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907 !-564 5331
E*(onMobil.
March 19, 2018
ER -2018 -OUT -060
Mr. Hollis S. French, Chair
Alaska Oil and Gas Conservation Commission
333 West Seventh Avenue, Suite 100
Anchorage, Alaska 99501-3572
Re: Point Thomson Unit 2017 Annual Reservoir Surveillance Report
Dear Commissioner French,
MAR 2 3 2018
AOGCC
ExxonMobil Alaska Production Inc. hereby submits an Annual Reservoir Surveillance Report for
the Thomson Oil Pool within the Point Thomson Unit in accordance with Rule 8 of Area Injection
Order No. 38 dated August 25, 2015 and Rule 5 of the Conservation Order No. 719 dated
November 9, 2015.
A technical review will be scheduled with representatives from AOGCC to review the annual
reservoir surveillance report in accordance with Rule 5(b) of the Conservation Order No. 719.
If you have any questions or require additional information, please contact Luke Motteram at
(907) 564-3697.
Sincerely,
Jamie Long
For and On Behalf of ExxonMobil Alaska Production Inc.
CC: I m
Attachment: Annual Reservoir Surveillance Report (2 copies)
Pressure Reservoir Report (form 10-412) (2 copies)
Annual Surveillance Form (form 10-413) (2 copies)
Annual Reservoir Properties Report (form 10-428) (2 copies)
ExxonMobil
Annual Reservoir Surveillance Report — 2017
Thomson Oil Pool
Point Thomson Unit
Introduction
This annual reservoir surveillance report is submitted to the Alaska Oil and Gas Conservation
Commission by ExxonMobil Alaska Production Inc., Point Thomson Unit (PTU) operator, in
accordance with Rule 8 of Area Injection Order No. 38 dated August 25, 2015, and Rule 5 of
Conservation Order No. 719 dated November 9, 2015, for the Thomson Oil Pool within the PTU.
The report covers calendar year 2017 for the Initial Production System (IPS) facility.
Enhanced Recovery Project and Reservoir Management —Rule 8(a) & 5(a)(v),(vi)
The Point Thomson IPS project produces natural gas and condensate from the Thomson Oil
Pool to recover liquid condensate for sale and reinject the residue gas as the enhanced
recovery mechanism (gas -cycling). Condensate is transported through the Point Thomson
Export Pipeline (PTEP) for delivery to the Trans -Alaska Pipeline System common carrier
pipelines.
The reservoir management strategy for the Thomson Sand is to reinject cycled gas to help
maintain reservoir pressure for condensate recovery and conserve the gas for future
development. The IPS also provides information about gas condensate production and reservoir
connectivity to assist in subsequent development plans.
Reservoir Voidage Balance —Rule 8(b) & 5(a)(i)
Monthly production and injection volumes and the reservoir voidage balance for the Thomson
reservoir by month and cumulative through December 2017 are summarized in Table 1.
Voidage replacement ratio in 2017 was 0.87 compared to 0.71 in field startup year 2016.
The Annual Report of Injection Project, Form 10-413, is included as Table 2.
Reservoir Pressure Surveys —Rule 8(c) & 5(a)(ii)
Reservoir pressure monitoring is performed in accordance with Conservation Order No. 719,
Rule 3. Static bottom -hole pressure measurements were collected from permanent downhole
gauges and corrected to Thomson reservoir pressure datum of -12,700' TVDSS (true vertical
depth subsea). Bottom -hole pressures were taken during well drilling prior to initial production or
injection, and subsequently during extended well shut in periods.
PTU Annual Reservoir Surveillance Report 2017 Page 1
ExxonMobil
In PTU -15 and PTU -16 initial reservoir pressure was recorded using wireline MDT during initial
drilling in 2010. Correcting to datum, the reservoir pressure measured in both wells was
10,100 psi. PTU -17 initial reservoir pressure data collected while drilling on December 29,
2015 was 10,107 psi at datum.
