
MR. KELLER: Well, I don't know if it's a
20
combination of 'the ,extrema temperature differenc·es. The problem
21
ws have \~ith the flar:s on an angle like this, the wind --- the
22
flame itself is not right at the tip; the flame itself is usually
23
24
a foot, or two feet, or three fe,et away from the tip. ~vith the
wind blowing right back at it, you g~t -a problem with after a
25
psriod of time the burner· tip itself, regardless of what kind yo~
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1 put on, ands·up burning up. ~ve have replaced several tips on
2
tips on th~t pla~form,
the platform. We do have John Zink
3 but th9Y' just d8teriorate \.¡ith time a.nd you can't rely on thsm
4 to main'tain.
5
MR. GILBRETH: ~fuat is the length of your
6 flara booms hers?
7
MR. KELLER: Approximately a hundred feet.
8
I don't have the exact figure. I can get those figures for you
9
if you ne2d them.
10
MR. GILBRETH: That's all I have.
MR. BURRELL: Mr. Harshall?
MR. MARSHALL: You mentioned, Mr. Keller,
that the flar.e being at an ang l·e , flare boom being at è.n 2~ngle ,
11
12
13
14
the wind would cause blow back, burning up the flares. Havs you
15
experimented with putting in an elbow so that the flare stack
16
would be vertical at its tip?
17
MR. KELLER: We do have those on the Grayling.
18
I don't believe the Monopod ones are turned up at the end. It's
19
simply a matter of whichever way the thing is pointing, your,boom
20
itself is out on an angle, and the wind can blow it ahd has blown
21
it right back onto the flare stack, r~gardless of which direction
22
it points. We prefer to have the flare tip pointing away from
23
the platform; this just extends the distance from the platform
24
that the flar= i tsslf is actually lit. We pref·er to have the
25
flames direct9daway from the platform.
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MR. MARSHALL: Has it ever happensd YOU'V9
2
had any liquids flood through that system?
3
HR. KELLER: Not to my knowledge. Ha have
4
flar9 scrubbers that are shown on the diagram that scrub any
5
liquids that might get into that system. They are in turn
6
piped back into our oil shipping line to shore. So I don't
7
not to my knowledge we have never had any liquids go out the
8
flare.
9
MR. ~~RSHALL: All right. Now, on the
10
Honopod you've used the word a burner tip. Ar·e --- do you haV'B
11
some wind baffl·es or electrical igniter system out on the ---
12
in operation on the Monopod?
13
MR. KELLER: We have just install~d el9ctrical
14
igni tar type thing on th·e Honopod. ~ve do have wind shields.
15
MR. NARSHALL: Have --- you men.tioned th?..t
16
you've had som~ back luck with electrical igniters. Have you
17
ever used any catalytic igniters, platinum catalytic igniters?
18
MR. KELLER: Not to my knowledge. The type
19
we have had is a sparkpl,ug type arrangement. Gas and air are
mixed together, and the spark is ignited and goes up.
20
21
MR. MARSHALL: Well, I'd just like to ask
22
one more question about the shape of the discharge vent there.
23
It I s pointed outward to proj act the flame away from tiH~ platform,
24
and I certainly understand that. Do you
do you think there's
25
a compromise batween maybe the length of the boom and the final
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1 direction of ·the flame? In other words, if the boom wars long~r,
I
2
could th~r9 not be a tip angl= such that it's burning in a
3 vertical 'position?
4
MR. KELLER: Well, you reach a limit of
5 the structural stabili~y of the flare boom, for one thing. Just
6 so long until the pipe you can project out and saf,ely hold it
7
up thsreonto the platform. I think we have designed the maximum
8
distc:nce \'le can --- that W8 can on our f laras to ke.ep th,~m as
9
far away as w: can from the facility.
10
HR. . HARSHALL: P,e.rhaps th,ers could b'9 a
11
compromise hatwssn a slight angLe from vertical of the burnar
12
tip and a vertical
flame. Have ybu ever done any expsri-
13
menting tlli th this?
14
MR. KELLER: I believe just about all our
15
tips do. Nhere the pipe com,es out the tip is directed up s:ame-
16
what. This is to obtain better burning.
17
MR. l>'lARSHALL: That's all the questions I
18
19
have.
MR. BURRELL: Mr. Kellar, ~.¡hat' s the --- I
20
have a little different approach. ~'Jhat' s the oil p~o,duction,
21
the daily oil production, of the Honopoà?
HR. KELLER: Approximataly 15,000 barrels
22
23
24
p9r day.
MR. BURRELL: 15,000. v'7hat' s the gas pro-
25
duction?
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10
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12
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18
19
20
21
22
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25
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MR. KELLER: Gas --- solution gas production
is approximately 15,000.
MR. BURRELL: Okay, th~tls what I wanted to
know. Okay. Two booms ~nd two flares?
MR. KELLER: Yss, sir.
MR. BURRELL: Were they both installed
initially, or was one added 1atar, or do you know?
MR. KELLER: No, we had one flare originally,
and ---
13
MR. BURRELL: And you addsd on,s later?
MR. KELLER: --- we added onl8 later ---
MR. BURRELL: I sea.
MR. KELLER: --- when we had morè gas
14 'production then.
15
MR. BURRELL: Do you knew why
MR. KELLER: And pressur2.
t.1R . BURRELL: '+. wa.s added later?
~...
MR. KELLER: Yes, ..... was to dissipate the
~J.-
16
heat. We
I'm sorry I don't have a diagram of the Monopod
platform, but there are two pipe racks on the platform for the
drilling operation, and the pipe racks, the surface of them
consisted of wood that was treated and not supposed to burn or
anything, and we had instanc9 where the wood actually caught
fire on one of these cases where it was shut down with our
existing compressor setup which doesn't handle the gas used on
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1 th~ new compr9ssors will, and it actually caught this wood on
2
fire so we --- this was one of the prime rsasons for adding tha
3
second flare boom, and we'v~ since put sts:l decks on our pipe
4
racks to pr:vent this from recurring.
5
MR. BURRELL: Was your fire a result of an
6
instantaneous discharge situation?
7
HR. KELLER: Yes. I believe it was a shutdown
8
condition with our existing compressors.
9
MR.BURRELL: Could that be solved by changing
10
the location of the flare boom?
11
MR. KELLER: Well, this is what wa did. Wß
12
put one on the northwest cornar and one on the south; this is
13
where they are located, on opposit~ sides of tha platform. The
14
ona on the northwest is directed the furth~rest away from ,either
15
of the pips racks and the living qUê.rt,ers.
16
MR. BURRELL: Why could not all the gas be
17
directed through that one flare boom?
18
MR. KELLER: Number one, it would take a
19
total redesign of our safety relief systems. All of our separators
are on the production deck on the opposite side of the platfoIill,
20
21
and this is where part of the gas goes, and even that flara is
extremely hot undar,normal conditions, and under shutdown con-
ditions it's to us unacceptable for just one flare.
22
23
24
MR. BURRELL: No doubt, as long as gas is
25
being directed to it, it would be extremely hot; I'll buy that.
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1 But why couldn't --- other than the design problems, is there
(
2
any reason why it couldn't be run through the north boom?
3
MR. KELLER: No, we just feel that it's safsr
4 the way we have it.
5
MR. BURRELL: Your---you've got 15,000
6 cubic fset, and you want to flare a million max. total?
7
MR. KELLER: That's right.
8
MR. BURRELL: Dolly Varden's got three times
9
as much gas they're producing, and they want to flare half as
10
much; can you explain that?
.
11
(
MR. KELLER: Well, like I say, one of the big
,12 considerations is this shutdown condition where we have ---
13
MR. BURRELL: They have a shutdown condition
14
too, don't they?
15
MR. KELLER: Yes, Yies, sir, I ---yes.
~lR. BURRELL: And th'ey , rs designed for ;..\-
-'.....
MR. KELLER: Yes, ,and W9 feel we'rs designed
16
17
18
for it. We have --- with this new system operating, like I say,
19
we'V:9 had no expe:rienc9 with it yet to really --- w'e feel that
20
this amount of gas will he sufficient, but our instantaneous
21
22
discharge rate is almost twice that of the Grayling and the
Dolly Vard,en. This is the design of the compressor; they're
(
23
bigqar, holdrrore gas at pressure.
24
HR. BURRELL: Are you sa.ying the reason th'8n
25 '
for --- the basi6 rsason perhaps for assassingthat the larger
~1
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1 ,flares and l~rger flared volum~ is the design of tha compr~ssors?
(
2
~m. KELLER: Not the design of the compressors
3 per see ,It's just the entire system all t~gethar, we feel for
4 saf9ty reasons that \Ve ne'ed the two.
5
MR. BURRELL: I'd I ik,e t.o know why. Wha t
6 is the differenc~ batween the two systems that nscessitatês this
7 increas,ed volumre?
8
~lR.KELLER: The engineering design of tha
9 total package, basically, is the reason we have more.
10
MR. BURRELL: Aria you saying there I s some-
11 thing wrong with the design?
12
MR. KELLER: No¡ sir, I'm not. This is jURt
(
13
a different design concept.¡ the way these two compressor sets
M 'are designed, if we have an electrical failure or fuel fail~re
15 or somsthing, all t.he system' there in tha t packa~ge bleed s down
16 at once.
17
18
MR. BURRELL: But isrlt. that true on th,e
other platforms such as the Dolly Varden?
MR. KELLER: Not to the extent that this
system is, and this is based on the dresign of these two com-
19
20
21
pressors the way they operate in this tandem condition where one
22
turbine drives two compressors and the way the module is built
(
23
of necas.sity has to be small to fit on the platform, but'.the
system has to be down to be safe.
24
25
t-1R. . BURRELL: Well, you see my problem, it's
~1
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1 difficult to explain why with one-third of the gas production,
2
you nesd twice the flare?
3 MR. KELLER: Basically it's the discharge
4 rat·e and to dissipate the heat. This is our reason for it.
5 MR~ BURRELL: Do you think it'd be rÐasonable
6
,to,have some kind of a trial period here, an actual historical
7
performance period to find out what is require before a final
8
order on this matter?
9
MR. KELLER: I think particularly in the
case of the Monopod it vrerywell could be.
10
11
MR. BURRELL: Thank you v/~ry much, Hr.
12
KelleJ;. Anymore questions?' Thank you, sir.
13
MR. ANDERSON: Mr. Keller,
14
MR. BURRELL: You will be available later,
15
will you, sir? Excuse ms.
16
MR. KELLER: Yes, sir.
17
MR. ANDERSON: On your Monopod Exhibit A,
18
was that prepared under your direction?
19
MR. KELLER: Yes, sir.
20
MR. ANDERSON: We I'dlike Honopod'..Exhibi t Þ.. to 1:
incorporated in ··the record.
21
22
,MR. BURRELL: ~œ' 11 enter into ,evidence Hono-
23
pod Exhibit A.
24
MR. ANDERSON: Our next witness is Mr. B. C.
25
Anderson of Atlantic Richfiald Company. Mr. Anderson was qualifia<
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1 at y:estsrday I.S hearing by incorporation of his qualifications
2
pres2nted in Conserva.tion Order No. 83. He ask that they ba
3 accepted here.
4
MR. BURRELL: They are accepted.
5
MR. ANDERSON: As I pointed out earlier,
6'
Mr. Chairman, Mr. Anderson.wil1 be testifying on tha King Salmon
7
platform, HcArthur Riv,sr Field; after which h,e will then go to
8
the Platform A and Platform Spark in the Trading Bay Northeast
9
Pool.
10
MR. B. C. ANDERSON: Gentlsmen, I am B. C.
11
Anderson. I am the District Engineer for Atlantic Richfield
12
Companyls South Alaska District, headquartered hare in Anchorage.
13
Atlantic Richfield Company operates Platform King as a subopera-
14
tor in the Trading Be"y unit of HcArthur River Field. Exhibit
15
Ona shows th8 loca:tion of this platform in r,:elationto the other
16
platforms: in th9 field, th,e outline of ths field based on the
17
approximate productive limits, and the Trading Bay Onshore
18
production Facility.. We III have to find anoth:er way, I think, to
see the whole exhibit.
19
20
Platform King production comes fro11l ten wells with twelve
completions in the G, Wast Forelands and Hamlock Pools. Daily
21
22
production is 26,500 barrels of oil per day, 2200 barrels of
23
water per day, and 8500 mcf psr day of gas. A rotative gas lift
24
system provid9s 23,000 mcf per day of high pressure gas for
25
artificial lift purposes. ,Approximately 70,000 barrels per day
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1 of filtered and treated Cook Inlet watsr is injected in four
2
wells on the platform as a part of the field's water flood pro-
3 gram.
4 Platform King has two enclosed dsck lev;ls, maasuring
5 approximately 110 f~2t squ~re. Referring to Exhibit Two, equip-
6 'ment on the platform includes oil and gas saparation ~quipment.
7 I want to get these slides here so he can point these out.
8
(Pause) Excuse the delê.Y. Equipment on the platform includes
9
oil 'and gas separation equipment, two 2,125 horsepovver Horthing-
10
ton mainliner compressors, one 1100 horsepower Solar York centri-
11
fugal compressor, one 6,000 horsepower Nordberg turbine powered
12
water injection pump with related water filtering equipment and
13
deaeration tower, t\..¡o 1250 K~~ electric gt-2;ncrators powered by
14
~ Rustin turbines, t,.¡o 1500 KN generators driven by General r,lotors
15
diesels for rig power and standby, one 350 horsepower boiler,
and a variety of other related producing and drilling equipment.
16
17
Normal, manpO'~..¡er on the platform without rig operation is about
18
twenty-five people..
19
The flare system en PlatfofID King consists of three flare
lines: a twelve inch low pres~ure flare handles gas flashed from
the first stage suction scrubbers of the Worthington mainliner
20
21
22
compressors and oxygen enriched gas from the d~aeration tower.
23
The main flare system or high pressure flare system is a twenty-
24
four inch flare boom that handles gas relieved from the system
25 '
beb~een the oil and gas separators and the compressors. This
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1 system provides the primary relief in the event of a surge in
2
production, compressor shu~down, electric power failure, ar other
3 upset in'the facilities. A third twelve inch line ties into the
4 pressure relief valve and rupture ~iscs system throughout the
5 production facility. A John Zink cle2..n burning flare tip
6 ins~alled on the high and low pressure flares is designed so that
7 the burners on these ~wo flare systems are separated by several
8 feet at the end of the flare boom. Proper operation of these
9
clean burning flare tips requires the use of aspirator gas
10
equivalent to about thirty per cent of the total flared volume
11
at minimum safety pilot conditions.
12
(
As the description of the King platform and its equipment
13 indicates, pla.tforms in the Cook Inlet wat.ers are extremely
14 complex and rather unique in design. They are relatively small,
15 compact platforms and are heavily laden with equipm~nt. The
16 equipmßnt is quite reliable, but any equipment is subject to
17
18
19
20
21
22
(
23
24
25 I
~1
failure. Due to the climatic, conditions, platforms, in the
Inlet are almost fully enclosed. This is som,swhat different
from the normal open design for mos~ other offshore areas.
Extensive measures must be taken to prevent dangerous concen-
tr~tions of gas in enclosed platform areas to minimize the
accompanying risk of fire or explosion on a platform. The uniqua
conditions in the, Cook Inlet, also require that many systems
which are separat-ad where conditions permit are in this cass
all contain2d on a common platform. It is common practicß in
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1 other areas to have separation equipm9nt, comprsssors, and firsd
2
vessels separated. Safs~y features must be quite extensive to
3 protect lif9 and property in any offshors operations. Th9re are
4
obviously some special consid~rations for the Cook Inl~t type of
5
opera.tion.
,6
provisions must be mads for the safe release of gas when
7
thar9 ar~ surg~s in production \~hich cannot be otherwise handled
8
or when there are shutdowns dus to machanical or elsctrical
9
failuras. Production surg~s are especially common in gas ,lift
10
operations. The special considera.tions discuSS3d make it neces-
11
sary that all pressure release of gaseous vapors be gathered and I
12
carried to a rsmote flare forccmplete combustion in order to
13
protact th9 platform, its occup2.nts and equipm~nt. Th~ minimum
14
safety pilot volume is undoubt~dly r~latsd to many factors,
15
including but not 1imi t,s.d t.O 'equipm~nt compl:exi ty, total syst::=m
16
d~sign, system volumes, and flo~.g rates handled; how'9v~r, thara is
17
nO,prscedant or gsnerally accepted engineering procedur~ for
18
establishing a minimum safety pilot size for operations having
19
ths uniqu9 design and operating conditions of the Cook Inlet
20 '
pla~:.:forms. Tha minimum vo1U11lS must ensure tha.t a pilòt will ha
21
m~intained during variabl9 wind conditions and provida positive
22 ~
ignition of any suddsn release of gas caused by an upset or a
23
failure \vhich brings about an exc~ssiv? pressur':e in any system.
24
Our reconul1snd-ad minimum safety pilot size is bas,ad on tha
25
judgment of exp=.rienced op'erating personnel who are thoroughly
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1 familiar wit4 the daily op~raticns of this platform. It also
2
gives full consideration to the naed for minimum flara volumss
3 from pl~~forms in th~ Inlet under Existing Conservation Corr~ittêe
4 Orders. On this basis W~ r~commend a safety pilot volume for
5 King platform of 800 rncf,per day on a monthly average ba.sis.
6 Exhibit #3 shows a sch~matic drawing --- (pausa) ---
7 Exhibit # 3 shows a schematic dra.wing of Platform King IS facili ti,es
8 with gas volumes for òparation under minimum safety pilot con-
9
ditions. Under these operating conditions, 31,94.0 mef par day
10
of gas is flashed from the oil and gas separators. This ,velum::&.
11
includes gas lift gas, solution gas, flash of liquids from all
12
scrubbers throughout the system operating at a higher pressure,
13
and flashed gas from the crud!s surg'e tank. Gas from the crud:~
14
surge tank is not n'ow being comprsssed and put back into the
15
Inlet gas stream, but we plan to convert an existing compressor
16
on the platform to this service.' The minimum safety pilot
17
vol~~e of 800 mcf par 'day is shown on this diagram. The remaining
18
produc;~d gas from the separators, tota.lling 31,140 mcf per day,
is delivered to the suction of the compressors. 7,140 mcf per
19
20
da~t'. of this gas goes to the Solar York booster compr·essor which
21
discharges at about 300 psig. 3500 mcf per day of the gas from
22
the booster compressors goes to the fuel systam. This includes
23
gas used, for the Rustin turbine powered g:enerators, the Nordberg
24
turbine which drives the water ~njection pump, the Solar turbine
powered compressor, the steam generation ,equipm'ent, boilers,
25
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filter flàsh; and de aeration for removal of oxygen from injèctad'
2
water. Fuel for the Worthington compressors is being suppliad by
3
gas ''lell gas due to detona.tion and maintenance problems that have
4
been experienced with casinghead gas fU9l. We ars currently
5
working with Worthington representatives in an effort to modify
6
the Worthington. fuel system so that these compr'essors will also
7
operate satisfactorily from the casinghead gas fuel system. The
8
remaining 3,640 mcf per day of gas discharg<ad from the Solar York
9
compressor will bE delivered to shore to be pròcessed by th;e
Trading Bay Production FAcility Liquid Extraction Plant and
10
11
subs,equently compressed for delivery to the gas pipeline now
12
being constructed by Union and Marathon.
13
Referring back to the compressor suctions on Exhibit #3,
14
24,000'mcf per day of gas from th~primary separators is dalivsred
15
to the two Worthington mainlin,er compressors .T,hese compressors
16
sarve the rotativa gas lift system. The suctfon volume is
17
reduced by 1200 mcf per day due to shrinkage from condansation
18
in the compression process~ The remaining 22,800 mef per day of
19
gas discharged from these compressors is returned to the gas lift
20
system.
21
22
In summary, I ~ave discussed the highly complex, compact
and enclosed conditions that make Cook Inlet platforms unique.
23
24
Although the equipment onboard King platform is capabla of theor-
'a tic ally handling all produced casinghead gas without a flare,
25
ths unique nature of the platform makes it essential that a
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1 saf,ety pilot bs mainta.ined for safe operations. To provide this
2
safety the pilot must ensure positive ignition of any sudd~n
3 rel-aass of gas to th~ flare system. ~\19 found no precsdent or
4
commonly accepted engineering pr=.ctic'B for calculating a minimum
5
safðty pilot size for the unique Cook Inlet type of operation.
6
Our recommend~d minimum saf~ty pilot size is a balance of the
7
judgm~nt of our operating personnel who are most familiar with
8
the platform and the recognized necessity for minimum flare
9
volumes for platforms in the Cook Inlet undar sx~sting Conser-
10
vation CCl1'lmit'tsa orders. Atlantic Richfield Company respectfully
11
requ3sts the assignment of a safety pilot volurne of 800 mef per
12
d~y en an avaragz monthly basis for ths King Sêlmon platform.
13
Th5.t concludss my direct bestimony. Thank you for your 3..tt.snt.icn.
14
~lR. BURRELL: Thank you, ~·lr. And'8rson. 1iJ~ 'II
15
ask you about this platform before. you go on to th'e oth'èrs you' r'2
16
speaking to. Mr. Gilbreth?
17
HR. GILBRETH: Hr. Andsrson, referring to
18
your Exhibit #3, the safety pilot strength of 800 mcf per day,
19
I notice you also have a low pressure flare there ,showing 500
20
mef psr day. Is that a continuous flare?
21
HR. B. C. ANDERSON: Yes, sir. That is gas
22
that has b:e~en used ~n ths deaeration process. I '11 be glad to
23
go into th~ deaa~ation process for you and discuss that in soma
24
'detail if you'd like.
25
MR. GILBRETH: Well, my question is this:
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1 are we r2ally talking about 800 or 1,300,000?
2
MR. B. C. ANDERSON: Well, our --- our fêelin~
(
3
here was that the gas that is handled in the deasration proc3ss
4 --- 1st me start by explaining how this process works because
5 that'll give mora people a feel forth~ system. But this d2asra-
6 tion process is for the removal of oxygen from the water that will
7 be injected into ths formation. The water Is taken from the Cook
8 Inlet which has a high oxygen content. We mus,t remove the
9 oxygen for two reasons·: one, it is very carrasi va; and sé9;condly,
10 it causes the gro\vth of bactaria which will plug the surface
11 equipm~nt as well as the wells downhole. So we use gas through
12 this tow',er. tvat;sr is introduced, at the top of tha tow:;;r, runs
(
13
down through trays, and thesa trays have bubble caps in thsm to
14 ,let the gas bubble, up through the water and strips the oxygen
15 out. Any oxygen that is left in the water has_to then be removed
16 by an oxygen scavaging chemical, so ws get it essentially oxyg.en
17 free,. So w:a have looked at it like this: we fe,el that the
18 gas used in the deaeration process is a used gas; it does go
19 through our fuel meter; it has been our practice and wa feel that
"'20 --- felt that ìt was appropriàt.e that this gas he shown as a fuel
21
since it is used gas, rathert.han a flare. We purposaly showed
22
it on this diagram to bring it to your attention in case you
23
should feel otherwise. Our legal people told us that they felt
that under their interpretation that the gas was used and should
(
24
25
be called a fuel. So we have handled it in this manner.' If the
~1
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1 Cornmittes feels otherwis~, than our total flare voluma would b9
2
1300 mcf per day.
3
MR. GILBRETH: Now, did I un~srstand your
4 testimony to indicate that the point in which this flaring occurred
5 is two different places, a few feet apart?
6
MR~ B. C. ANDERSON: That's correct. I have
7 a slide, a back up slide if you'd like to sae it, that shows
8 the John Zink clean,burninç(,flare tip, and the tips of those
9
two burners there, thosa two flares, are separated in the John
10
zink design by a distance ,of about six feet.
11
MR. GILBRETH: On the low 'pressure flare,
12
the one with the 500 mcf a day, that's all that will ever com-=
13
through that side of it, is it not?
14
MR. B. C. ANDERSON: That's correct. That
15
is a continuous volume that will he going through there at all
16
timas that the dsaeration t,ow,ar is in operation. I bslieve that
17
I also said --- I think thare's some gas back on the previous
diagram that's flashed off of the first stage' suction sc,rubbers
18
19
on 'the compressors,. This is a very small volume of liquid t.hat 's
20
caught in thoss, and is essentially zero, so the voluma thers is
21
the 500 from the deaeration tower.
22
MR. GILBRETH: Then the 500 is essentially
23
ind~pendent of emergency type operations; it would be going on
24
continuously?
25 '
MR. B. C. ANDERSON: That is correct.
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MR. GILBRETH: Is it possible to utiliz9
2
this 500 to h~lp kaep the pilot going on the em9rg~ncy flares?
3
MR. B. C. ANDERSON: The problem that we
4 encounter there is that of course they Ire not in the same
5 loc~tion which crsates some problem, and ths reason they're net
6 is ths design for the smokel~ss flare burning there, so this
11
7
creates a probl,em. If you were to p~t the two --- by some change
in design if they could be put together where they burned in ons
8
9
common spot, then you'd still have a problem there that part of
10
your safety pilot is Qf course to ignite the gas that might cerne
11
out un~er a real shutdown op:eration, but as I pointad out in my
12
dirct~ct testimony" you also have --- in õi gas lift typa op~ration
13
which' I'm sura you're already farniliar with, you have surges as
14
Your 'equipm:ent is 8i tting therE? running
,the gas com~s back.
~I+
......-
15
a set condition and handl:2s gas at a rathar constant voluma,
16
your compr'.essionequipment, so when these surges come, back from
17
the Úells, you have to have som,sthing to allow these variations
18
in gas to go out, and I think that if you combined thas$ volumss~
19
you'd certainly have too little to take care of that type surge.
20
So } really don't fe,el personally that it is praè~icål to combins
21
the two.
22
MR. GILBRETH: If we could go back to your
23
Exhibit #2 for just a moment.
24
MR. B. C. ANDERSON: All right, sir.
25
MR. GILBRETH: You show in the upper lefthand
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1 corner of Exhibit #2 relief flare, and thsn ~ high prsssure
2
flare, and a low pr3ssur~ flare too.
3
MR. B. C. ANDERSON: Yss.
4
MR. GILBRETH: Do these actually repres3nt
5 thre9 separate flares I or is it jus,t the connection t.hat migh't go
6 into one flare boom?,
7
MR. B. C. &~DERSON: No, these actually go
8
all the way from the base of the boom to the top æ s,eparata lin~s.
9
The relief flare is ,a separate line and ties only into our
10
relief and rupture disc systems; this ensures us that there is
11
no back prsssure on that line due to any of the surges coming
12
out. And the high pr9ssure flare" I'd have to look back at my
13
,testimony to make sure I don't confuse you and me both, but the
14
high pressure flare is the large boom; it's a twsnty-four inch
15
in di2.ro~t3r boom, and then it COffi:SS up to the end and goes throug~l
16
the John Zink ~ burner, and then the other line runs up by the
17
side of it, the other t,,,o lin'as. The twenty-four inch lin'&; is
18
actually --- it' ssvedgi3d do\.¡n to a smaller line when it comes to
th'S burning end, and it provid,es both a minimum back pressure on
that flare system as well as the structural strength t.hat's
19
20
21
necessary for the flare to be maintained at its angle.
22
MR. GILBRETH: Well, basically do you have
23
just the one flara boom or
24
MR. B. C. ANDERSON: That's correct. They
25
just run out on,e line and th:ey end at a common place.
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MR. GILBRETH: What aboùt your pilot thsra,
2
do you have a separat= pilot, or do you just burn from th~ main
3 lins?
4
MR. B. C. ANDERSON: No, there's no pilot
5 as such, insofar as a ling going out to provide pilot gas. The
6
pilot is actually gas that should b= burning continuously off of
7
the flare system, and it's th= low --- it's the low burner
8
pesi tion, if you please, and then \.¡h:en the surges corne, that
9
same fl2.m,~ vlill bE: ~nlarged to handle the larg,e volUI1l'a.
MR. GILBRETH: What is the source of the
11
pilotgas; is it from the high pressure flare or th,e low pr¡=ssure
12
fla.re?
13
MR. B. C. ANDERSON: It would be from the
14
high pressure flare. as shewn on our other diagram b2Ck on #3
15
hers.
16
MR. GILBRETH: Okay.
17
HR. B. C. ANDERSON: The 800 mef, sge, comas
out of the high pressur,e flare, see, the lette~ring' righ t helo\.,
19
tha 800 mef.
20
HR. GILBRETH: Oh, I see, yes.
21
HR. B. C. ANDERSON: And the low pressure
22
handles the dsaeration gas.
23
MR. GILBRETH: Within this high pressure flar:?;
24
ralisf line or the high pressure flare lin'9 here, is there any
25
measurement made of the volum~ that goes through?
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MR. B. C. ANDERSON: No, sir, th~re is not
2
a direct m~asurement¡ it is done by a gas balance¡ th~re is no
3
mgasurem~n~, no orifice m9ter or anything of ~hat type on tha
4
line becausa of th~ restric~ion that it would cause, and I might
5 elaborate a little on that. There's been soma discussion of
6
that in other. testimony. If Wß were to put a restriction in th-e
7
line and sst it so that it could mgasur,e the pilot flara volUJ."1ls,
8
th~n the orifice plats size opening would be pretty small and
9
of courS9 it wouldn~t measur~ th~ large ,flàre volume, 'you just
10
couldn't have th~ rang9¡ plus a small size to handle the pilot
11
volume to IDaasur,e it would represent quite a restriction in tha
12
ovarall line.
13
MR. GILBRETH: Your design is such 'th3.t onC8
14
you get the remsrg;ency condition, 'svsrything is thrown \vid.e opan
15
to the flare, is that right?
16
NR. B. C. ANDERSON : That's corr'sct:. '~'¡h :~n
17
an emèrgency condition comes, it just pops right:, to thr8 flare.'
18
Of courS9 it d09S have a valve on the c0ntrol lins; it senses
19
on tha prassure; it dOBsn't just necessarily just open it up,
20
you~ow, at the fi~st littla upset. It tends to maintain a
21
stablg pressure in th9 system.
22
HR. GILBRETH: I b:eli,ev,e that answars my
23
qusstions. Thank you, sir.
24
MR. BURRELL: Mr. Marshall?
25
11R. HARSHALL: Hr. Anderson, you mentione:d
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1 th~t you did.have a slide th~t showed the datail of th~ John
2
zink clsan burning flare. I'd like to see that if you ---
3
MR. B. C. ANDERSON: Fine. Would you put
4
that slid; up there.
(Pauss.) Is that clear 9nouqh there? The
5
6
MR. MARSHALL: That1s batter.
7
HR. B. C. ANDERSON: Okay. The lower line
8 thsre of courss is the relief line which ti~s into our so-called
9
pressure relief valv:Bs and our ---. or pop valv,es, they're
commonly called --- and our ruptur~ discs; and it has a turn on
the end of it thsre that puts it out over the end of your main
10
11
12
burn,er. Th:e twenty-four inch fl3.re is your main high pressurs
13
flare coming out, and then there's quite a bit of design in tha
14
flare tip itself. This aspirator gas which is taken off the
15
System and actually jets the gas out so it ,can draw oxygen and
16
gat complete combustion. And then the low pr:essure flare, a tw:alvs
17
inch line over there, is actually tipped to one side in the desig~
18
and this then is very similar in design to the main burnar, but
19
this is for the low pressur,s system. That's where your deaeratio:1
20
gas will be coming out. And the --- I'm not sure that 'th3.t
drawing is to scale; it perhaps is, but in looking at the datail
drawing on that when we made up the slide, as I recall correctly,
21
22
23
looking from the edge of the low pressure flare pipe Qv:ar to the
or '
edge of the burner on the high pressure/main flare there was six
24
25
fast from just ths edge of the pipe to edge of the pipe, not
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1 centsr to can~~r. If you have any particular ques~ions, I'll be
2
glad to try to answer them; I'm not sure I can.
3
MR. MARSHALL: Are you satisfied t.'lith the
4 smokeless aspect, the efficiency of the smok9lass aspect of t.h~
5 flar~s?
6
HR. B. C. ANDERSON: Tha.t's a --- not at the
7 prasant time, no. We paid about $125,000 to install that fIara
8
tip, and we are having some difficulties with
vIe'rs right
..a.
.:L .... .
9
now have had the John Zink
man out as wall as people out of·
10 our general engineering departm,snt in Dallas who ware involved
11 in th~ design, and thsy have taken pictures of the tip and are
12 discussing some of the problems that wa are having with it right
13
now in 'hopes of finding t.he solution to that problem. That
14
particular flare tip design was sslected because we anticipated
15
a ~lide range of burning, let's say from our minimum pilot con-
16
ditions on up to the conditions wher'9 you might have an ups-et,
17
and from th9 information wa gathered this was the only tip we
18
could find that would cover the total range smokeless, and so
19
we doaxpect certainly to gat the tip --- for that tYP'3 of
20
investment --- êxpect to get it to where it does s~ti~fy us.
21
At the presant tima, though it doešn't.
22
HR. BURRELL: Mr. Anderson, you said 8,500
23
mcf par day?
24
MR. B. C. ANDERSON: That is th9 --- that's
25
the formation gas, and of course if you want to add the total gas
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1 in the systê~, ---
2
MR. BURRELL: Right.
(
3
MR. B., C. ANDERSON: --- we could hav~
4 23,000 mcf par day of gas lift gas that is rotated in the
5 syst~m.
6
MR. BURRELL: Y2ah. And you propose to
.7 flare som2 one million-three mcf?
8
MR. B. C. ANDERSON: If the Committee chooses
9 to ---
10
MR. BURRELL: Yeah.
11
MR. B. C. ANDERSON: ---combine the deaeratìo~
12
gas with the ath~r, that is correct.
(
13
MR. BURRELL:
(In~udible). There's quite
14
,a variance h9ra, as I have discussed be.fore with th,a other pl:.t-
forms. At least it would s,e:em to me th-er~, ' s qui t,e a va.ri:tnc~
15
16
here b~twe'~n the amount of gas b,eing flar:~d in an em:erg:9ncy
17
situation.
18
MR. B.', C.' ANDERSON: Thera is soms variance,
19
yes.
20
,MR. BURRELL: Yeah. You stat,ed your prabl,em
21
was, as I understand it, there's some equipment and soms work to
22
be done to install this 'equipment. Do you see any rr6al problêrt1
23
with so~e kind of a historical period hera of seeing how things
(
. 24
go be fora setting a monthly averaga p2rh~þs?
25
MR. B. C. ANDERSON: I ---
~1
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1
l,lR. BURRELL: Your nlli'11bsr is a ma.ximw1, is
('
2 it n~t?
3
HR. B. C. ANDERSON: Ne, it is not.
4
MR. BURRELL: Your 800 ---
5
MR. B. C. AHDERSON: iJc, our numb,~r is
6
MR. BURRELL: --- is not a m~ximum?
7
MR. B. C. ANDERSON: No,' sir. I don't
8 belisve that I could --- the way we approachad this thing was
9 lik3 this: we recognize ,that due to surges in the system thsra
10 ara going to bs timss this thing is '. continually varying" E.nd S0
11 we sought what w~s thought it would taka on anavarage for th'8
12 month on a daily rate averaga for the month, so thara will ba
(
13 _ varia'tions around th3.t particular number, but the number \..¡e' ra
14 ~sking for is 800' mcf per day on a monthly average basis for
15 the high pressure system.
16
MR. BURRELL: But your high prsssurs system
17 would flare more 'than that
18
MR. B. C. ANDERSON: It would have to flare
19 mars. than that on ·an instantaneous type basis I' whenever a. surge
20 ce:.m3 back, a well head'sd, . or the gas lift system ---
21
MR. BURRELL: Or a strong wind?
22
MR. B. C. ANDERSON: The wind would c=rtainly
(
23
affe~t it, but our number hare is for --- is to me~t any weather
24
condi tions sinc9 we wouldn't' expect to be abla to t:ell our
25
field psoplethat, wall, the wind's down, cut tha fIara back.
,~1
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1
Weirs looking for somethi~g we think we can live with day in ~nd
('
2
day cut on an average basis.
3
MR. BURRELL: Bu~ this 800 then, you would
4
probably flQre mora than that on csrtain days?
5
MR. B. C. ANDERSON: On certain days, that
6
is correct.
7
MR. BURRELL: Othsr days less?
MR. B. C. ANDERSON: Other days less, that's
8
9
correct .'
10
MR. BURRELL: Thatls all I have. Mr. Gil-
11
brsth?