A summary of static bottom -hole pressures is shown in Table 3, Form 10-412 Reservoir
Pressure Report. Table 4 is the Form 10-428 Annual Reservoir Properties Report required by
20 AAC 25.270(e). Average properties are quoted, noting that ranges for porosity, permeability
and water saturation are relatively wide. Thomson Oil Pool can be characterized as a retrograde
condensate reservoir which helps to explain the reported properties.
A reservoir pressure map is shown in Figure 1. Analysis of pressure surveys indicates limited
reservoir pressure decline. The variation from initial recorded pressure and between wells is
within the expected range given temperature corrections and fluid gradient variations.
Production &Injection Log Surveys —Rule 8(d) & 5(a)(iii)
No production or injection log surveys were run during the reporting period.
Fracture Propagation into Adjacent Confining Intervals —Rule 8(e)
Downhole and surface wellhead gas injection pressures and rates for PTU -15 and PTU -16 are
shown in Figures 2 and 3, respectively.
For PTU -15, at an injection rate of 111 MMscf/d (million standard cubic feet), injection pressure
of 10,245 psi was recorded at the downhole gauge October 9, 2017. Equivalent maximum
reservoir sand face pressure was 10,575 psi with an injected gas gradient.
At PTU -16, a downhole injection gauge pressure of 10,672 psi was reached November 11, 2017
at an injection rate of 102MMscf/d. The corresponding maximum sand face injection pressure is
11,082 psi using an injected gas gradient.
In accordance with Area Injection Order No. 38, Rule 4, gas injection pressures were
maintained below 11,500 psi at the reservoir sand face.
Declining PTU -16 injectivity was observed in May 2017, believed to be caused by plugging of
the gravel pack completion. Flowback cleanup of the well was effective in restoring injection
capacity with no reoccurrence of the issue observed.
Mechanical Integrity Test (MIT) Results —Rule 8(fl
No mechanical integrity tests were performed during the reporting period.
PTU Annual Reservoir Surveillance Report 2017 Page 2
ExxonMobil
Inner and Outer Annulus Monitoring —Rule 8(g)
Casing annulus pressures of production and injection wells completed in the Thomson reservoir
are monitored in accordance ;,^,pith Area Injection Order No. 33, Rule 5, and Conservation Order
No. 719, Rule 7.
Digital continl Inl m nrP_CCI IrA mnnif'nrinn is incfnllorl r%M r,�r%k •�r,r,o .I. .,-r r)--1 n-ri i A n
r..■ vvvv.. v ...tl...LVI 11 ly IV 11 1,)LLA11Vu %ii I cat.JI I Q� 11 JUJU) LJ r- I V I J, Piu-iuand
PTU -17. Control room alarms are in place to notify operations of high pressure for initiation of
manual bleed down intervention.
An annotated summary of annulus pressure monitoring is shown in Figures 4 to 6.
Special Monitoring —Rule 8(h) & 5(a)(iii)
No special monitoring was undertaken during the reporting period.
Pool Production Allocation —Rule 5(a)(iv)
Point Thomson production is wholly allocated back to the sole producing PTU -17 well from the
Thomson reservoir. Condensate liquids are metered at the custody transfer meter on Point
Thomson Central Pad. Total produced gas from PTU -17 is calculated as the sum of injected gas
into PTU -15 and PTU -16, lease fuel, pilot/purge and flare gas.
Reservoir Surveillance Plans —Rule 8(i)
Reservoir surveillance plans for next year include the collection of surface wellhead and
downhole pressure and temperature data, which will be used to monitor reservoir pressure, well
productivity and injectivity. Casing annulus pressures will continue to be recorded to monitor
integrity of the wells.
Pressure and temperature data will be complemented by well production and injection rates,
together with metered condensate, gas and water volumes. The information will be used to
calculate gas -condensate ratio, water cut and voidage replacement for the field.
No production or injection log surveys are planned for next year.