12
,MR. GILBRETH: Hr. Anderson, in the early
'(
13
part of your tastimony you came out with a figure something like,
14 thirty psr cent of, the gas produced went t.o your pilot or SOffie-
15 thing; what was that thirty per cent?
16
MR. B. C. ANDERSON: That was --- how about
17 going back to slide two, if you would, 'please. The de aeration
18 --- pardon me --- yes --- th'e aspirator gas· which \ve I ve callsd
19 thirty per cent, that thirty per cent applies only to the minimum
20 flare position or 800 mef per day. I believe if you can follow
21 the line there, come back down just a little bit. This is ---
22 at this point right h~re that he has on the drawing is where
(
23
our gas comes off of our system between the separators and the
24 compressors and goes into the knock out drum; if you can follow
25 . tha line on up, well, this would go on out to the flars. Follow
~1
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1 it on ùp, wa ·take gas off of that for the aspirator gas, and
2
that thirty per cent is what we're taking off. Now, you'rs
3 actually ~-- there's a graph; we have a graphical type prasen-
4 tation; I do not have a slide of this; that shows the aspirator
5 gas goes up as the amount flared goes up, but it is not a constan~
6
per cent. It is a straight lin'e, but it starts at som~thing
7
other than z,aro since 'you have to hav,e som9thing at. the> starting
8
point. But just for 8xample, lat me give you a figura her~ on
9
the total flared gas, let's say aspirated and main flare; if I
10
was flaring atsorne rate ,at, a period of time of ten million cubic
11
fe1et per' day or 10,000 mcf per day if w? ~'Vant to stay in the same
12
units, it would raquire something like, oh, a little over one
13
million cubic fe~t p~r day of aspirator gas, so the thing does
14
vary. Whatw8 did, we took the 800,000, read what it would take
15
in that, thirty per cent at that point, but it cannot baextrapo12:!.:.:
16
directly.
17
MR. GILBRETH: All right. We havs heard
18
testimony from the other witnesses this morning on an instantan90us
19
rate under emergency conditions. Have you calculated or deter-
20
min~d an instantaneous rate for your platform?
21
MR. B. C. ANDERSON: I did not approach the.
22
probl~m from that --- from that m9thod. I think we recognize too
23
that part of the design or part of the factors that affect what
24
your minimum flare siz,e should be ars certainly the system velum; I
25
and the rate going into it, and I think I listed about four things,
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1 the system d~sign, and you of CQurss could ta.ke that syste.m and
(
2
say zero at the end of the flare tip and corne back and look at
3 your ~otal volum~ in input and c~lcula~e what your instantansous
4 rat~ would b: with no back prsssura on th~ and and what your
5 prsssurB drops ar~ and gat an instan~an2ous unloading rata if ths
6
,thing was to suddsnly pop. Ne didn't approach ..... from that Ÿ/3..Y;
~\¡..
you could probably look a,t our' total gas cycle volum3s and gat.
7
8 some h3.ndl e' on it ,in comparison to tha other psopl,s i howsvar, it's
,
9 not tctally just that; you'd have to also look at the tot~l syst~m
10 t.hat you hav.e, and ~'lhat that you have tra.pped, which is a part of
11 it as wall as the, rata flo\ving into it at any given point in tims.
12 But as ê.. ballpark type number, that'd be ona way. We ha. v,s not
(
13
calculat3d; we could havs that done.
14
HR. GILBRETH: That's all I have. rrhank you"
15 Mr. Anderson.
16
MR. BURRELL: Thank you, Mr. Anderson. Do
17 you want to move onto another platform?
18
MR. B. C. ANDERSON: Yes.
19
MR. A.l~DERSON: Hr. Anderson, I" d lika t:.o ask
20
you whether King platform Exhibi ts # 1 through # 3, tog'ether with
21
the plan visw of the John 'Zink
smokeless flare tip were
22
prepared by you or under your direction?
(
23
MR. B. C. ANDERSON: Y'6S, sir, they wer'6.
24
MR. ANDERSON: We ask that the King Exhibits I
25
#1 through #3, together with the plan visw of the John Zink
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1 smokeless flare tip be introduc~d into evidsncs.
2
MR. BURRELL: Could ws label the John
3 Zink on~ 'Exhibit #4?
4
MR. ANDERSON: Yes.
5
MR. BURRELL: Exhibit #4, and could we hays
6a copy of that?
7
HR.. ANDERSON: Yes. We can make that avail-
8 able to hand in.
9
'MR. B. C. ANDERSON: I can make it avai labl,£
10
just by (unintelligible).
(Pause. )
11
HR. BURRELL: Thank you v,ery much, sir.
12
MR. B. C.ANDERSON: Excuss me, are you rea.dy
13
for ---
14
MR. BURRELL: Procead.
15
MR. B. C. ANDERSON: 11m still the sarna B. C.
16
Anderson; I have the same job, I think. Atlantic Richfield
17
Company operates Platforms 'A' and Spark in ths Trading Bay Field.
-....-
Exhib~t 1 shows the location of th:ese pla.tforms in relation to
18
19
the other platform in the fi,eld, ths outline of the unitized 'G'
20
and Hemlock Northeast Oil Pool's productive limit, and the Granite
21
Point Onshore production facilities.
(Mr. Anderson's testimony
22
is attached as an axhibit to .this transcript.)
23
MR. BURRELL: Thank, you, Mr. Anderson. Mr.
24
Gilbreth?
25
MR. GILBRETH: Mr. Anderson, you have a
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1 twsnty-four ~nch high pressure flare on Platform Spark, do you
2 not?
3
B.C.
MR./ANDERSON: That's correc~.
4
MR. GILBRETH: And didn't you tsstify in the
5
case of the King ~h~t you had a twen~y-fcur inch flare lina also?
B.C.
MR./ANDERSON: Yes,' sir, that's correct.
6
7
Now, these flare lines are svledged down to a much smaller SiZð
8
at the snd. As I pointed out before, their primary purpose for
being that size is £or structural strength, and also that since
9
10 .
the lin9 is th~re and sealed and they can come into it on ons
end and out on the other, it creates no back pressure. The flare
12
boom on Platform 'A t, I do not hav,e an exact measurement i I
13
looked at it, and I would say it's about eighteen inches in
14
diarn~ter, and gas is not passed through that boom; the lines
15
run up the side instead.
16
a
MR. GILBRETH: The --- there is/consid2rable
17
difference in' the volume that you r'6conunended here for the pilot
18
b'etw:ssn the two.· Does this again come back to the equipment
19
onboard and the emergenby situations that ,would arise from this?
B.C.
MR.1ANDERSON: Yes, sir, that is porrect.
20
21
Comparing Platform 'A' with Platform Spark, Platform lA' has
22
three wells that operate with a
Reda or subm'ersible pump, so
23
thers ar~ only thrse w91ls on gas lift, \.¡hich gives us very
24
little gas lift on that platform. On Platform Spark it is a
25
totally gas lifted operation, and handles quita a bit more gas
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1
and so this ~s primarily the difference in the thing is your g=s
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2
volums handled.
3
MR. GILBRETH: Okay. Could you briefly t~ll
4 us what th9 differ=nc~ in the volumg you recomm~nd b9twesn ths
5 King and the Spark is?
6
HR. B. c. ANDERSON: Well, once again thers
is a larger va I urn,e handled on Platform King, quits a bit larger
than either Platform Spark or Platform 'A' , and there's quite a
7
8
9 bit mor,e oil produced as a daily rate there. Of courS,2; I don't
10 consider it as directly a straight line relationship. Thara some-
11 thing that requires a. -~- som,s part of it requir',=s th:s minimum
12 size to keep the, thing burning; there's some part of it requires
(
13
wh3.t. 'ara your surg'9s that you ha.V3 in your systßnl which ti£:s
14 back to the ,volumes processed, the confined volume you may have to
15 releas:s and this typa of thing, so I feal tha.t thsy are compa:'.:.ibl i.:..:;.
16 Oncs again, our recommendation is based on judgm3nt; it's based
the
17 on judgment which is built from ~experience in op9rating/platforIas
18 ,and 'hõ.ving flaJ;8s blown out under some situations, and in the
19 case of Platform 'A' and Platform Spark, having operated th'ere
20 with very low flare volumes for soma period of time, and so it's
21 that type of thing that's built in our r'8cornm:endations and not an
22 engineering calculation.
(
23
MR. GILBRETH: And you've actually experienced
24 it there, haven't you~
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25
MR. B. C. ANDERSON: In Platforms 'A' and
~1
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1 Platform Spa.rk, \v~ 'va oparatsd r:luch of tha tirn: vary naar thes~
2
v~lums, 2.nd Pla.tform Spark '\vs buy gas, if ýou :--- -,
3
MR. GILBRETH: \~at happsns if you run in~o
4a deficiency there? Do you bring in m~ka up g~s for your pilot
5 volum9?
6
MR. B. C. ANDERSON: Well, it's not exactly
7 ---it doesn't come in for the pilot volume, but it --- in ,sffsct
8 ~.¡è feal strongly enough about the ne,ed for ths safety pilot that
9 say on Platform Spark whare ws arê alr,eady rats d,efici,snt that
10 wa do flara a volume in the order of what we!.re talking .about
11 here, and at the same time we are buying gas from ~ha Mobil-Union
12 supply that comes from the Granite Point Field on this contact
13
'tV'hichI spoke about yesterday a.nd also a little bit in my tasti-
14 'many hers today. So this gas do'es corns into our system and goas
into the fuel system and enables us to maintain a safety pilot.
MR. GILBRETH: In other \vords, you' rs
actually paying 'in some cases for gas you're flaring for the
safety pilot?
MR. B. C. ANDERSON: Not diractly, but in
net \V'ise we do. Ne US'9 ana gas for one purpos:e a.nd flara another,
but we're not buying gas and then running it out the flare and
flaring it, but it
MR. GILBRETH: Just as a matter of curiosity,
I ,\V'onder, the oxygen enriched gas that you get, does this burn
as well or hetter than just normal unstripped casinghead gas?
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1
HR. B. C. ANDERSON: Yes. I don't think
2
thera's any real differenc~; so far as I know ---
3
MR. GILBRETH: Can 'you ~~ll the diffsrence
4 when they're burning?
5
MR. B. C. ANDERSON: --- th~re's no real
6 diffsrance in the way they burn. Of coursa the gas is going to
7 be saturë:.tad with water which most low pressure gasi9s ar'ê anyway
8 when they come off t~e saparator.
9
10
MR. GILBRETH: That's all I have.
HR. BURRELL: " Hr. Marsha.ll?
11
!4R. MARSHALL: Mr. And:srson, did you mention
12
:the natura of the burning tip on Platform 'A' and Spark?
Are
13
t.hes:e also the John Zink
design?
14
HR. B. C. ANDERSON: No, the tips on Plat-
15
form 'A' and Spark are not John Zinke
The tips on Platform
16
'A', the high pressure flare is a four inch line, and it's open
17
on the and; the low pr9ssure flare is a three inch line, and it
18
is op,en on the end. John.....,Zink
tips have not bsen used th~r8.
~9
20
The Ringleman test for the srookel'sss flare ha.s been satisfactory
on thes= low flare systems thers, so this is the r'sason we haven It
On
gon-e to that on the Platform 'A'. /Platform Spark our high pres-
21
22
sure flè..re system, : as I'v,a comm'ented before, is a twenty-four
inch boom; it goes to an eight inch nozzle, and thisnozzl-s is
shi·eldsd; and on the low pressur'e flare, it has a four inch lin2, I
and it's open on th~ end with a shield; and the relief and ruptur:s
23
24
25
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pag¡a 76
1
disc flare i& a six inch lina, ~nd it is open on the end with a
2
shi9ld on Platform Spark. And for th~ same reason we haven't
3
install8d John Zink
tips on t.hos=.
4
MR. MARSHALL: Thank you.
5
MR. BURRELL: You had 400 mcf par day, Mr.
6
Anderson, on 'A', and 600 mcf pgr day on Spark, on a monthly
7
averag,~basis?
8
MR. B. C. ANDERSON: That is correct, sir.
9
MR. BURRELL: Doss this represent a maximum
which you think you'd n¡eed in case of an instantan'eous rsle;;.sa?
MR. B. C. ANDERSON: No, sir"it does not.
It's just as on thß King, it ---
HR. BURRELL: S3-IDS as ---
MR. B. C. A.t~DERSON: --- repres ants. our
av'.erage si tuaticn, and ---
MR. BURRELL: --- the King; your best guass
as to a monthly average.
HR. B. C. ANDERSON: And also on thë Sp2rk,
the 600 does not includs the daaeration gas that comes ovar there,
so I think 50 mcf on the cpsration there.
MR. BURRELL: 50 roef on that~
MR. B. C. ANDERSON: Yes, I think the
schema tic ShO~"lS it thera some;~.¡here.
Yss,
.~
~-
Just a sacond.
is, on the bottom there. Sae the line coming over on Spark,
coming out of the. dea·e.ration tc\.¡ar ov,ar there.
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1
MR. BURRELL: Do you think yoú'd minimiza ~hs
2
flaring in any way if you had bsttsr tips on those open linss?
3
HR. B. C. ANDERSON: No, sir, I do not. I
4 ,think this is strictly just for --- just for complete combustion
5 to get mor'S oxyg·en ther:e so it gets rid of the trail of smoka
6 that would come off of our ---
7
MR. BURRELL: You might minimiz~ the smoka
8 but not the gas?
9
MR. B. C. ANDERSON: The amount of the smoke,
10 they' r9 strictly for smoke and not for th'e amount of flare.
11
11R. BURRELL: I have no further questions,
.12 thank you, Mr. Andarson.
13
l1R. ANDERSON: I'-1r. Anderson, were your
14 ,Exhibits #1 through #4 prepared by you or under your diraction?
15
MR. B. C. :~.NDERSON: Yes, sir, they were.
16
MR. 'ANDERSON: Mr. Chairman, wa ask that
17 Exhibits #1 through #4 which we'll designate as Platform 'A' and
18 Spark Exhibits #1 through 14 be introducsd into evidenca."
19
MR. BURRELL: We'll accept those into
20 evidence for the record, and if you raproduce the smaller copies,
21 we'll accept them~ They are copies of the bluélines, right?
22
MR. B. C. M~DERSON: That's correct. The
23
slides in all of my testimony ars exact reproductions off of the
24 blueline copy.
25
MR. BURRELL: Thank you, Mr. Andsrson. You
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18
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påge 78
i:
~
1 will bs available latar for further quastions?
2
MR. B. C. M1DERSON: Yes, sir, I will.
3
MR. BURRELL: Th~nk you.
4
MR. ANDERSON: Mr. Chairman, as I m~ntioned
5
earlier, we would like to at this time recall Mr. J. R. ßarb~r
6
who will testify concarning the West Foraland Production Facility,
7
otherwise known as the Trading Bay Production Facility, and the
8
siza of the safety pilot at that facility.
9
MR. BURRELL: We'll go off tha record for a
10
few minutes here while we change tapes.
11
(OFF THE RECORD)
(ON THE RECORD)
12
13
MR. BURRELL: Waf II go back on ~1e record
14
~ now.
15
MR. ANDERSON: You may proceed, Mr. Barbar.
MR. BARBER: Okay. My name is John Barber.
Marathon Oil Company's responsibilities
. MR. ANDERSON: Could you spaak just a 1i ttl:e
louder?
MR. BARBER: Okay. Marathon Oil Company's
re~ponsibilitias as a subopsrator in the McArthur River Field,
Trading Bay Unit, includes not only the operation of the Dolly
Varden Platform, but also the operation of the West Foreland
Production Facility located on the west side of Cook Inlet as
shown on my Exhibit #1 or the Pipeline Exhibit #2 from yesterday's
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1 testimony.
2
Oil and gas from th~ Dolly Vard~n, Grayling, King Salmon,
3 and Monopod platforms are processed through the West Foreland
4 'Production Facility. Approx~mats1y 130,000 barrels of oil and
5 51,000 mcf of gas will be processed at this facility aach day.
6 The basic equipment layout of the facility is illustrated
7 in Exhibit #4. The major ccmponsnts of this processing system
8
includ~ the Battery No. 1 oil treating unit, which is composed
9
of lins heaters, a flow splitter, heater treatgrs, and crude oil
10
storage tanks; ,the Battery No. 2 unit is essentially the sarns as
11
the No~ 1 unit, consisting of a flow splitter, hsater treaters,
12
and crude oil storage tanks. Tha gas handlirig complex includes
the Liquid Extraction Unit ~nd the comprzssor station. Hydro-
carbon liquids ars recover:.;¡d from'theproduc:ed gas in t.he'LEX
13
14
15
Unit and the residus gas will be compressed and transportad across
16
Cook Inlet to ,the Nikiski area. The quarters facilities for our
17
opsrating personnel are also shown on this exhibit. This faci-
18
lity contains complete living acconunodations for approximately
19
forty men.
As stated 'previously, approximately 130,000 barrèls of
oil and 51,000 mcf of gas will be processed at this facility each
20
21
22
day. A safety pilot is essential to the safe operation of this
23
facility'1ust as it is essential to the operation of producing
24
platfonls in the In1.et. HO\'l'8V,er , it is apparent. frem the,~xhibi t
25
that the operations 2.nd the physical location of theequipm'ent
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{
1 at tha W9st Por,eland product.ion Facili ~y is consid,~rably dif-
2
f'~r.ent from operations and 'equipm~nt plac·:sm::nt on product.ion
3
platforms in Ccok Inlet.
4
Process equiprnant2t this onshore facili~y is spread ~ut
5
over an arga of a.pproximately forty acres, whereas the aV9rag,2:
total deck spaca on a platform in Cook Inlet is considerably
6
7
less than one acre. Being able to spread the process equipment
8
over a large area co~stitutes one reason that the necessary size
of the safety pilot will vary fromcnshore to offshore. Bscauss
9
10
equipm'ent is spread out over a larga ar'za, as indicatså on ,th~
11
Exhibit, th.e sudd;:sn gas surge resulting from a compressor shut-
12
dO\lJn is not nearly as pronounc3d a~; the West Forel2..nd Production
13
Facility as it is on the polly Varden platform. At the H:sst
14
Foreland Production Facility, there is considl~rable distanc:e
15
betw·sen the compr·essor station and the flare tip; consequently
16
the surge of gas expands through a greater volume prior to
17
exiting out the flare tip. As indicated on th,e :equipment plat,
18
a gas surge resulting from a compressor shutdown must travel.