Development Plans —Rule 80) & 5(a)
As noted above, IPS operations will provide data and information regarding production, well and
reservoir performance, and IPS facility performance to assist in evaluation of development
plans. Expansion plans are described in the PTU Plan of Development (POD) dated July 1,
2017, submitted to the Alaska Department of Natural Resources.
PTU Annual Reservoir Surveillance Report 2017 Page 3
ExxonMobil
ATTACHMENTS
Table 1: Monthly Production, Injection and Voidage Balance Summary......................................5
Table 2: Annual Report of Injection Project (Form 10-413)..........................................................6
Table 3: Reservoir Pressure Report (Form 10-412)....................................................................7
Table 4: Annual Reservoir Properties Report (Form 10 -428) ......................................................8
Figure 1: Thomson Reservoir Pressure Map...............................................................................9
Figure 2: PTU -15 Injection Pressure and Rate..........................................................................10
Figure 3: PTU -16 Injection Pressure and Rate..........................................................................11
Figure 4: PTU -15 Annulus Monitoring.......................................................................................12
Figure 5: PTU -16 Annulus Monitoring.......................................................................................13
Figure 6: PTU -17 Annulus Monitoring.......................................................................................14
PTU Annual Reservoir Surveillance Report 2017 Page 4
ExxonMobil
Table 1: Monthly Production, Injection and Voidage Balance Summary
Month
Condensate
(STB)
water
(STB)
Dry Gas Production
(MSCF)
Dry Gas Injection i
(MSCF)
01/2017
236,667
3,202
4,458,103
4 330 263
V2/2V 1 I
20, 7 5 7
249
3991550
3371753
03/2017
1957395
27574
31714,478
3,5787412
04/2017
192,487
21209
35602,139
37482,618
05/2017
929795
11305
177247885
116455352
06/2017
81400
103
155,883
129,879
07/2017
53,903
671
9817229
922,416
08/2017
2111248
27586
318987251
31766,855
09/2017
50,092
574
891,894
828.113
10/2017
2321249
31032
4,3071306
41179,198
11/2017
2871261
31634
574467402
51295,588
12/2017
1657047
21171
37086,881
279897877
TOTAL
11746,301
22,310
32,666,999
31,486,325
Note: Bc = 0.999 RB / STB
Bg = 0.480 RB / MSCF
Bw = 1.000 RB / STB
Bc = condensate formation volume factor
Bg = dry gas formation volume factor
Bw = water formation volume factor
MSCF = thousand standard cubic feet
RB = reservoir barrels
STB = stock tank barrels
VRR = voidage replacement ratio
VRR
(RB/RB)
0.87
�� O A
I
1111168YA
0.86
0.75
0.84
0.87
n wi
we A
W O A
0.87
PTU Annual Reservoir Surveillance Report 2017 Page 5
ExxonMobil
Table 2: Annual Report of Injection Project (Form 10-413)
STATE OF ALASKA
ALASKA OIL AND GAS CONSERVATION COMMISSION
ANNUAL REPORT OF INJECTION PROJECT
FOR THE YEAR: 2017
20 AAC 25.432 (2)
Name of Operator
Address
ExxonMobil Alaska Production Inc.
PO Box 196601 Anchorage, AK 99519-6601
Unit or Lease Name
Field and Pool
Point Thomson Unit
Point Thomson Field, Thomson Oil Pool
Type of Injection Project
Name of Injection Project
Number of Inj./Conservation Order
Authorizing Project
Enhanced Recovery (Gas -Cycling)
Initial Production System (IP S)
AIO # 38 and CO # 719
1. WATER INJECTION DATA
As of Jan. 1, active w ater inj.
Water inj. w ells added or
As of Dec. 31, active water
Annual volume water inj.
Cumulative w ater inj. to date
w ells
subtracted
inj. Wells
0
0 0
0
0
0
2. GAS INJECTION DATA
As of Jan. 1, active gas inj.