19
through approximately t'(ÑO hundred and fifty fe,et of twelve inch
20
diameter pipe, on·e thousand fe·et of sixteen inch diam-st:er pipa,
21
and an eight f09t diameter liquid scrubber before rsaching th~
22
flare tip. Expansion through this system greatly dampens the
23
initial gas surge.
24
Also ,at the ~vest Foreland Production Facility, the flare
25
tip is located over three hundred feet from any process equipment
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1 a.nd one thousand f'ß'êt from the personnel quarters. The addi'tional
(
2
distanc2 batween the flare tip and othsr facilities at the onshore
3 site graatly increases the chance that if any unburnsd hydrocarbo~
4 gas is allowed to escape from the flare tip, it would dissipa-ta
5 below explosive limits before reaching a source of ignition.
6 In view of the operating conditions, equipnlent placemant,
7 and weather,eonditions at the Trading Bay Production Facility,
8 Harathon submits that tte volume up to 300 mcf per day is required
(
9 for an adequate safety pilot. live testified as to why we feel
10 tha safety pilot at the West Foreland Production Facility does
11 not require as great a' volume of gas as the one on the platform.
12 The question might now arise as to why we feel that 300 mef per
13
da.y is required.
14
I've quoted the large volumes of oil and gas that is
15 handlsd at this facility. When we complete our compressor
16 station expansion, we will have approximately 10,000 horsepowar
17
of compriession at this facility, which on a complete,
shutdown
18
could be releas,ed out the flare tip. W,s have nin~3 heater treabers;
19
we havre three line heaters and t~.,o flow splitters as part of our
20
process equipment. This could all relieve in the flare also.
21
22
Ne have ths LEX plant that could r'slieve in the flar,e. So we
do submit that 300 is required for the onshore production facility.
(
23
Now, this conclud~s my prepared testimony; lid be happy to att~mpt
24
to answsr any question~ that you might have.
25
MR. BURRELL: Thank you, Mr. Barber. Any
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1 questions?
2
MR. GILBRETH: Mr. B~rb~r, your fl~re stack
3 at th9 ~'V:st For~land Facility, does it ,extend up into th3 a.ir?
4
MR. BARBER: Yes, sir.
5
MR. GILBRETH: It's not horizontal or ---
6
MR. BARBER: No, sir. It's in a'vertical
7 position.
8
MR. GILBRETH: Would thsre be lsss likelihood
9
of the flare going cut if it wer9 in a pit below ground' level,
say?
MR. BARBER: If it was in a pit below ground
12
lev'al?
13·
MR. GILBRETH: Yes. .1 ask this because
14
Mobil had one this way for quite som'etime and it s:eemed to be
15
fairly satisfactory; I don't knew what their experience was.
16
MR. BARBER: Well, in the past ours was also
17
in a pit, and I can only say ws have flared much more than 300
18
to the pras9nt time at the facility, both when it was horizontal
19
and vertical, and 'tve have not ·exp;erienced any problzms si tiler W?~y
20
vli th it, so that's the only 'f.,ray I could a.nswsr thE. t.
21
HR. GILBRETH: It. is true; I guess, th~t
22
any gas that you ~oald flare at this point would be lost for sale
23
to the op~rators, wouldn't it?
24
HR. BARBER: It certainly would.
25
MR. GILBRETH: Lost for sale becaus'e it will
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1 hav2 a ligh~·in it?
2
HR. BARBER: Y~s, sir. \"le would a-:.tampt,
3 of course, to ks::p our safst.y pilot to a minimum.
4
HR. GILBRETH: I don't hava any ether
5 questions.
6
HR. BURRELL: Mr. Harshall, do you ha..ve z..ny
7
qU9s-::ions?
8
HR. HARSHALL: Yes. Mr. Barber, vlould you
9
describe the burner tip at the West Foreland Facility ---
10
MR. BARBER: The ---
11
MR. ~mRSHALL: --- or the flare stack?
12
MR. BARBER: Our burner tip, present burnar
13
tip, just from an obsarvation, is very similar to tha ana tha~
14
you sa:~" projected for the King S~lmon Platform, \vithout the
15
siza flare on it; the main tW2nty-four inch flarE that you saw
16
projec'ted on the scrsen resemblasour flare tip at the \"¡'est
17
Foreland production Facility very much the sarna. Thsy are John
18
Zinke
19
MR. MARSHALL: They are John Zinke
20
MR. BARBER: The one that we have- and both
21
of them are John Zink
tips. Mainly designed for smoks.
22
MR. !1ARSHALL: I have one little quðstion
23
about your Trading Bay Produc~::ion Fe..cili ty map hare. I presurn~
24
that the sixt:sn inch flar8 line is --- is this a double lins
25
running under 'th9 words Battary Two?
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MR. BARBER: No. That is a single sixtean
2
inch flare line from the LEX plant to tha flare tip.
3
MR. ~ßRSHALL: I sae. And then tha~'s unifi;~
4 with the flare line coming up from the compressor stations?
5
HR. BARBER: That is corr~ct, y=s.
6
MR. MARSHALL: Thank you. Another problsm.
7
our -,-- what --- ho\.¡ do you choose to --- perhaps you I ra going
8
to cover this, Hr.. Andsrson. Wa have Exhibit # 4 on our:. reduced
9
size exhibit here.
10
MR. ANDERSON: Yes. I propose to clarify
11
that..
12
MR. Þ~RSHALL: That's all the questions I
13
have.
14
MR. BURRELL: I have no questions.
15
MR. ANDERSON.: Mr. Barber, did you refsr to
16
as
this/Exhibit #41
17
MR. BARBER: Y~es, I d,id in my tes timony .
18
MR. ANDERSON: I think we ---
19
HR. BARBER: It was so numbered bscause I
20
planned to be on one time.
21
t-iR. ~rDERSON: Yes, we changed 'our ordar, Hr.
22
Chairman', and I \vould suggest that we change this -exhibit t-o
23
We~t Foreland #2 and Exhibit #2 at the Pipeline Hearing should
24
be West Forsland's Exhibit #1 here, and we shall furnish you
with reduced copies of that axhibit.
25
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Pag:a 85'
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MR. BURRELL: Weill acc~pt it for thë
2
record.
3
MR. ANDERSON: Hr. Chairman, also -thera's
4 on9 other matter which we might have Mr. Barber talk about as
5 long as he is here, and that is concerning the size of the
6 safety pilot for the Dolly Varden platform; it'll just take a
7 moment, I believe.
8
MR. BURRELL: All right.
9
MR. BARBER: It appears maybe that we had
some confusion in my Direct earlier.on the 1,000 mcf for the
platform as to an everyday volume of thirty a month, and I
testified that I did not think we wouldneedthirty a month, but
I did not mean to infer that we should be limited to something
~ess than thirty if the need should arise. We should have that
flexibility that on some ,month we may need thirty, and I wanted
to try to clear up that area.
MR. BURRELL: Well, let me explore that just
a second. Would less than thirty a month be satisfacto~if you
had the exception for an emergency condition. In no way any
number we .might set, if we set a specific number, wou~d preclude
an emergency; we're not going to endanger either life or property,
and any Order we would iSSUè which would do so I think would be
23
illegal and immoral both.
MR. BARBER: Yes. I would look on the emer-
24
25
gency as something over and above a safety pilot.
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MR. BURRELL: I would too.
2
MR. BARBER: I was looking at just the safety
3 pilot volume here.
4
MR. BURRELL: All right.
MR. BARBER: I look to a million per day.
MR. BURRELL: I understood you to testify
5
6
7
earlier, maybe I'm mistaken, I understood you to testify earlier
8
that a million a day' average average 'or thirty a ~onth, thirty
million a month average, would cover the strong winds under a
9
complete shutdown of both compressors?
MR. BARBER: That covers just the safety
pilot. Of course, when the compressor's shutdown, there is alot
larger volume that's flared at that time that's over and above
what, we would include in the safety pilot volume.
MR. BURRELL: Both of these are flared through
the same boom.
MR. BARBER: It's flared through the same
boom.
MR. BURRELL: Right, that's what I understood,
okay. Then the thirty million a month would not inclUdeshut--
down?
MR. BARBER: Would not be the emergency type
situation.
MR. BURRELL: Just the situation if both
compressors were down?
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MR. BARBER: Right, for just a few moments,
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yes, sir.
3
MR. GILBRETH: In other words, the million a
4 day that's here or the thirty million a month that you testified
5 to is just for the pilot light, exclusive of all other flares,
6 by itself?
7
MR. BARBER: Yes, sir. That's with every-
8 thing running and just the pilot>burning, yes, sir.
9
MR. BURRELL: I'm glad we got that clarified.
10 Thank you very much, Mr. Barber.
11
MR. ANDERSON: Mr. Chairman, that's all we
12
have at this time. We'll proceed with Granite Point after
(
13
lunch', if ---
14
MR. BURRELL: Right, we'll adjourn until
15
ona-thirty for lunch.
16
17
(OFF THE RECORD)
(ON THE RECORD)
18
MR. BURRELL: Good afternoon, ladies and
19
gentlemen, we'll reconvene the hearing.
20
MR. ANDERSON: Mr. Chairman, as I mentioned
21
earlier, Mr. W. R. Harrison and Mr. Rischer ~hórnton, attorneys
22
for Mobil Oil Corporation, will handle the Granite Point Mobil
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Number One platform.
24
25
MR. BURRELL: Thank you, Mr. Anderson.
MR. THORNTON: This is R. M. Thorton of the
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1 law firm of Holland and Thornton, representing Mobil oil
Corporation. Mr. Chairman, as you and the rest of the
2'
3 Commission are aware, Mobil,', Oil Company has contested Conser-
4 vat ion File No. 102, and it's presently: in the Superior Court
for the State of Alaska. That of course will have some outcome
5
6 on any flaring insofar as the Mobil platform is concerned.
7 Prior to testifying here, the Mobil witnesses are appearing here
8 today with the understanding that such appearance will not
9 constitute a waiver of any right of Mobil in such case, nor shàl1
10 any such testimony be used in any manner prejudicial to such
11 right. ' Subject to that, we will proceed with our testimony.
12
MR. BURRELL: Mr. Thornton, I --- the last
13
bit of it there threw me just a bit, sir. YOU mean that as far
14 ,as you are concerned, the record of this testimony cannot be
15 used in any subsequent judicial proceedings?
16
MR. THORNTON: We have no objection to it
17 being used in any other judicial proceedings.
18
MR. BURRELL: All right, I'm talking about
19 the one now pending.
20
MR. THORNTON: We --- actuálly, we have no
21 objection to its being used in the currently proceedin9 --- in
22 the current proceedings, so long as it's not used in a manner
23
to constitute a waiver of that proceeding.
24
MR. BURRELL: All right. I have no objection
25 to that so long as it can be used --- in no way is it intended to
~1
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constitute a waiver of any right in the proceedings ---
2
MR. THORNTON: In other words, our appearance
3
here today is not to be constituted as a waiver of any rights
4
that we're asserting in the contest that we presently have filed
5
in the Superior Court.
6
MR. BURRELL: That's accepted.
7
MR. HARRISON: Mr~ Chairman, members of the
8
Commission. W.,R. Harris of --- Harrison, appearing for Mobil
9
Oil Corporation. With your indulgence of the Commission, I'd
like to set the record straight on the hearing that was held
10
11
the previous day. There's been a lot of comment about the
12
gentleman that sat next to me in the rear of the room here yes-
13
terday, and I'd like the record to show that Mobil disclaims
14
any association with this individual. He is not a Mobil employee,
nor is he on retainer to Mobil. (Laughter.)
16
MR. BURRELL: The only reason the question
17
c~me up, Mr. Harrison, is Mobil's the only one that didn't have
18
---the only operator that did not have an engineer speak, and
19
he was sitting next to you
(laughter) ---
20
MR. HARRISON: I figured ~hat, and a lot of
21
you probably in your minds figured that my witness was unavailable
22
to testify. Mr. Chairman, we have one witness who will appear
23
in this matter being heard by the Commission today; it's Mr.
24
,Max Beazley. Mr. Beazley has not previously testified before
25
this Commission, and with
we'd ,like at this time to have Mr.
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1 Beazley qualify himself as an expert witness in this matter.
2
Mr. Beazley, would you proceed and tell the Commission your
3 background and education and so forth.
4
MR. BEAZLEY: My name is Max Beazley. I
5 live at 7311 Madylnn Drive in Anchorage. I graduated in 1949
6
from University of Southern California with a degree in Chemistry.
7
I'm registered as a Professional Chemical Engineer in the State
8
of California in 1957. I've worked for Mobil Oil Company for
9
sixteen years as a chemical engineer, as a production engineer,
10
'and as an operations engineer. My present assignment is
Associate Operations Engineer with the Alaska Producing Division;
12
I have occupied that position for approximately two and a half
13
year s .
14
MR. BURRELL: Thank you, Mr. Beazley. Without
objection, we'll accept your qualifications. Sir, were you
16
sworn earlier?
17
MR. BEAZLEY: Yes, I was.
18
MR. HA.RRISON:'Mr. Beazley, in your capacity
19
as an Assistant Operations Engineer, are you familiar with the
Mobil Granite Point platform?
21
MR. BEAZLEY: Yes, sir, I am.
22
MR. HARRISON: Are you also familiar with the
23
safety flare equipment that is located on that platform?
MR. BEAZLEY: Yes, I am.
25
MR. HARRISON: In preparation for this hearinq,
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1 have you prepared a statement which you wish to give to this
2 Commission at this time?
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MR. BEAZLEY: Yes, I have.
4
MR. HARRISON: Will you now proceed with your
5 statement, Mr. Beazley?
6
MR. BEAZLEY: All right. I'll skip the first
7 paragraph since I've already gone over that. Mobil is operator
8 for itself and Unioâ Oil Company of California on the southern-
9 most platform in the Granite Point Field. We are now producing
10 approximately 6100 barrels a day of oil and 6500 mcf per day of
11 associated gas.' We are cycling some 6200 mcf per day ,of gas to
12 lift the oil to the surface. We therefore are handling 12,700
(
13
mcf per day of gas on the platform. Of this amount, we are now
14 compressing approximately 8500 mcf per day of gas: 6200 mcf for
,15 gas lift, 1300 mcf for use as fuel, and 1000 mcf --- up to 1000
16 mcf for sale to Atlantic Richfield Company. There are two com-
17 pressors on the platform available for this service. The first,
18 a Cooper GMBA 12, is rated at 1550 horsepower and is capable of
19 handling 7500 mcf per day. The second, a Clark HMA 8, is rated
20 at 350 horsepower and, is being used to compress gas for sale to
21 Atlantic Richfield Company. The balance of the gas, 4200 mcf
22 per day, is being flared in a sixteen inch ~ink.flare. We
(
23
presently are in the process of replacing the flare tip with a
24 twelve inch tip manufactured by National ~~~Oil Company. We
25 expect the new tip to burn the excess gas more efficiently.
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The plåtform is connected to our shore site facility with
2
two eight and five-eighths inch subsea pipeline. One of these
is used to transport our produced crude oil to shore for treatinr
3
4
and shipping through the Cook Inlet Pipeline System. The other
pipeline is carrying about 1200 mcf per day of gas at 150 pounds
to be used for fuel by ARca and our own shoresite facility.
The gas now being flared is composed of the following:
5
6
7
8
crude surge tank vapors:-~400 mcf per daYi deaerator vapors -
9
100 mcf per day; gas liquid stabilizer overhead 120 mcf per day;
separator gas 'in excess of compressor needs - 3580 mcf per day.
The first three gas streams men't'ion-ea are at atmospheric pressure,
and the separator gas pressure is presently about 55 pounds.
Exhibit #1 which is attached to the testimony is a schematic
representation of the existing gas facility system and illus-
trates all of the gas sources mentioned. As can be seen from
the schematic diagram, all gas to be flared,:inöluding the
\
separator gas, is routed to the well cleanout tank and then to
the flare. The tank and all subsequent piping is operated at
essentially atmospheric pressure. In addition to the::continuous
sources of flare gas, all emergency relief and vent valves are
21
piped into the flare system. In the event of a compressor
22
(
24
malfunction '·or other emergency shutdown for overpressure, the
23
gas in the affected piping will be relieved to the flare. When
this occurs, it is essential to the platform safety that the
25
flare have a sta~le flame so that the vented gas is ' burned. I
~1,
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1 know of no established technical method for determining the
("
2
minimum volume of gas necessary to maintain this stable flame.
3 Weather and operational conditions will have a large effect on
4 this minimum volUme. It is therefore recommended that the
5 Mobil-Union Platform be allowed to burn continuously as a safety
6 pilot 1,000 mcf per day on a monthly average with a fifty per
7 cent tolerance to be used at the discretion of the operations
8 supervisor in charge.
9 It is further recommended that as experience shows that
10 a change in the volume Œ gas so flared is necessary, that such
11 a change be granted on an administrative basis. ,That concludes
12 my prepared tes~imony.
(
13
MR'. HARRISON: Mr. Beazley, is your",
14 ~ recommendation as to ,the volume of the safety flare on the Mobil
15 platform based on a single flare operation?
16
MR. BEAZLEY: Yes, it is.
17
MR. HARRISON: A change in operating conditions,
18 changes what would you recommend, as to the recommended volume
19 for a safety flare?
20
MR. BEAZLEY: To start a changed operation
21 with a second flare, if that were necessary, I would have to
22 recommend the same volume and depend on experience to show us
(
23
what volume was actually necessary for any changed condition.
24
MR. HARRISON: Mr. Chairman, that concludes
25
our testimony as to this witness, and he will now be available
~1
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Page 94
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1 to answer any questions.
2
MR. BURRELL: Thank you, Mr. Harrison. Mr.
3 qilbreth; do you have any questions of Mr. Beazley?
4
MR. GILBRETH: ,Mr. Beazley, this
you.
5
recommend a minimum safety pilot allowance of 1,000 mcf per day
6
with a fifty per cent tolerance?
7
MR. BEAZLEY: Yes, sir.
8
MR. GILBRETH: You've heard, I guess, the
9
testimony of some of the other operators here this morning,
indicating that they felt the 1,000 mcf per day would be adequate
over a period of a month, some days requiring more and some days
requiring less. Is that--- the fifty per cent tolerance you
have there, 'is that what you're meaning in it, or are you
· actually meaning an allowance, up to 4500 mcf per month?
MR. BEAZLEY: Based on what I know now, I
would have to suggest that this be a 4500 mcf per month, presuming
that we couldn't predict the minimum requirement for thirty days
in a month.