Gas inj. wells added or
As of Dec. 31, active gas inj.
Annual volume gas inj.
Cumulative gas inj. to date
w ells
subtracted
Wells
2
0 0
2
1 31,486,325
1 38,495,500
3. LPG INJECTION DATA
As of Jan. 1, active LPG inj.
LPG inj. wells added or
As of Dec. 31, Active LPG inj.
Annual volume LPG inj.
Cumulative LPG inj. to date
w ells
subtracted
w ells
0
0 0
0
0
0
4. PRODUCTION DATA
As of Jan. 1, Total oil wells
Oil wells added or
As of Dec. 31, Total oil wells
Annual volume oil and/or
Cumulative oil and/or
subtracted
condensate produced
condensate to date
1
0 0
1
1,746,301
2,217,946
As of Jan. 1, Total gas wells
Gas wells added or s ubtractE
As of Dec. 31, Total gas wells
Annual volume gas produced
Cumulative gas to date
0
0 0 1
0 (see above)
32,666,999
41,592,128
5. INJECTION VOLUMES (Reservoir Barrels)
Annual Volume
Cumulative since project start
Water (surface bbls.=reservoir bbls.) (A)
0
0
LPG (Surface bbls.=reservoir bbls.) Indicate type of LPG, Butane, Propane or other. (B)
0
0
Standard CFXvolume factor v where �
Z (Compressibilty factor) X Tr (reserwir temperature, OF absolute) X 14.65
Gas
5.615 cf/bbl. X Pr. (reservoir pressure, psia) X520 (absolute equiwlent at 60-F) (C)
15,120,402
18,484,024
TOTAL FLUIDS INJECTED (reservoir bbls.) (A)+(B)+(C)
15,120,402
18,484,024
6. PRODUCED VOLUMES (Reservoir Barrels)
Oil (Stock tank Bbls. X formation volume factor) (D)
1,744,555
2,215,728
Free Total gas produced in standard cubic feet less solution gas
Gas produced (Stock tank bbls. Oil produced X solution gas oil
ratio) X volume factor v calculated for produced gas (E) 1
15,687,3 87
19,9701453
Water (surface bbis.=reservoir bbls.) (F)
22,310
27,955
TOTAL PRODUCED VOLUMES (reservoir barrels) (D)+(E)+(F)
17,454,252
22,214,136
NET INJECTED (+) OR PRODUCED (-) VOLUMES (5.)-(6.)
-2,333,849
-3,730,111
Year end reservoir pressure Datum feet
psia Subsea
10,085 -12,700
I hereby certify that the foregoing is true and correct to the best of know edge.
Signature: Luke Motteram
Date: 16 -Feb -18
Printed Name: Luke Motteram
Title:
Production Engineer
PTU Annual Reservoir Surveillance Report 2017 Page 6
ExxonMobil
Table 3: Reservoir Pressure Report (Form 10-412)
PTU Annual Reservoir Surveillance Report 2017 Page 7
STATE OF ALASKA
ALASKA OIL AND GAS CONSERVATION COMMISSION
RESERVOIR PRESSURE REPORT
1. Operator:
2. Address -
Alaska Production Inc.
PO
PO Box 196601 Anchorage, AK 99519-6601
3. Unit or Lease Name:
4. Field and Pool: 5. Datum Reference:
6. Oil Gravity:
7. Gas Gravity:
Point Thomson Unit
Point Thomson Feld, Thomson Oil Pool -12,700' TVDSS
37 API
0.7
8. Well Name and 9. API Number
10. Type
11. AOGCC
12. Zone 13. Perforated 14. Final Test 15. Shut -In 16. Press. 17. B.H. 18. Depth 19. Final
20. Datum
21. Pressure
22. Pressure
Number: 50XXXXXXXXXXXX
NO DASHES
See
Pbol Code
Intervals Date Time, Hours Surv. Type Term. Tool TVDSS Observed
TVDSS (input)
Gradient, psi/ft.
at
Datum (cal)
Instructions
Top - Bottom (see Pressure at
TVDSS instructions Tool Depth
for codes)
Morrison
PTU -15 50089200300000
GI
668150
Sand 12622-12804 7/18/2017 1056 SBHP 177 10420 9767
oms-on
12700
0.14
10083
PTU -15 50089200300000
GI
668150
Sand 12622-12804 9/24/2017 424 SBHP 176 10420 9769
Morrison
12700
0.14
10085
PTU -16 50089200310000
GI
668150
Sand 12763-12908 7/18/2017 1056 SBHP 171 10022 9722
omson
12700
0.14
10094
PTU -16 50089200310000
GI
668150
Sand 12763-12908 9/24/2017 424 SBHP 171 10022 9722
omson
12700
0.14
10095
PTU -17 50089200330000
0
668150
Sand 12619-12823 7/18/2017 155 SBHP 199 10571 9734
Morrison
12700
0.16
10084
PTU -17 50089200330000
0
668150
Sand 12619-12823 9/24/2017 184 SBHP 197 10571 9732
12700
0.16
10083
23. All tests reported herein w ere made in accordance w ith the applicable rules, regulations and instructions of the Alaska Oil and Gas Conservation Commission.
I hereby certify that the foregoing is true and
correct to the best of my know ledge.
Signature Luke Nbtteram
Title Production Engineer
Printed Name Luke Nbtteram
Date February 16, 2018
PTU Annual Reservoir Surveillance Report 2017 Page 7
ExxonMobil
Table 4: Annual Reservoir Properties Report (Form 10-428)
STATE OF ALASKA
-
ALASKA OIL AND GAS CONSERVATION COMMISSION
ANNUAL RESERVOIR PROPERTIES REPORT
1. Operator: 2. Address:
—
ExxonMabil Alaska Production Inc.
PO Box 196601 Anchorage, AK 99519-6601
3. Feld and Fool 4. Fool Name 5. Reference 6, 7, Porosity 8. Permeability 9. Swi (%} 10. Oil 11. Oil 12, Original 13. Bubble 14. Current 15. Oil 16. Gas 17.
Gross 18. Net Pay
Code: Datum (ft Temperature M (md) Viscosity @ Viscosity @ Pressure Point or Reservoir Gravity Specific Pay
19. Original
20. Bubble Point 21. Gas 22. Original 23. Current
(ft) (ft)
TV DSS) (°F) Original Saturation (psi) Dew Point Pressure ('A P) Gravity
Formation
Formation Compressibility GOR (SCF/STB) GOR (SCF/STB)
(Air
Pressure Pressure (cp) Pressure (psi)
Volume
Volume Factor Factor (Z)
= 1.0)
m oFFon (cp) (psi)
Factor
(RB/STB)
(RB/STB)
668150 Thomson Oil Pool -12,700 230 15 100 42 1.81 1.81 10100 10100 10085 37 0.7 235 235
0.0029
0
1.5 20,000 20,000
I hereby certify that the foregoing is true and correct to the best of my knowledge.
Signature Luke Motteram
Title Production Engineer
Printed Name Luke Motteram
Date February 27, 2018
PTU Annual Reservoir Surveillance Report 2017 Page 8
ExxonMobil
Figure 1: Thomson Reservoir Pressure Map
408000 416000 4244000 43-200-0 440000 44v --C-0 50 -CO g 464000 472001 48000 �0
00 504-000
5120W
c :�( �sAyu3Ts.srfYr hi .imA..3 iIIsssDv.. �.dL.vihv�rK#sHrvsi r,R.fii.)r 3.i.sY svp�.iAv.Y3r%A�.iH ssa g
i�.,�e,' �-rA�uYav� .mCv�i✓.�AurY�„sA�.r� �� �vhtY�isvYiv �iyA.vcD3ss3ui�.ArvAirsiuA,�Miac�� A�
'elF d
s ...