MR. GILBRETH: You don't have any experience,
I don't guess, now at the lower rate, know what kind of a volume
you really have to have on the platform?
MR. BEAZLEY: No, we don't. We're not capable
of ~xperience in this range of operation now.
MR. GILBRETH: Incidentally, how many flares
do you have on your platform?
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MR. BEAZLEY: Just a single flare.
(
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MR. GILBRETH: Just a single flare. Can you I
3
tell me what the size --- I saw the burner tip, sixteen inch
4
Zi.nk ---
5
MR. BEAZLEY: Yes" this --- Ì:t's a sixteen
6 inch flare tip now with a sixteen inch pipe leading to it.
7
MR. GILBRETH: Going to a twelve?
8
MR. BEAZLEY: No, it will be when we have
9 completed the change. Right now it's a sixteen inch pipe leadin~
10 to a sixteen inch tip.
11
MR. GILBRETH: Okay. For the pilot gas, do
12
you have a separate pilot line, or does it feed through the six-
\
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13
teen inch line?
14
MR. BEAZLEY: We have three pilot lines on
15 the flare tip as it exists. These are igniter pilot lines. I
16 wouldn't consider them safety pilot lines.
17
MR. GILBRETH: Do you mean by that that they' ;:-e
18 subject to go out?
19
MR. BEAZLEY: Yes, they are. Our experience
20 with them has been quite bad¡ they~re not reliable.
21
MK. GILBRETH: Is there any prQvision in your
,22 platform hookup to measure the gas that is used for the safety
(
23
pilot?
24
MR. BEAZLEY: No, sir, there is not.
25
MR. GILBRETH: Is your hookup like the other
...... 1
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If
Page 96
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1 platforms, such that if'an overall emergency condition arises,
2
that your control valves will all be opened to the flare?
3
MR. BEAZLEY: That's correct.
4
MR. GILBRETH: With the piping that you have,
5-
would it be feasible to measure the gas you use now on the
6
platform, the pilot gas?
7
MR. BEAZLEY: No, sir.
MR. GILBRETH: That's all I have right,"now,
8
9
thank you.
MR. MARSHALL: Mr. Beazley, you're replacing
your Zink flare tip with a smaller Natiònal Air/Oil tip?
MR. BEAZLEY: Yes, sir.
MR. MARSHALL: Could you describe briefly
,the difference in these tips?
MR. BEAZLEY: Yes, the new tip is commonly
called a steam injection flare tip. It has a ring on the end of
it ,which injects gas through I believe it's eighteen nozzles
into the flame itself. This induces turbulence and çreates"
better combustion characteristics.
MR. MARSHALL: I see. It then is a smoke
its.purpose,is to ·achieve smokelessness,
MR. BEAZLEY: That is correct.
MR. MARSHALL:
rather than perpetuating
tqe flame?
MR. BEAZLEY: That's correct.
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MR. MARSHALL: Thank you.
(
2
MR. BEAZLEY: In other respects it's similar
3 to the old flare, except it's smaller.
4
MR. MARSHALL: Thank you. I have no other
5 questions.
6
MR. BURRELL: Mr. Beazley, as I understand
7 it, you are requesting 4500'mcf per month as ---
9
M2.. BEAZLEY: It's ---
MR. BURRELL: --- as discretionary
MR. BEAZLEY: Yes. I would exp~ct 1', or would
8
10
11 like to have a nominal volume with a tolerance in the wording Of
12 the order; this would be appropriate to us.
í(
13
MR. BURRELL: Could you tell me what you're
14 currently flaring' per month under platform operating conditions?
16
MR. BEAZLEY: Approximately 4200 per day.
MR. BURRELL: 4200 per day?
MR. BEAZLEY: Yes.
MR. BURRELL: You mentioned the possibility
'15
17
18
19 of --- I shouldn't say the --- well, I guess possibility is the
20 right word --- possibility of a second flare boom u~der certain
21 circumstances, in which case when you get it, you'd probably
22 want to have roughly the same size flare and ---
( 23
24
25
MR. BEAZLEY: Yes, sir. Without --- pardon?
MR. BURRELL: Go ahead.
MR. BEAZLEY: Without knowing more of the,
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~
1 potential change than that statement, I would have to recommend
2
that, yes, sir.
3
MR. BURRELL: Could yOU" give me some idea of
4 the circumstances under which you might find it necessary to
5 install a second flare boom?
6
MR. BEAZLEY: I would think that the addition~l
7
production over what we see now, or a 'different conditions of,
a
safety,/different' ,type of operation ,which might create more
8
9
hazardous conditions with the flare boom that we have.
10
MR. BURRELL: Well, unless you find a new
11 oil pool or something like that, I would say there'-s"' probably
12 not much chance of the former.
13
MR. BEAZLEY: I would say the chances were
14
, slim, yes, sir.
15
MR. BURRELL: What change in operations do
16
you contemplate? That's kind of a broad term; I guess I should
17
MR. BEAZLEY: I don't contemplate any change.
18
MR. BURRELL: What possible chagge in
19
operations could occur that might necessitate a second flare
20
boom?
21
MR. BEAZLEY: I can't visualize'any right at
22
the moment. Perhaps a different recovery method or similar
23
change in operation of that nature.
24
MR. BURRELL: I'm just trying to get some
25
idea if we had an imminent problem here.
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1 '
MR. BEAZLEY: No, sir, we· do not. I know of
f
2
none.
3
MR. BURRELL: I see.. Does this maximum that
4 you've requested of 4500 mcf per day --~ does that cover such
5 things as, oh, emergencies. that might arise out of instantaneous
6 discharge situations?
7
MR. BEAZLEY: No, sir. This would be the'
8 volume that I think we would attempt to maintain routinely, whic~
9 as I mentioned in my testimony would be at the discretion of the
10 operations superintendent. My feeling is that he's the man in
12
charge of the platform, and he should have some discretion. I
expect he would operate prudently and would not burn more gas
t.han was necessary.
11
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14
MR. BURRELL: Sure, well, I'm not arguing,
15 --- I didn't mean to imply that he.might., What is your instan-
16 taneous discharge volume? I don't believe you testified to it.
17
MR. BEAZLEY:, No, sir, I have not. calculated
18 that.· It would be, re]~atively smaller than other platforms or
. .
19 people have testified for, other platforms, ,but I did not calculate
20 it.
21 MR. GILBRETH: And yet you're as,king for a
22 larger flared volume?
(
23
MR. BEAZLEY: Yes, sir.
24
MR. ..GILBRETH: Even though you have less of
25 an instantaneous
~1
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MR. BURRELL: Of course some of the others
1
did indicate that the instantaneous discharge volume would not
2
3
be cover~d"by the requested flare volume. .
MR. BEAZLEY: Yes, sir. The other people
4
5
testifying for the other platforms had benefit of experience
6
with their system, some of them at least. We have none, no
7
8
,experience, and don't have the capability of getting any
experience.
9
MR. BURRELL: You indicated that 4500 per
10
,day--- 4500 mcf per day per month, e£cuse me, might be something
you', d want to dowitho'maintained b~rning; would this lje regard-
11
12
less of wind conditions, regardless of ---
13
14
MR. BEAZLEY: No, sir.
MR. BURRELL: compressor operations or ---
MR. BEAZLEY: I would leave ,that at the .,dis-
16
cretion:':!of the: ,operations supervisor and would leave it up to
him. The maximum volume I would say would be contingent upon
18
bad conditions for thirty day&'a month.
19
MR. BURRELL: Uh-hmrn. In other words, ---
20
MR,. H~RRISON (?) : Gentlemen?
MR. BURRELL: if you didn't have
MR. HARRISON (?) : Could I interrupt this
21
22
23
matter?
24
MR. BURREL~: Yes, sir.
25
MR. HARRISON: You used the term 4500 a month;
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1 I believe that'd be more like 45,000 mcf a month.
2
MR. BEAZLEY: That's right.
3
MR. BURRELL: What? I beg your pardon, okay.
MR. HARRISON: Right.
MR. BURRELL: 45,000, thank you.
MR. HARRISON: Right.
MR. BURRELL: I· can't keep my zeroes straight.
4
5
7
Assuming no unusual wind conditions and assuming the compressors
9
-
~re operating, it's nowhere near this figure,' is that correct?
MR. BEAZLEY: Yes, sir.
MR.' BURRELL: That's all I have, Mr. Beazley~
Mr. 'Gilbreth?
MR. GILBRETH: No 'questions.
MR. BURRELL: Mr. Marshall?
MR. MARSHALL: No.
MR. BURRELL: That's all we have, sir.
MR. HARRISON: Mr. Chairman, at this time
if this matter is now concluded, Mr. Beazley would also at this ~irr
is prep~red to testify concerning the safety flare at the shore-
site, Granite Point Shoresite, which:.is operated, as you know,
by Mobil.
MR. BURRELL. : Thank you, Mr. Harr i son.
MR. HARRISQN: Would you again state your
name and your position for the record and proceed to testify in
this matter, Mr. Beazley?,
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MR. BEAZLEY: My name is Max Beazley,
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2
Associate' Operations Engineer for Mobil Oil Company, Alaska,
3
Producing Division.
(Mr. Beazley's testimony attached as an
4
,exhibit to this transcript.)
5,
MR. HARRISON: Mr. Beazley, do you have a
6 recommendation to give to this Commission today as to the volume
7 of gas for a safety pilot operation at the Granite Point Shore-
S site?
9
MR. BEAZLEY: Yes, I would recommend that
10 this volume be set at 100 mcf per da~ as we are now flarin~with
11 the fifty per cent tolerance to take ,care of, variability in
12 conditions.
(
13
MR. HARRISON: Mr. Chairman, that concludes
14 Mr. Beazley's testimony as to the Shoresite flare. He will now
"15 be responsive to any questions.
16
17 Gilbreth?
MR. BURRELL: Thank you, Mr. Harrison. Mr.
18
MR. GILBRETH: Mr. Beazley, I'd be interested
19 in hearing the reason that 'you need the flare at the Granite
20 Point Shoresite? Can you tell us where the flare is located
21 with respect to the battery an~ the other facilities, personneL
22 quarters, and what have you?
(
23
MR. BEAZLEY: Yes. Our normal flare was
24 located below the battery, closer to the beach than our facility;
25 it's presently out of service. It's identical to the flare
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1 that's on thè platform except that it's vertical. The flare
2
we're using now is, in our burn pit in the waste water pit, and
3
we're using it there until the other flare can be ~ut back in
4 service. It was damaged by frost heave during the winter. We
5
have ,to burn this much'gas in order for the same reasons as the
6
flare on the platform, in order to' maintain a flame so that we
7
can burn gas if it is accidentally vented. ,This volume requirëd
here is much smaller because --~ as others have testified,
8
9
because of the location of it, the smaller volumes of gas, and
the lower pressures.
MR. GILBRETH: What about the remoteness of
12
the flare; could it be moved far enough away from all the~faci-
13
lities so that it wouldn't be necessary to burn it, or would it
14 still create a hazard?
15
MR. BEAZLEY: I believe it would still create
16
a hazard because the flare would still be in one relative
17
position to the facilities, and if th~ wind were adverse, it
'could still create a hazard for the~iving quarters that are
18
19
attached to the facility.
20
MR~ GILBRETH: How far away is your flare now
from your living quarters and other equipment and how fa~ must
21
22
you get the permanent flare fixed?
MR. BEAZLEY: Our flare now is approximately
23
24
--- I'm guessing at this number --- five or six hundred feet
25
from the living quarters, and it will be as much as a thousand
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1 feet when it's installed permanently.
2
MR. GILBRETH: How about from your other
3
tank battery equipment?
4
MR. BEAZLEY: It's closer to the tank battery
5 equipment, but is still a distance, I believe, of about three
6
hundred feet. The permanent' flare will be a distance of about
7 six hundred feet.
8
MR. GILBRETH: On your present platform
hookup, do you anticipate any surging under emergency conditions
9
of gas or oil volumes coming to shore that would overload your
equipment onshore?
MR. BEAZLEY: No, sir, I anticipate no
problems in that respect.
MR. GILBRETH: That!s all I have.
MR. BURRELL: Mr. Marshall?
MR. MARSHALL: ' Mr. Beazley, I believe you
mentioned that your flare arrangement was similartto that which
'was on the platform. I didn't quite'understand this. Does this
mean your --- you have a 'similar type of flare tip, or was this
just some other mechanical arrangements?
MR. BEAZLEY: No, the flare tip at the Shore-
site is identical to the tip on the platform.
MR. MARSHALL: That is it's a National Air/Oi~?
MR. BEAZLEY: No, the existing flare, which
is a Zinke
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MR. MARSHALL: ah.
2
MR. BEAZLEY: But it is placed in a vertical
3 position..
4
MR. MARSHALL: I see, thank you. Does it
5 seem to operate in a better fashion in a vertical position than
6 on the platform mere I assume it's angled steeply away?
7
MR. BEAZLEY: Yes. The flare on the platform
8 is angled a~ a forty-five degrees, and in my own personal
9 experience I know of no difference between the two.
10
MR. MARSHALL: I see, thank you.
MR. BURRELL: Is that all, Mr. Marshall?
11
12
MR. MARSHALL: That's all.
13
MR. BURRELL: Mr. Beazley, in connection with
14 your testimony on the production site as well as the production
. '15 pIa tfo+"m, would it be fair is I revise your request and say
16 you're asking, for production site 150 mcf per day and platform
17 1500 mcf per day
18
MR. BEAZLEY: That would be sensible.
19
MR. BURRELL: --- averaged monthly ,at that
20 rate?
21
MR. BEAZLEY: Yes, sir.
22
MR. BURRELL: Because that's the way I read
the other number, plus fifty per cent discret.ion..
, MR. BEAZLEY~ That' would be acceptable, yes.
MR. BURRELL: In other words, the fifty per
23
24
25
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1 cent you wou~dn't mind if we allowed you to go dówn with it,
but it would be below,
2
3
MR. BEAZLEY: No, sir, that's ---
4
MR. BURRELL:
fifty per cent in the
5 lower direction.
9
MR. BEAZLEY: --- that's correct.
MR. BURRELL: That's all I' :.hav:e. Thank you.
MR. BEAZLEY: Thank you.
MR. HARRISON: Thank you very much.
MR. ANDERSON: Mr. Chairman, as I indicated
6
7
8
10
11 earlier, we'll continue with Granite Point and yield to Mr.
12 Ralph C. Crews, attorney for AMOCO Production Company, who will
t
13
introduce his witnesses.
14
MR. BURRELL: Thank you, Mr. Anderson.
'15
MR. CREWS: I'm Ralph Crews of the law firm
16 of-Crews and OWens, representing AMOCO. Our testimony here today
17 will concern Order No. 102 concerning Bruce and Anna platforms
18 ,at Granite Point, Order No. 105 concerning platforms Baker and
19 Dillon in Middleground Shoal. Testimony will be given in three
20 parts. Mr. Millard Owens will testify as'to the schematic dia-
21 grams of the platforms; Mr. Bart Giles will testify as to the
22, gas,needed'for the safety pilots; and Mr. Owens will then again
(
23 '
'testify as to the f lare ~:or~..the' safety' pilot- needed-: .on the East
24 Foreland.
25 Mr. Owens will be the first witness and has not testified
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previously before this þody, so we'd li~e to ask some prelimina~y.
questions as to his qualifications. Would you state your name,
2
3
please, Mr. OWens?
4
MR. OWENS: Yes, Millard Owens.
5
MR. CREWS: And by whom are you employed?
MR. OWENS: AMOCO Production Company.
MR. CREWS: Arid how long have you worked for
6
7
AMOCO?
8
9
MR. OWENS: Going on ten years.
MR. CREWS: Would you give a brief resume of
your educational background?
MR. OWENS: I receivèd a degree of Petroleum
Engineer from the Colorado School of Mines in 1962.
MR. CREWS: And would you give a brief resume
of your work experience with AMOCO and particularly that in the
Cook Inlet Oilfield?
MR. OWENS:, I started work for AMOCO Production
Company immediately upon leaving college in Wyoming and worked
in three different areas in Wyoming, working with drilling,
completion operations, workovers, waterflooding, steamflooding,
gas handling, gas process, ,w9rk in gas plants, attended a school
for process engineering for the company, in the year 1965, then
moved here to Alaska in August of '66 and"have been here working
in this area ever~"' since. My primary work here has been involved
in the design and layout of production facilities, both onshore
and on platforms, with artificial lift equipment, Kobe and gas
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1 lift, and al~o with waterflood installations and the current
gas handling equipment.
2
3
'MR. CREWS: Are you a member of' any pro-
4 fessional associations?
5
MR. OWENS: Yes, I am a current member of
6 the S. P. E. of ~'..:I .·M~E':;~ ~
'7
MR. CREWS: We offer Mr. OWens as an expert
8 witness.
9 Without objection, we'll accept
MR. BURRELL:
Mr. Owens as an expert witness.
you?
MR. OWENS:
Yes, sir, I was.
10 You were sworn earlier, weren't
11
12
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13
MR. CREWS: Mr. Owens will offer his testi-
14 mony in narra ti ve'.
. '15
MR. OWENS: The exhibits that were just
16 handed to you are labeled One through Four, and they show the
17 £law schematic for the four platforms that AMOCO productión
18 Company operates in Cook Inlet. This is a typical schemátic
19 which covers basically the very sa'me thing we've shoWn on
20 those drawings, except there are a few modifications ~r changes
21 between, the systems that we will note as we go through this.
22 In looking'_ at our flow schematic, we bring our produced
<.
23
crude into a production separator at roughly sixty pounds pres-
24 sure which we then separate off the gas which comes off and goes
25 into the gas handling system on the platform. This system is
~1
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~ with
split into two'parts,/one part being the high pressure gas that
2
then is carried on into a scrubber, from the main scrubber into
'3
a secondary scrubber,· and then into a gas compressor, and from
10
11
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4
the gas compressor into a cooler, from the cooler to a scrubber,
5
from there into a glyco: dehydrator, and from that point it is
6
either shipped to the beach or used as fuel. You'll note that
7
we do take off from there for high pressure fuel; this is pri-
8
marily used for the fuel for the turbines that are used to
9,
I
power the various equipment on the platform. Backing up to
this point ahead of the gas compressor facilities, we then have
a line taking any of the other gas that we feel we need on the
platform to, go to our safety pilot coming off and purging these
12
13
lines, keeping a purge that goes through a knockout drum, and
14
from there into the såfety'pilot.