C>
C,
L
n
z
AL Injector
'lo-
3 4 Smiles
r
..
4=111.10 160-00 444000 433200-0, 4 COCC- 44800-0 4560,0, 46400-0 47200-0 4 O-0 0 488000 496000O-4 0 2`00
PTU Annual Reservoir Surveillance Report 2017 Page 9
ExxonMobil
Figure 2: PTU -15 Injection Pressure and Rate
10000
7500
CL
CL
5000
2500
0
PTU -15 Injection Pressure & Rate
250000
200000
150000
,4-
.M
It
100000
50000
U
zvj a nri t enii i 1Jfrv1arf17 06,%pr/17 30/Ap r,;'l 7 24/May/17 171Jun/17 l 1 IJ u Ill 7 OWAugf17 28.(Augil7 2lfSepl17 1510 ctf, 17 OWN ov,01 7 02fDec/17 216/Dec/17
Start Time: 0 1 IJ a n/l 7, 12:00:00 AM Span: 52.142857142857146 We0s End Time: 01.0anf1B 12:00:00 AM
* ptP1785001 Ol.PV Description Current Value Units Min Max Scale Ag g re g ate Tolerance
* ptl`1561001 — 02.PV Well #15 Sub Surface Casing 9762. 10 PSIG 0 12500 Left Fits 5
PTU 15 Wellhead Prs 8175.11 PSIG 0 12500 Left Fits 5
* ptF156100106.13V PTU 15 Inj Well 0 MSCFD 0 250000 Right Ave ra g e 5
PTU Annual Reservoir Surveillance Report 2017 Page 10
ExxonMobil
Figure 3: PTU -16 Injection Pressure and Rate
12500
10000
7500
CL
5000
2500
0
PTU -16 Injection Pressure & Rate
'150000
200000
150000
Cr
100000
50000
z -+w a w" i t 'wft e fill 13frular.07 0 15,fA p rf 17 30/Apr.?l7 24fMay/17 17/Juni,17 1 VJ u Ill 7 041Aug/17 281.Augfl7 21/Sepfl7 l5!OoVl7 08/Nov,,'17 02fDec/17 1.15IDeell'o
Start Time: Ol/Janfl7 12:00:00 AM
Span: 52.142857142857146- We elks
End Time: 01 Qanfl8 12:00:00 AM
Description Current Value Units Min
M ax Scale
-Aggregate Tolerance
* ptP 178500102. PV
Well #115 Sub Surface Casing 9720.20 PSIO 0
12588 Left
Fits 5
* ptPI552001-08.PV
PTU 16 Inj Gas To Inj Well 7706.77 PSIG 0
12500 Left
Fits 5
* ptFI552001—OC.PV
PTU 115 Inj Well 0 MSCFD 0
250000 Right
Average 5
PTU Annual Reservoir Surveillance Report 2017 Page 11
ExxonMobil
Figure 4: PTU -15 Annulus Monitoring
4000
:3000
kA
CL
2000
1000
0
PTU -15 Annulus Pressure
-L,wj a nil i r ioir eD.C1 e i w rvgar l i 02fApr 1 7 25/,Apr.117 18fMa-i
yf 17 10.0 u nil 7 03.0 u 1/17 26.0 u Ill 7 18.?Au gf 17 1 OfS e pf 17 0310 ct(l 7 26i0cV17 18fNov/17 1lfDee/17
Start Time: 01fJanf17 12:00:00 AM S p a n: 52.142857142857146 We ek's End Time: O1/Jan/18 12:00:00 AM
• PtPI5151001 lL9.PV Description Current Value Units Min Max Scale Aggregate Tolerance
• ptP 166 1001 17.PV PTU 15 InnerAnnulus Prs 0 PSIG 0 5000 Left Fife 5
PPTU 15 Intermediate Annulus P 0 PSIG 0 5000 Left Fits 5
PtPI58100118.13V PTU 15 Outer Annulus Prs 0 PSIG 0 5000 Left Fits 5