Also feeding into this is gas that'comes from the pre-w~ter
16
knockout which takes the ---- any gas that comes off at this
17
point which is lower pressure gas, feeds this into the system,
18
and it goes to the safety pilot also. Then we have a separate
19
system that is the tank vent system, taking gas off from the
surge tank on the platform, feeding this gas into a ~eparate
21
knockout drum, and this in turn goes to the flare for the safety
22
23
pilot. These two flares are designed such that the one flare
here for the tank vent system is angled over into the path of
24
the high pressure flare at-the,tip~ Now, these flares --- these
25
flare lines come off as one single flare boom on all four of our
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1 platforms, so we do have only one single flare boom with pri-
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marily the two lines here going out that flare boom. We do not
3 have a pilot light as such separate from this .~]e use the flare
4 lines themselves as the means of keeping the flare lines --- the
5 flare burning.
6 One of the 'primary reasons for this is that we feel that
7 these lines must'be purged at all times to be safe. We cannot
8 leave them dormant; therefore we carry gas through them at all
9 times, and the pilot gas that we will be asking for consists of
10 the gas combined between these two flare tips.
11 Looking at your schematics that you have there, you'll
12 notice that the Anna, Bruce, and Dillon platforms follow this
(
13
primary design;' the major difference in --- the only' difference
14 ~ between
in those three platforms is that on the Dillon
15 platform we have a --- or actually preparing to install a
16 reciprocating compressor which will handle the gas, whereas the
17 other platforms have Solar driven re'ciprocating compressors
18 centrifugal compressors, pardon me. Then if you'll look at 'the
on
19 Baker platform,/that particular platform we have a Worthington
20 gas lift compressor at that position where we do take the gas up
21 to a thousand pounds pressure to use tâ:'s'·:: gas lift. Now, this
22 is the only basic difference in the flow schemes of the four
(
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platforms" and that essentially covers this part of the pre-
24 sentation.
25
MR. BURRELL: Thank you, Mr. Owens. Does
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i any member of the Committee have any questions of Mr. Owens
2
'3
at· ,this time?
MR. GILES: Why don ~,t I continue, sir,
MR. BURRELL: Fine.
MR. GILES: --- and then you can ask us both
4
5
6
questions.
7
MR. BURRELL: All right.
8
MR. GILES: Bart Giles, AMOCO engineer at
'.Denver. And at the outset I should say that I too am testifying
9
10
on Conservation File 102, Granite,Point, and 105, Middleground
11
Shoal. '
12
'Gentlemen,' safety is the most important factor; we've got
13
to protect personnel and the platform. We have from eight "to
14
as many as forty people living on the platforms at one time, and
15
their safety is of utmost importance. We have extensive sys-
16
terns of gas and fire detection and alarm, automatic fire suppressic
by dry , chemical Taylonwhich is a smothering gas and/or C02 and
water deluge; all these have been installed on each of the plat-
forms,to ensure safety of operating personnel. A safety pilot
17
18
19
20
is necessary to ensure that any gas released by relief'valves or
21
during star~up and shutdown of equipment will be burned and
22
cannot create an explosive atmosphere on the platforms.
23
Now, as to the volume necessary fora safety pilot and how
24
we selected it. An average flare volume of 700 mcfd seems
25
advisable in our opinion at each of our four platforms. It's no-:.
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1 based on any~good, practical expèrience, but based on what our
(
2
p~atforrn operating people feel they can live with to keep the
3 pilot lit under adverse wèather and: wind conditions. There is
4 unfortunately no reliable technical method' available to design
5 or calculate the minimum volume under such conditions, and there
6 are no precedents established elsewhere; I'm afraid you've heard
7 this same tune earlier today.
8 Since we handle less than 10,000 mcfd on any of our
9 platforms, including both gas lift gas and produced gas, we
10 are not concerned with blowing out the pilots during an emergency
11 ~ituation where all gas must vent temporarily through the pilot.
12 Now, experience ,in operating under a 700 mcfd saféty pilot
(
13
demonstrates to our platform operating people that it's not
14 ,enough of a~ average volu~e to be safe, so gentlemen, weill
15 be back; we'll request administrati~e approval for a greater
16 pilot flare, without, we trust, the need for another full blown
17 hearing, unless there be objections during the custo~ary ten
18 day protest period. We're making investments to handle the gas
,19 and get it to shore, so it would be illogical, unwise, to flare
20 more gas than is absolutely necessary; it'd just make good sense
21 to recover as much through revenue as we can of thìs investment
22 tha t we I ve made.
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So, in sum and substance, we are saying' that. a sufficient
24 volume safety pilot to assure safe platform operations is a
25 must in our view. On the other hand, we can' respect the fact
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1
that
well, at least we imagine that you'll be looking to
2
keep the flare pilot to a minimum to satisfy whatever needs
3 you may feel you have. But whether we consider that 700 mcfd
4
a maximum or a minimum, we think the 700 is a practical average
5
that should satisfy both considerations. We're talking about
6
an average over a monthly period.
7
MR. BURRELL: Thank you, Mr. Giles. Mr.
8 Gilbreth?
9
MR. GILBRETH: Mr. Owens,
MR. CREWS: Mr. Owens has somemore testimony,
if ---
MR. BURRELL: Oh, okay.
MR. CREWS: --~ you'd 'like to wait until
14 he t~rmina tes .
·15
16
17
19
20
21
22
(
24
25
....... 1
MR. BURRELL: Sure.
MR. OýŒNS: My name is Millard Owens again,
18
and I would like to present her~ briefly what we feel is a
minimum safety pilot for the East Forelands DE~livery Facility.
At the East Forelands Delivery Facility we are handling the
production from the Anna, Bruce, and Dillon platforms.; we do not
23
handle the Bakerpcoduction, this goes through Shell operating
facility. Now, this total production amounts to right at 13,000
, ' \
barrels of oil per day current rate. Now, also as soon as the
production facilities are put in to handle the gas, we will at
that time be handling in the neighborhood of 12-15,000 mcf per
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1 day of gas through thatpfaci~ity-also. This gas will be brought
2
in to some scrubbers at the facility and there transferred to the
3
pipeline, for sale. We presently have a flare at the shore
facility where we are taking the vapors frpm'the pre-water
4
5
knockout and the treater and we also pipe our relief lines into
6
that flare, and we feel ,that we need a minimum of 100 mcf per
7
day on a monttüy average for a safety pilot for this flare at the
8
East Foreland Facility. This is basically what we're asking for
9
in that" 'respect.
MR. BURRELL: Does that conclude the AMOCO
testimony?
12
MR. CREWS: Yes, sir, it does.
13
MR. BURRELL: Mr. Gilbreth, do you have any
14
,qu,estions?
15
MR. GILBRETH: Yes. Since most of your plat-
forms are essentially ,identical, at least for the purposes that
17
we're talking about here, is there any way in which the gas goinç-
18
to the flares for safety pilot purposes can be measured on any
19
of your platforms?
MR. OWENS: No, we do not have the 'means of
doing that.
MR. GILBRETH: You would propose determining
23
the
this/way everybody else has, by a matter of deduction?
MR. OWENS: Yes, sir, that is correct.
MR. GILBRETH: The 700 mef per day that you've
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1 asked for, that would be the sum or the tota~ ~lare for the
2
platform and not' for'each of these 'lines goin9 into the safety
pilot, would it, 700 total?
3
4
MR. OWENS: Yes, sir, that is correct, it
5 - would be total.
6
MR. GILBRETH: Do you have any history on
your platforms that might indicate to you that this 700 is a
7
8
reasonably good figure, or is it something that's been pulled
9
out of the air?
MR. OWENS: Well, I think we have somewhat
of a feel on the Dillon platform, but that's the only one of
12
the four.
13
MR. GILBRETH: The rest have all flared in
14
excess of that':--':"
MR. OWENS: That's correct.
16
MR. GILBRETH:
in the past? What
17
could you tell me what the~proximate size and length of your
18
flare booms are?
19
MR. OWENS: Yes. ~n the Anna, Bruce, and
Dillon platforms, they are twelve inch lines; each 'one of the
21
two flare lines going out are twelve inch, and they are approxi-
22
mately a hundred feet long. Now, these are swedged down at the
end: the high pressure flare is swedged down to eight inch,
23
24
and the tank vent flare is swedged down to six inch tip. We
25
also have a shroud that we had designed to put around the flare
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1 tips in order to help prevent the wind from blowing it out and
2
also to enhanqe the combustion to --- in order that we do have
3 a smokeless flare.
4
MR. GILBRETH: Your gas production, I'm sure,
5
in the past has been a little greater than it is now. Do you
just
have any idea/offhand what the ,maximum volumes you've handled
6
7
were?
8
MR. OWENS: Somewhe're probably in the
9
neighborhood of 13,000,000, I think, is the most that we've
10
handled.
12
MR. GILBRETH: 13,000,000 a day?
MR. OWENS: Approximately, :'·right. That
13
would be my estimate.
MR. GILBRETH: I think that's all I have
right now.
MR. BURRELL: t-lr . Marshall?
MR. MARSHALL: The shroud which covers your
14
16
17
18
flare tips or which is installed on~,-i:.hem, you say this åssists
19
in creating a more smokeless situation in the burning process
and it also serves to help prevent the wind blowing them out;
is this a --- sort of a fabrication made by AMOCO produc.:tiòn"
or is this a commercial tip of some sort?
23
MR. OWENS: This is a locally-'fa1:>ri(:ated
device that we 'had designed ourself and had built locally, and
the primary purpose of it is to pro~ide a venturi effect to
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1 draw additional air into the stream and to. provide a more
2
smoke free flare, but also at the same time it does provide
3 some wind protection for it, yes.
4
MR. MARSHALL: Does the burner tip --- is the
5
attitude of the burner tip approximately the same as that of
6
the vent pipe?
7
MR. OWENS: No, we come out on the vent
8
pipe at an angle. In other words, the flare lines themselves
are at an angle, but when we get to the end, we turn them up
9
for probably about a three foot section, and then this shroud
is placed around that tip, and that is where we also reduce the
size at that point.
MR.· MARSHALL: Thank you.
MR. BURRELL: Is that all, Mr. Marshall?
MR. MARSHALL: Yes. '~,'.::~.; ~
MR. BURRELL: Mr. Owens, you mentioned
a 13,000,000 figur~; would you tell me what that was again, the
18
maximum gas you'd handled?
MR. OWENS: ~i ell,
MR. BURRELL: Was that per platform; is that
mcf per day; would you explain what that is?
MR. OWENS: That would be for anyone plat-
form at a maximum capacity of oil production which was several
23
years ago.
MR. BURRELL: And at that time the maximum
25
any platform handled was 13,000,000 cubic feet of gas per day,
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1 iSi'that. right?
2
MR. OWENS: That is correct, but that's an
.3 estimate~
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4
~. BURRELL: Yes, I understand that; it's
5
just a pocket figure. But that's for one platform?
6
MR. OWENS: That is correct.
MR. BURRELL: That_' s all I have.
MR. CREWS ': Mr. Owens, were AMOCO's five
7
8
9
exhibits prepared by you or under your supervision?
MR. OWENS:, Yes, they were.
MR. CREWS: We offer the exhibits into
evidence, Mr. Chairman.
MR. OWENS: We're calling the small set
One, Two, 'Three and Four,'and we're calling the master graph
there that's kind of a typical sketch No. Five.
MR. BURRELL: Well, why don't .we just accept
One through Four into evidence, if that's acceptable, and tell
l.
you --- let you keep your margin:.' since ---
MR. OWENS: That's fine.
23
MR. BURRELL: --- they're virtual replicas of
that.
~R. OWENS: Yes.
MR. CREWS: The four are accepted?
MR. BURRELL: The four are accepted as
AMOCO Exhibits One through Four.
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MR. CREWS: That concludes AMOCO's testimony.
2
MR. BURRELL: Thank you very much, gentlemen.
3
MR. ANDERSON: Mr. Chairman, testimony for the
4 final two platforms in the Middleground-Shoal Field will be
5 presented by Shell Oil Company, and Mr. Joseph Rudd who is
6 attorney 'for Shell oil Company will introduce his witnesses.
7
MR. BURRELL: Thank you, Mr. Anderson.
8
'MR. RUDD: We have just one witness; it is
9
A.O.P. Casparian, Division Mechanical Engineer for Shell from
Los Angeles. Mr. Casparian h~s qu~lified before and'of course
testified yesterday~ We will have one exhibit; a large version
of it is posted on the bulletin board; we'll distribute small
copies for your use' during his' ,testimony, and at the end Mr.
Casparian will give you a' similar small size copy with colors
on it which .should b~ the record exhibit.
MR. CASPARIAN: My name is Pete Casparian
with Shell oil Company, Division Mechanical Engineer. Shell
Oil Company is operator for the SAS platforms 'A' and 'c'in
Middleground Shoal Field. Each 'of these two platforms is a
completelyselfcontained oil'producing operation. The Middle-
ground Shoal Field,is under waterflood, and each of our platforms
houses a complete water injection plant. In addition, all
.producing wells on these platforms are gas 1ifted.~latforms·
'A' and 'c' currently produce approximatelY'IO,OOO barrels a,
day of oil each and inject approximately 15,000 barrels a day
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1 water, each one. Produced gas or casinghead gas averages about
(
2
5,000,000 cubic feet per day per platform.
Th~ objective of this hearing today', is-to consider the
3
4 amount of gas necessary to maintain an adequate safety pilot on
5 our production platforms in the Inlet. First I shall discuss
6 why gas needs to be vented; then why a flare is required; and
7 finally the minimum average rate of gas that we feel is required
8 to maintain continued safe operations on our two platforms in
9 Middleground Shoal Field.
10 SAS Exhibit #1 is a generalized and simplified schematic
11 of our, gas handling system on both platforms and is typical
12 for both Platforms 'A' and 'C'.The gas that must be handled
('
13
by this system falls in two categories, which are, one, con-~'
14 ,tinuous gas disposaL and two, intermittent gas disposal. Our
15 operations require continuous disposal of small streams of gas
16 primarily for saf:ety reasons, and this has been pointed out in
17 prior testimòny. The first of these streams is shown on ,the
18 diagram outlined with broWn. I don't kncwwhether you can tell
19 w~ich, stream that is, but --. This is gas from our oxygen
20 st~ipping tower used in our waterflood operations. This vessel
21 utilizes produced gas to remove oxygen from the water being
~ injected in our waterflood operations'. The operating pressure
(
23
of this vessel must be maintained as near as possible to atmos-
24 pheric pressure to minimize the retention'of gas in solution in
25 the water. This gas in solution in the water represents a safety
~1
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1 hazard in that it could'cause cavation in pumping equipment in
2
the waterflood system, and cavation in this pumping equipment
3 could result in explosion or fire. So to attempt to recover
4 the tail gas containing 02 is unsafe and such gas is disposed
5 of.
6 The second stream of continuously disposed gas is a
7 venting of tank yapors'from:the,ondeck tank and the girder
8 tank. Although these two tanks are notusèd,':on a¡ continuous
9
basis for oil handling, they do nonetheless continuously give
off hydrocarbon vapors. These tanks are not designed for
pressurized operations and consequently must ,be operated at or
to. be
near atmospheric pressure. Here agàin, we consider it/unsafe
to attempt to recover these vapors since overpressuring of these
,vessels would be unsafe. This system is outlined in orange on
the ãiagram on the board.
The last stream of continuous gas disposal I will dis-
cuss is outlinéd in red on the diagram. 'This' is the purge
system for all our emergency blowdownlines, which I will dis-
cuss ina moment. As you c~n see on the diagram, we have
several relief lines going ~o our flare boom. Each of these
23
lines is continuously purged with gas to ensure that air does
not enter into the line and create an explosive mixture. This
purge gas provides flashback protection for all flare and vent
stacks to prevent the, propagation of flame into the flare sys-
tern due to the entry of air. Therefore the purge gas flow must
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1 be high enough to overcome this situation. The installation of
2
any equipment to recover this gas would of course defeat the
3
emergency relief purpose.
4
In addition to the continuous disposal of gas that I have
5
qiscussed, our disposal system must handle some intermittent
6
streams of gas. The first of these is a surge gas system which
7
is shown on in green on the diagram. I mentioned earlier that
8
all of our producing wells are gas lifted. Gas lift wells do
9
not always produce oil and gas at a steady, constant rate. The
heading nature of these wells sometimes causes very high
instantaneous flow rates which may fora short period of time
exceed the capacity of our compression equipment. The function
is
of this system/to dispose of these surges in flow rates. We
do not 'anticipate that this amount of surge gas will be large
since the compression equipment that, we have at present and
that which we are installing to ship our gas to shore is capable
of handling about four times the initial average excess casing-
head gas rate.
The final streams of intermittent disposal gas that I,
will discuss ar~shown in, yellow on the diagram. This system
is the emergency relief system for all pressure vessels and
compressors on the platform. As shown on the diagram, this
23
system consists of several lines from the compressors,separaèörs,
and scrubbers¡, This system is required to avoid' overpressuring"'
, '
of vessels upon equipment malfunction, in addition to blowing
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1
down these vessels for equipment maintenance, etc. As an
2
example, if a compressor were to shut down for some reason,
3
the pressurized gas is the compressor cylinders is immediately
4
vented. -This instantaneous rate is several times greater than
5
the rates of gas being compressed and the piping has to be
6.
7
designed such that the gas can be relieved safely. This source
of gas is not to be considered as part of the safety pilot
8
flare as it occurs intermittently.
9
Other sources of gas that have to be vented that are not
shown on the exhibit are purgingof<oompressors after they have
been down to remove air out of the cylinders; loading compres-
sors, blowing down separators, surge vessels, etc., for equip-
ment maintenance. These amountsagain are small in terms of
total volume.
Ilve discussed so far in detail the need to continuously
and intermittently dispose of gas on our platforms. I will now
di~cuss alternative methods o~ gas disposal and point out why
we consider flaring to b~ the safest disposal method for these
,platforms. As was pointed out in prior testimony, platforms in
Cook Inlet are a unique situation compared to offshore p~oductio~
elsewhere. These platforms are totally enclosed due to severe
weather conditions. A~y gas vent stacks or flare st~cks'must
be located on the platforms due to severe tides and ice con-
ditions in the Cook INlet. Since the gas disposal must be on
the platform and'since the platforms are totally enclosed, we
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1 consider a continuously burning flare to be the only safe method
2
of gas disposal. Venting would release hydrocarbon vapors in
3
close proximity to the enc~osed platform, which in turn could
4
cause an unsafe condition to exist due to flammable gas mixtures
5
occuring at the platform. Thus this safety pilot has to be in
6
operation all the time under varying wind and temperature con-
'1
ditions such that instantaneous discharg~ of gas at high'rates'
8
will be safely burned.
9
I have reviewed with you the gas disposal systems on our
platforms and discussed the reasóns why we must have a pilot
flare burning at all times to maintain a safe operation. Adequa~e
12
technology and experience exists for the design of gas disposal
systemssùch as I have described. We feel that we have a well
13
14
designed and safe gas d~sposal system on our platforms which
ensures the.:safestoperation~ 'I have stated: that :it ,is imperative
15
16
that we have a pilot flare burning at all times to ensure the
17
safe release of this disposal gas; however, the volume of gas
18
required to keep a pilot flare burning under varying wind and
19
platform operating conditions is not readily predictable with
the technology that exists today.
21
To conclude, I wish to state that the SAS Group has made
22
a very large investment to comply with Conservation Order NO.
23
105. The economics as we've discussed and presented to you on
several previous occasions are quite poor and we do not expect ,
of
to recover all/our investment. It is therefore to our advantage
24
25
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flare
1 to minimize the safety/pilot, consistent with good safe operating
practice to maximize the volumes of casinghead gas sold and ,hence
2
3
recover a larger portion of our investment. I therefore questio~
4 the necessity that the minimum gas rate for a safety flare be
5 set by the Conservation Committee, rather than to a.llow each
6 operator to set his own limit consistent with his operations.
7 You heard yesterday that industry overall has spent several
8 million dollars and considerable engineering to comply with the
9 no-flare order, and I feel quite çonfident that they would wish
10 to maximize their return on their, investment and hence not dis-
11 pose of 'any gas to flare other than that req~~red to maintain
12 continued safe operations. However, if the Alaska Oil & Gas
,(
13
Conservation Committee' reaches a different conclusion based on
14 ~estimony, Shell oil Company, as operator for the SAS Group,
, ·,15 requests that the minimum monthly average of 700 mcf per day
16 be set as' a permissible gas rate for a safety pilot per plat-
" form, for our,MGS Field operations. We do not presently' flare
18
any gas in our onshore operations; how'ever , if conditions change
inthe future which may necessitate the flaring of gas ~ we wish
to request 100 mcf per day for our onshore operations as a
19
20
21 safety pilot. We of course intend to make every effort to
22 minimize the amount of gas f~ared, but if we find that a, ,larger
(
23 ,
gas rate is required to maintain safe operations, we would plan
24 to request a variance to the order and request that this be
25 made on an administrative basis. Thank you.
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1
MR. RUDD: Mr. Casparian, in connection with
2
SAS Exhibit #1, was that prepared by you or under your super-
3 vision?,
4
MR. CASPARIAN: That was prepared under my
5 supervision.
6
MR. RUDD: We would ask that that be admitted
7 in evidence, and we'll give you the colormpy to include in the
8 record.
9
MR. BURRELL: Thank you. 'We'll accept that
10 in the record. I understand
11
MR. RUDD: Excuse me?
12
MR. BURRELL: ---that's the same one as the
13
one on the wall?
14
MR. CASPARIAN: That is correct.
15
MR. RUDD: Just the legend is moved to, the
16 center of the, page, but ---
17
MR. BURRELL: Oh.
18
MR. RUDD:. --- the diagram is the same.
19 '
MR. BURRELL: Thank you. That will be given
20 to us?
21
MR. RUDD: That will be ---
MR. CASPARIAN: Yes, sir.
MR. RUDD: given to you at the close of
22
23
24 the session.
25
MR. CASPARIAN: They'll be just the same as
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1 you have except in colors.
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MR. BURRELL: Mr. Gilbreth?
3
MR. 'GILBRETH: Mr. Casparian, your recom-
4 mendation for the 700 mcf, is 'that based on actual experience
5 that you people have gained, or is this an estimate of what you
6 think will be necessary?
7,
MR. CASPARIAN: This is an estimate on what
8 we think is necessary. The --- we tried to arrive at' it:,'from
9 s;'----. based on what technqlogy has --- or is available. It's
10
primarily the purge rate that we feel, is necessary in our
11
flow lines to keep them safe.
12
MR. GILBRETH: The volumes that are being
(
13
used on your platform are considerably less than some of those
14
,for example ,in McArthur River. Do you have any idea what type
15
of an instantaneous rate you might have on your platforms?
16
MR. CASPARIAN: Well, we did not calculate
17,
it fpr this hearing; however, we did as a ballpark estimate
18
would be on the order of about four to five times the amount of
19
gas that we're compressing and which amounts to some seventy
20
million cubic feet per day as an instantaneous gas rate, but that
21
is a ballpark figure.
22
MR.~ GILBRETH: I don't have any further
(
23
questions.
24
MR. BURRELL: Mr. Marshall?
25
MR. MARSHALL: Mr. Caspar ian, would you please
..... 1
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1 review the nature of the burner tips on your platforms?
(
2
MR. CASPARIAN: The burner tips, we do not
3 have any' burner tips on our flare stack other than ,straight
4 runs of pipe. ,This is --- we feel that the problem that's
5 germane to this hearing is on the minimum safety pilot rather
6 than the reduction perhaps in smoke emission at the present time.
7 We are looking at a safety stack or a burner tip to reduce
8 smoke emission.
9
MR. MARSHALL: The reasæ that· I am interested
10 in the nature of the burner tip is because I believe it could
11 ' have an effect on how efficiently the burner stays lit, and this
12 is the ~---~his'is my reason for the final question. Thank you
'{
13
ver.y much.
.14
MR. BURRELL: I don't have any questions,
15 Mr. Casparia~, thank you, sir.
16
MR. RUDD: Mr. Chairman, that completes the
17 testimony for SAS and; in 'fact all'the testimony that I know of
18 that's plan~ed. I'd like to note in closin~ that all of th~
19
testimony that was given today i~ predicated upon the installation
20
and the operation of the facilities that were described during
21
the hearing yesterday, and we simply want to point out that any
Order entered as a result of this hearing 'sh~uld be coordinated
in time with the Orders resulting from yesterday's ~earings.
22
(
23
24
25
MR. ' BURRELL: Thank you, Mr. Rudd.
MR. ANDERSON: Mr. Chairman, I might just
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1 add if any o~ the operators have any further testimony that they
('
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want to offer that I don't know about.
4
MR. BURRELL: Does that conclude
MR. ANDERSON: Yes.
MR. BURRELL: --- the testimony from the
3
5
6 operators then?
7
MR. ANDERSON: Yes, it does.
8
MR. BURRELL: We'll take a fifteen minute ---
9 well, let's --- well, all right,'we'll take a ten minute inter-
and
10 mission here. We want to do a little talking here, /then'wet ll~'open
11 it up for questions from anybody from the floor.
12 (OFF THE RECORD),
i(:
13
(ON' THE RECORD)
14
MR.' BURRELL: Is there anybody in the audience
15 who has any questions of,' any of the operators or anybody else?
16 Or any statements they have to make? Oh, one thing, yeah, if
18
anybody has any printed copies of their testimony, we'd apprecia-;e
it; we can get it back if it's the only one you've got or some-
thing, but it makes it an awful lot easier when we get to the
17
19'
20 reproduction stage; we'd appreciate it if you'd leave it with
21 Mr. Marshall here when you go on out.
22 I totalled up ali, the requests onshore and offshore; it
.(
23,
adds up to l3~6 million cubic feet per day. The current flares
24 are somwhere 'near ,ninety-five to a hundred million cubic feet
25
per day. So disregarding the Mobil problem, just assuming if
~1
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at all possible,
2
MR. THORNTON: You can't just disregard the
3
Mobil problem.
4
MR. BURRELL: We have to operate off our
Order until the judge tells us differently. That's some fourteen
per cent of the current 'flare, and that would be an improvement,
5
6
7
I think. I don't have anything else. We'll adjourn, thank
8
you.
9
END OF PROCEEDINGS
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MECHANICAL ENGINEERING TESTIMONY
(
My name is Richard Keller, and I am Area Engineer for Union
Oil Company, Anchorage District, Alaska. My purpose here today is to
describe the gas processing system and the need for safety pilots and
to recommend sa fety pil at sizes for the Grayl i ng p 1 a tform.
.~~,~,,:.;.~~"~..,..
The need and justification for safety flares in Cook Inlet oil
and gas platform operations has been demonstrated by the Industry1s ex-
cellent safety record. Hydrocarbon gas may be released through safety
relief systems to the atmosphere instantaneously on these platforlns,
resulting from such things as:
1. Compressor failures
l
2. Excessively high pressure in vessels, piping, and
compressors
3. Line' breaks and leaks
4. Power faï'lure, fuel failure
5. Fire
6. Excessive platform vibration
High-rate gas surges resulting from such upsets cannot feasibly be handled
in furnaces or other enclosed burning equipment. Facilities must be
(
available to allow quick release and safe burning of the excess gas at
an appropriate location. Properly designed safety flares have proven to
be the most satisfactory systems available.
The Cook Inlet platforms are unique as compared with platforms
and production operations elsewhere in the world. The production areas of
these platforms are enclosed, 'because of the severe weather conditions in
Alaska, and typically, large throughput volumes of oil and gas are processed
R. C. Ke 11 e r
5/11/72
(
I~
(
in very compact spaces. The enclosed areas of these platforms are not
swept clear of hydrocarbon vapors by prevailing winds, as is the case on
(
the open platfornls in other offshore areas. The various compartments
on Cook Inlet platforms are continuously purged with fans to vent any
hydrocarbon vapor accumulations which could result in explosive gas mix-
tures inside the platform structµre.
The need for safety flares on land is not as critical since
onshore oil fields are usually laid out over several hundred acres. In
many other offshore areas, platform flares or vents can be located on
adjacent auxiliary structures at a safe distance from the platform, which
also eliminates or minimizes the need for safety pilots.· The water depths
and environment of the Cook Inlet make this type of operation impractical.
(
It is imperative that our safety pilots, located on the platforms, be
operational at all times, under severe temperature variations, high wind
conditions, and minimum flow conditions, such that an instantaneous dis-
charge of gas at high rates will be safely ignited and burned and not be
forced back into the structure through the fresh air purge system.
Union Oil Company operates the Grayling platform in the McArthur
River Field~ Trading Bay Unit. This platform produces over 50,000 BOPD.
We currently compress in excess of 55,000 MCF of gas per day. Approxi-
mately 37,000 MCF per day of this gas is compressed to 1100 or 1300 psig
(
and utilized as artificial lift gas to produce oil wells. The remaining
produced gas is compressed to 250 psig for transportation to shore and
platform fuel usage. This platform also processes and injects over 50,000
BWPD for pressure maintenance of the oil reservoir. I hope you can appre-
ciate that this involves a large arnount of equipment installed in a small
area. All of the Grayling equipment, including two drilling rigs, is
R. C. Keller
5/11/72
-2-
i'r"'-
(
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located on three decks, each approximately 100 feet square.
We have a schematic drawing, Exhibit A, which illustrates the
f
gas flow on the platform as well as the safety relief and flare systems.
Oil and gas from the producing wells enters a combination of
five gas-oil separators. Here the gas is separated from the oil at 50~
psig and enters a common gas mánifold. The gas then goes to one of three
existing compressor packages. We currently have installed a total of
nine, eleven-hundred Horsepower turbine-driven, centrifugal compressors
on the Grayling. We will be adding a tenth 1100 Hp compressor this fall
to increase our gas lift capacity.
The first gas lift compressor package consists of three 1100
(
Hp compressors operating in series. The gas goes through a cooler,
scrubber, then the first stage compressor and is discharged at l50±
psig. The gas then goes through another cooler, scrubber, then the
second stage compressor and is discharged at 450± psig. The gas is
again cooled and scrubbed and is finally discharged from the third
stage compressor at 1300~ psig. This gas is cooled, then piped to the
producing wells where it is utilized in lifting tDe oil and is continu-
ously recycled.
The second gas lift compressor package operates in a similar
manner, except that there are only two stages of compression, and two
t
1100 Hp compressors operate in parallel in each stage. The discharge
pressure of this package is 1100-2.- psig.
The new 1100 Hp compressor which will be installed this fall
will tie into the first stage discharge of the two gas lift packages and
will result in increased gas lift capacity. It will also tie into the
R. C. Keller
5/11/72
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gas to shore system for added flexibility.
The third compressor package is \,,,hat we call our IIgas to shorell
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system. It consists of two 1100 Hp compressors in parallel, and the opera-
tion is similar to the other packages previously mentioned. Gas discharged
from these compressors goes through a cooler, scrubber, than a glycol con-
tactor, which dehydrates the gas prior to shipment to shore. These two
compressors have a combined capacity of 20,000 MCF per day. Solution gas
produced with the oil is currently averaging approximately 18,000 MCF per
day. We can obtain fuel gas for our equipment at the dis~harge of these
compressors. Our current fuel gas requirement on this platform averages
6,500 MCF/D, which is more gas than many platforms even produce.
The Grayling platform, then, has adequate facilities to compress
(
and transport all produced gas to shore, but we do need to main in ade-
quate safety p-ilots on the platform flares. This platform has two safety
flares on it because of the large volume of gas conlpressed and the number
of compressors on board. We feel that two flares are needed here in order
to safely dissipate the tremendous heat evolved under emergency flare condi-
tions. Under emergency, or unscheduled shut-down conditions, when all com-
pressors go 'down and vent at o~ce, it is estimated that an instantaneous
discharge rate of over 100,000 MCF per day is released in a matter of
seconds. Our experience has shown that approximately 1,000 MCF per day
per flare is needed to maintain a safety pilot under adverse wind condi-
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tions such that a sudden gas discharge will not extinguish the flare. If
the flare is extinguished, the, hydrocarbon vapors released could be induced
back into the platform by the various purge fans, thereby creating a poten-
tially dangerous situation.
R. C. Keller
5/11/72
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Union Oil Company is determined to transport all possible pro-
duced gas thrcu0~¡ the new gas gathering system now being constructed and
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to maintain minimum safety pilots on the platform, consistent with sound
safety practices. Of paramount importance to us are the lives of our
people on the platform, but also to be considered is the sizeable plat-
form investment and future prodðction, all of which depend upon maintain-
ing a safe operation.
We therefore respectfully recommend that the Conservation Com-
mittee assign 1,000 MCFjD per flare on a monthly average basis for the
safety pilot sizes on the Grayling platform.
That concludes my testimony.
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R. C. Keller
5/11/72
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MECHANICAL ENGINEERING TESTIMONY
(
My name is Richard Keller, and I am Area Engineer for Union
Oil Company~ Anchorage District~ Alaska. My purpose here today is to
describe the gas processing system and the,need for safety pilots, and to
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recommend safety pilot s'izes for the Monopod platform.
......-_...c::..:;¡: ...c".~~....,.,..,.'
I have testified previously as to why safety pilots are re-
quired on Cook Inlet platforms and will now discuss only the Monopod.
I wish to have my previous general comments rega.rding the Grayling plat-
form incorporated into this testimony.
Union Oil Company operates the Monopod platform in the Trading
Bay Field. This platform produces approximatly 15~OOO BOPD. It also has
(
the capacity to process and inject 65,000 BWPD. As stated yesterday, we
are in the process of installing five new compressors on this platform in
order to comp 1 y vJi tll Conserva t i on Order No. 103. These new compressors
and related equipment should be in operation by September 1, 1972.
We are currently flaring in excess of 7~OOO MCF per day of
casinghead gas on the Monopod because of our inability to compress and
treat all produced gas. We have' not· had the equipment to draw the t,10no··
pod flares down to pilot size, as we have had on the Grayling platform.
Exhibit A is a schematic drawing showing the way our new gas
process flow, safety relief, and flare systems will look when the new
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compressors and related equipment,have been installed.
Oil and casinghead ga~ from the producing wells enters a com-
bination of four gas-oil separators. The gas and oil are separated at a
-1--
pressure of 50_ psig and the gas enters a common manifold. The gas then
R. c. Ke 11 er
5/12/72
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goes through a pre-compressor scrubber to the suction of two 3300 Hp,
turbine-driven, tandem compressor sets. Two centrifugal compressors are
(
driven from each 3300 Hp turbine. Gas enters the first stage compressor
of each set, is discharged at 185 psig, goes through a cooler, scrubber,
then to the second stage compressor and discharged at 500 psig. The gas
from each compressor set is then cooled, combined, and scrubbed a final
time before being dehydrated in the glycol contactor for transportation
to shore. The capacity of these two tandem compressor sets is in excess
of 35,000 MCF per day.
t
Gas lift gas can be obtained either upstream or downstream of
the glycol contactor. As much as 14,000 MCF per day of gas lift gas can
be compressed from 500 to 1100 psig by the 1100 Hp turbine-driven com-
pressor. This gas will be used to artificially lift fluids from the wells
and will be continuously recirculated. Fuel for the platform equipment
will be obtained upstream of the contactor. Platform fuel gas requirements
will be approximately 4,000 MCF per day when the new system is operational.
In view of our current solution gas production being approxi-
mately 15,000 MCF per day, it is evident the Monopod platform will have
more than adequate compression capacity to transport all produced gas to
shore.
The Monopod platform, like the Grayling, has two safety flares
in order to safely dissipate the heat evolved under emergency flare condi-
tions.
{
It is estimated that with the new system operating, an instan-
taneous flare discharge rate of 178,000 MCF per day would occur within
seconds after a total compressor shut-down.
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R. C. Keller
5/12/72
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Due to the similarity of equipment, gas compression require-
ments, and flare configurations between the Monopod and Grayling plat-
(
forms, it is anticipated that approximately 1,000 MCF per day per flare
will be required to maintain the pilots in a lighted condition under ad-
verse wind conditions such that an instantaneous gas discharge will not
extinguish the pilots.
The lives of our men on the platform depend upon maintaining
a safe operation.
These safety pilots will be kept to a minimum rate, consistent
\^/ith sound safety practices and all excess casinghead gas will be trans-
ported ~o shore for disposition.
We, therefore, respectfully recommend that the Conservation
(
Committee assign 1 ,000 MCF per day per flare, on a monthly average basis,
for the safety pi 1 ot si zes on the ~~onopod p la tform.
That concludes my testimony.
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R. C. Keller
5/12/72
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ENGINEERING TESTIHONY
ATLANTIC RICHFIELD COHPANY
ALASKA OIL AND GAS CONSERVATION CO~lliITTEEHEARING
MCARTHUR RIVER FIELD--CONSERVATION ORDER NO. 114
MAY 12, 1972
{'
Atlantic Richfield Company operates Platform King as a suboperator in the
Trading Bay Unit of MeArthur River Field. Exhibit 1 shows the location
of this platform in relation to the other platforms in the field, the
outline of the field based on the approximate productive limits, and
Trading Bay onshore 'production facilities. Platform King production comes
from t'en wells wi th twelve completions in the "G", Wes t Forelands, and
Hemlock pools. Daily production is 26,500 BOPD, 2200 BWPD, and 8500 }lCFPD
of gas. A rotative gas-lift system provides 23,000 MCFPD of high-pressure
gas for artificial lift purposes. Apprdximately 70,000 BPD of filtered and
treated Cook Inlet water is injected in four wells on the platform as a part
('
of the field's waterflood program.
~latform King has two enclosed deck levels measuring approximately 110' square.
.
Referring to Exhibit 2, equipment on the platform includes oil and gas separ-
ation equipment, two 2125 HP Worthington Mainliner compressors, one 1100 HP
Solar-York centrifugal compressor, one 6000 HP Nordberg turbine-powered water
injection pump with related water filtering equipment and deaeration tower,
two 1250 ~v electric generators powered by Ruston turbines, two 1500 KW
generators driven by General Motors diesels for rig power and standby, one
350 HP boiler, and a variety of other related producing and drilling equipment.
Normal manpower on the platform without rig operation is about 25 people.
(
The flare system on Platform King consists of thre.è flare lines. A twelve-
C'
inch low-pressure flare handles gas flashed from the first-stage suction
scrubbers of the Worthington Mainliner compressors and oxygen enriched gas
from the deaeration tm.¡er. The main flare system, or high-pressure flare
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system, isa 24-inch flare boom that handles gas relieved from the system
between the oil and gas separators and the compressors. This system provides
the primary relief in the event of a surge in production, compressor shutdo\vn,
electric power failure, or other upset in the facilities. ,A third linê 12
inches in diameter ties into the pressure relief valve and rupture disc systems
throughout the production facilities. A John Zink clean-burning flare tip
installed on the high and low pressure flares is designed so that the burners
on these two flare systems are separated by several feet at the end of the
flare boom. Proper operation of these clean-burning flare tips requires the
use of aspirator gas equivalent to about 30 percent of the total flared volume
at minimum safety pilot conditions.
As the d~scription of the King Platform and its equipment indicates, platforms
in the Cook Intet \;a~ers are extremely· complex and rather lIDique in design.
They are relatively small compact platforms that are heavily laden with equip-
merit. The equipment is quite reliable, but any equipment is subject to failure.
)
Due to climatic conditions, the platforms in the Inlet are almost fully enclosed
This is somewhat different from the normal open design for most other offshore
areas. Extensive measures must be taken to prevent dangerous concentrations of
gas in inclosed platform areas to minimize the accompanying risk of fire or
explosion on a platform. The unique conditions in the Cook Inlet also reqUl.re
that . many' systems which are separated where conditions permit are in this case
all contained on a common platform. It is common practice in other areas to
have'separat~on equipment, compressors, and fired vessels separated. Safety
fea~ures must be quitè extensive to protect lif~ and property in any offshore
operations. There are obviously some special" considerations for the Cook Inlet
type of operation. Provisions must be made for the safe release of gas when
there are surges in produc tion which cannot be otherwise handled or \V'hen there
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are shutdow.ns due to'mechanical or electrical failures. Production
surges are especially common'in gas lift operations. The ?pecial,con-
siderations diseussed make it necessary that all pressure release of
J
gaseous vapors be gathered and carried to a remote flare for complete
combustion in order to protect the platform, its occupants, and equipment.
The minimum safety pilot volume is undoubtedly related to many factors
including but not limited to equipment complexity, total system design,
system'volumes, and flow rates handled. However, ,there is no precedent
or generally accepted engineering procedure for establishing a minimum
safety pilot size for operations having the unique design and operating
"èonditions of the Cook In~~t platforms. The minimum volume must ensure
that a pilot will be maintained during variable wind conditions and provide
positive ignition of any sudden release of gas caused by an upset or failure
('
which brings about an excessive pressure in any system. Our recommended
..
mi~imum safety pilot size is based on the judgment 'of experienced operating
)
personnel who are thoroughly familiar with the daily operations of this
platform. It also gives full consideration to the need for minimum flare
yolumes from platforms in the Inlet under existing Conservation Committee
orders. On this basis, we recommend a safety pilot volume for King Platforlli
"
of 800 MCFPD on a monthly average basis.
Exhibit 3 shows a schematic drawing of Platform King's facilities with gas
'volum~s for operation under minimum safety pilot conditions. Under these
{
operating conditions, 31',940 HCFPD of gas is flashed from the oil and gas
separators. This volume includes gas-lift gas, solution gas, flash of
,(
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'..' .~,.'.:"~,_, ..1f~~i~"S fro'm all scrubbers throughout the system operating at a higher
. près'sure, 'and flash" gas from the crude surge tank. Gas from the crude surge
tank is not now being compressed and put back into the inlet gas stream,
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but we plan to convert an existing compressor on the platform to this
service. The minimum safety pilot volume of 800 MCFPD is sho~yn on this
(
diagram. The remaining produced gas from the separators totaling 31,140
MCFPD is delivered to the suction of the compressors. 7140 MCFPD of this
gas goes to the Solar-York booster compressor which discharges at about
300 psig. 3500 MCFPD of the gas from the booster compressor goes to the
fuel system. This includes gas used for the Ruston turbine-powered gener-
ators, the Nordberg turbine which ~lrives the water injection pump, the
Solar turbine powered compressor, steam generation equipment, boilers,
filter flush, and deaeration for removal of oxygen from injected water.
Fuel, for the Worthington compressors is being supplied by gas-we11 gas
due to detonation and maintenance problems that have been experienced with
(
casinghead gas fuel. We are currently working with Worthington represent-
atives in an effort to modify the Worthington fuel system so thétt these
comPressors will also operate satisfactorily from the casinghead gas fuel
)
system. The remaining 3640 }1CFPD of gas discharged from the Solar-York
compressor will be delivered to shore to be processed by the Trading Bay
production facility Liquid Extraction Plant and subsequently compressed
for delivery to the gas pipeline now being constructed by Union and
Marathon. Referring back to the compressor suctions on Exhibit 3,
24,000 MCFPD of gas from the primary separators is delivered to the two
Worthington Mainliner compressors. These compressors serve the rotative
gas-lift system. The suction volume is reduced by 1200 MCFPD due to shrinkage
t
from condensation in the compression process. The remaining 22,800 MCFPD
of gas discharged from these compressors is returned to the gas-lift system.
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In summary, I have discussed the highly complex, compact, and enclosed
con~itions that ·make Cook Inlet platforms unique. Although the equipment
onbo~rd King Platform is capable of theoretically handling all produced
casinghead gas without a flare, the unique nature of the platform makes
it essential that a safety pilot be maintained for safe operations. To
provide this safety, the pilot must ensure positiÿe ignition of any sudden
release of gas to the flare system. We found no precedent or commonly
accepted engineering practice for calculating a minimum safety pilot size
for the unique Cook Inlet type of operation. Our recommended minimum
safety pilot size is a balance of the judgment of our operating person~el
who are most familiar with the platform and the recognized necessity for
minimum flare volumes from platforms in the Cook Inlet under existing
Conservation Committee orders. Atlantic Richfield Company respectfully
requests the assignment of a safety pilot volume of 800 MCFPD on
an average monthly basis' for the King S~lmon Platform.
That concludes my direct testimony. Thank you for your attention.
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SHORE SITE TESTIMONY - MAX BEAZLEY
.(
Treatment of the crude ·oil at the Granite Point Shore site involves heating
and weathering, so some gas must be handled at atmospheric pressure.
At the present time, the gas evolved in the weathering is burned in a
shore site flare. This gas is not measured, but is thought to be less than
100 MCFD. Vent añd safety relief valves are also connected to this flare
system so in the event of mechanical shutdown or overpressure, sub-
stantially more than this amount can be flared.
The only gas handled under pressure at the shore site is an average of
1,000 MCFD of gas sold to ARCO and about 200 MCFD used for fuel. The
fuel gas is used for heat, in the crude oil heater treater, and the glycol
heaters, ãnd for fuel for power generation, instrument air 'compression,
and crude oil pumping.
(
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SIMPLIFIED FLOW DIAGRAM
TYPICAL PLATFORM GAS DISPOSAL SYSTEM
CO. II~
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EXHIBIT t
AtlanticRichfieldCompany <>
McARTHUR RIVER FIELD HEARING
MAY 12, 1972
lOCATION MAP
EXHIBIT 2
AtlanticRichfieldCompany <>
McARTHUR RIVER FIELD HEARl NG
MAY 12, 1972
KING SALMON PLATFORM
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EXHIBIT 3
AtlanticRichfieldCompany <>
McARTHUR RIVER FIELD HEARING
MAY 12,1972
KING SALMON PLATFORM
GAS BALANCE
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KING SALMON PLATFORM
PLAN VIEW
JOHN ZINK SMOKELESS FLARE
TIPS and PIPING DETAILS FOR
FLARE BOOM
(
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TRADING BAY FIELD HEARING
MA Y 12, 1972
ATLANTIC RICHFIELD COMPANY
EXHIBITS
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EXHIBIT I
AtlanticR ichfieldCompany(>
TRADING BAY FlELD HEARING
MAY 12,1972
LOCATION MAP
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A tlanticR ichfie IdCom pany
TRADING BAY FIELD HEARING
MAY 12,1972
PLATFORM IIA"
SCHEMAT I C DIAGRAM
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-
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WELl\-\EðD t200M to.10, ~
--i ¡-----. ~ I
A-t --+ ~-1
-H---~ ,- ~
-H---~ ,,- I)
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..
------/"')J"
~ GAS LI..,¡E TO
SHORE
) H.J E: L : rtl
L ---r-; W L '1. '( C:rAC) ~
... í +ORT~I~GTO\.J ~ SCIZW," To L. ~
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EXHIBIT 3
A tlanticR ich Ii e Id Com pany
TRADING BAY FIELD HEARING
MAY 12,1972
PLATFORM SPARK
~~~·U~Mo.TI~ nlå~RdM
.J~
~,
) PA~\é
GAS FROM ~
MOBIL-UNION
750 Mcf/D '
.
,)
TO FUEL
1-:00 Mef/D
,
,..
.
50 Mef/D
--
250 ~f/D
DEAERATION
TOWER
ON -SHORE
FACILITY
430 Mcf/D
þ ~ -
'II
180 Mcf/D
~
.
~"
~,
I EXHIBIT 4
A tlanticR ichfie Id Com pany
TRADING BAY FIELD HEARING
MAY 12,1972
PLATFORMS'Ä1 B SPARK
GAS BALANCE
~
.. GAS FROM SHORE
500 Mcf/D
'f' 900 Mcf/D
J-
12600 Mcf/D
50 Mcf/D
.
---,
..
TO GAS LIFT
3120 McffP
GAS TO SHORE
180 Mcf/ D
)
Oil TO SHORE
120 Mcf/D
)
SPARK
PLA TFOR M
SHRINKAGE ,
700 Mcf/D
~
14200, Mcf/D 'COMPRESSORS'
:>
l
(
LOW PRESSUF£ FLARE
( ATMOSPHERIC)
..
A
PLATFORM
Oil TO SHÒRE
TO FUEL
500 Mcf/D
III
160; Mef/D
SHR,ÌNKAGE
200' Mcf/D
~
4000 MctlD COMPRESSOR
HIGH PRESSURE FLARE
240 Mcf/D
~~,
I
I 4
! PRODUCE D GA S
i ['620 Mcf/D
I i.INJECTED GAS
,12600 Mef ID
-
CRUDE SURGE VESSEL
..
:220 MCf~
,&
PRODUCTION'
SEPARA TOR
Mcf/D
500 Mcf/D
.... ,
f 1~7ÓO MCf(Q
1100
I
......
HIGH PRESSURE
FLARE
SAFETY PIL0,
600 Mcf/D -..
14920 Mcf/D
)
CRUDE ~URGE
TANK
PRODUCED GAS
1080 Mct/D
INJECTED GAS
3120, Mcf/D
þ
't
...
A ~
160 Mcf/O
SEPARATOR
(A TMOSPHERIC')
~' ).
I 4240 Mcf/O '
PRODUCTION ,
..
lOW PRESSURE
FLARE
SAFETY PIL~
400 Mcf/D & À
..
.
4400 Mcf/D
',..-.,
t-)
,..
~
II
;1fJ
~ :.t'-..
-~
AFFID~VIT
STATE OF ALASKA, )
THIRD J,UDICIAL DISTRICT, ) 55.
'. ..Mar-y--L.-Shak.e... ..... ... ...........
being first duly sworn on, oath
she
deposes a,nd says thaL....__........
is the....~.~.gª~...LÇ.~~;:~-- of the
Anchorage News, a daily news-
paper.That said newspaper has
been approved as a legal news-
paper by. the Third Judicial Court,
Anchorage, Alaska, and it is now
and has been published in the
English language continually as
a daily newspaper in Anchorage,
Alaska, and it is now and during
all of said time was printed in an
office maintained at the aforesaid
place of publication of said news-
paper. Tþatthe annexed is a true
copy of a. ____Ã-!e..gªl...Nº:t!.:~&~.)· 924-
as it was published in regular
issues (a nd not in supplemental
form) of said newspaper for. a
period of __._~_1?:~_______ insertions,
commencing on the -.l-3-....,day
April 72
of .___..___.._.._.........__,19 ._.m , and
ending on the.....J3.......... day of
b~th···~1i:--t-ì~~I·~~i~;~" a~~-··;~~t
such newspaper was regularly
distributed to its subscribers dur-
ing all of sa,id period. That the
full amount of the fee charged
for the foregoing publication is
the sum of $ 9.00 which
amount has been paid in full at
the rate of 25¢ per line; Mini-
mu~rge $705/00,./ j~ / /
SUb~?¿~~~
me this __J,t'd:;~----.APriJ.----.
19_72.;¿ /'.
..!:.~~~.........
----¿~~--
the State of Alaska,
Third Division,
Anchorage, Alaska
J1=~:~~~:IR~¿¿:-
OF
)
PUBLICA TION
['.;!
(' J
, ,
" '. .
MOll ÇE '~~. .,þU~~~tA~Ê~~¡'~. '
'$~\Þ '~e!¡' :,'$~'" ",,:jot"
ÞIiPA~TM,INT' '.',Jt: . ," . R&SõtlK\.~S
AllSk~ on: .~d~a~/ c1~~ï,rt~~:ton tomm:ttee
, . con..~r.Y~'~10,'~~~~!;\r'~~!i""~:;'¡1.·, rIb:
ReI . G.renlte'~blnt¡, JIII':;,L,:'!T~'ðlha"':~:Y :fMa',
McArthur ,River,: .jl~I'.I1I ,andM':,¡"",.
c;round ShoaIFI,,~~, . ..' I"~ ,I¡~"'>.",,":
The'A,llIska '.',' t,n\'.nd~.~,<cons'flit~~'j",
Con'II'I'Iltt.. ,. WII1,hO. 1~:\,';,IiÐ,:" t!l>. '~flr,,µ~~~, ;i~~
Titlt 11, Alaska,' Adl11~,ISt,r.ty~!,;:~d~bf,S::.
tlon 2009 tel I:OnsJ6~,\t1,:,,~,,~~t,,¡¡, ' "
! nacessary for". deq. ù.~:¡.~'.~t~~J~~tl;&¡:~:;
\ductlon platfbrms,. In.t ,W '~~l,ilj", '102
as requIred II\! Conl~'~,~, i~~':j~H~"~~~1: '
103, 1CM '.nd 1Ø~~,.., ,1,&'11,1...': ': ,i:':t!: i',:, ~,,,
'Th. hearlna w\ll'IfI::".I,d",,'.~~,IOQ, I.m., i
Mey 12,)~72, In tþe C¡ty\~~,"-~~t~~~~::~:1
of the Z. J, Loussac Llbr¡fy, ~". , .
and F St~.et, 'Anchqr~g.,.A\e,~kar, ,~t whl,ch
time operators of I','" l1il, p~~,I!;~,thln thl
referenced fi.'ds~.~..af:f,~c't":·,.¥\d Interested
partie~, will blh~~d.~"~':'."I" "'1, '
, ' '" ,'. .: ",,'. "\",'~,I"",J".,
'th&m,.'(' ::i~~.hì11,\::Jr. .
'.Executlve ~t!~.ry ,
Alaska ." Ol\.¡'¡""ØI~ C&ns.rvltlon
, .! COlt\mltt~e,"
300t,:,pQ.rcuplnl .Drive '.
:~··M~t«l.r~~'_il'I_.
Püb!l~:*~\\\ .·a~' ~1912 .)" ','
~~~'~'NO~'!t~},~~ ..' In
,--..
-L +.( Lov1
3
'-"
NOTICE OF PUBLIC HEARING
"'" /
'-
STATE OF ALASKA
DEPARTMENT OF NATURAL RESOURCES
Alaska Oil and Gas Conservation Committee
Conservation File No. 114
Re: Granite Point Field, Trading Bay Field, McArthur River Field and
Middle Ground Shoal Field.
The Alaska Oil and Gas Conservation Committee will hold a hearing
pursuant to Title 11, Alaska Administrative Code, Section 2009, to consider
the amount of gas necessary for adequate safety flares on production
platforms in the referenced fields as required in Conservation Order Nos.
102, 103, 104 and 105.
The hearing will be held at 9:00 a.m., May 12, 1972, in the City
Council Chambers of the Z. J. Loussac Library, 5th Avenue and F Street,
Anchorage, Alaska, at which time operators of the oil pools within the
referenced fields and affected and interested parties will be heard.
t:£,. {( ,/¡¡Jdt¿
Thomas R. Marshall, Jr.
Executive Secretary
Alaska Oil and Gas Conservation Committee
3001 Porcupine Drive
Anchorage, Alaska 99504
Publish April 13, 1972
It f wt i