PTU Annual Reservoir Surveillance Report 2017 Page 12
ExxonMobil
Figure 5: PTU -16 Annulus Monitoring
5000
4000
3000
rz,
IA
2000
1000
0
PTU -16 Annulus Pressure
.i-olodlje I 1 10)1- ears I e I U JJ1 rul a Y1 t U 2 fAk p rf 17 25.fAp rfl 7 18fIVIxy.(17 10fJun/17 03YJul/17 26M u 1/17 18,;Au gf 17 10/Sep/17 0310W1 7 2610 cV1 7 18f N ov/1 7 11fDec117
Start Time: 01fJan117 12:00:00 AM Span: 52.142857142857146 'Weeks End Time: OVJan/18 12:00:00 AM
• ptPI552001_1 09.13V Description CurrentValue Units Kolin Pular Scale Aggregate Tolerance (%)
PTU 16 Inner Annulus Prs 0 PSIG 0 5000 Left Fits 5
• ptPI552001-17.PV PTU 10 Intermediate Annulus P 0 PRIG 0 5000 Left Fits 5
V.w
" ptP 1552001 _18. PV PTU 16 Outer Annulus Prs 0 P8G 0 5000 Left F its 5
PTU Annual Reservoir Surveillance Report 2017 Page 13
ExxonMobil
Figure 6: PTU -17 Annulus Monitoring
501
4000
3000
IA
CL
CL
2000
1000
PTU -17 Annulus Pressure
Aw--.Prsj CI Ile I e I;-,. r ewil i i
1 uk, cars. -i tr u 41 hi9k p v I 1 21 5 f)k p rf 17 18f M ayll 7 1 0,Q u nfl 7 03fJ u If 17 26fJ u Ill 7
1 81.Au g1l 7 1013epfl7
0310 ct(l 7
2610 et/17 181N ovil 7 ll/Decfl7
Start Time: 01/Jan/17 12:00:00 AM
• PtPI561051 16.PV
• PtPI561051-17.PV
Span: 52.142E5er 1= 2857 146 Weeks
Description CurrentValue Units
Prod Well Inner Annulus Prs 800.488 PSIG
Prod Well Outer Annulus Prs 0 PSIG
Min May
0 5000
0 5000
Scale
Left
Left
End Time: 01/JanflB 12:00:00 AM
Aggregate Tolerance (%)
Fits 5
Fits 5
PTU Annual Reservoir Surveillance Report 2017 Page 14
STATE OF ALASKA
ALASKA OIL AND GAS CONSERVATION COMMISSION
RESERVOIR PRESSURE REPORT
1. Operator:
2. Address:
ExxonMobil Alaska Production Inc.
PO Box 196601 Anchorage,
AK 99519-6601
3. Unit or Lease Name:
Point Thomson Unit
4. Field and Pool:
5. Datum Reference:
6. Oil Gravity:
7. Gas Gravi :
�
8. Well Name and 9. API Number
10. Type
11. AOGCC
12. Zone
13. Perforated
14. Final Test
Point Thomson Field, Thomson Oil Pool
15. Shut -In 16. Press.
-12,700' TVDSS
37 API
0.7
Number: 50
See
Pool Code
Intervals
Date
17. B.H.
Time, Hours Surv. Type Temp.
18. Depth Tool 19. Final
TVDSS
�?0. Datum
21. Pressure
22. Pres sure at
NO DASHES
Instructions
Top - Bottom
Observed
TVDSS (input)
Gradient, psi/ft.
Datum (cal)
(see
Pressure at
TVDSS
instructions for
Tool Depth
codes)
PTU -15 50089200300000
GI
668150
omson
Sand
12622-12804
7/18/2017
1056 SBHP 177
10420 9767
12700
Thomson
0.14
10083
PTU -15 50089200300000
GI
668150
Sand
_ms
12622-12804
9/24/2017
424 SBHP 176
10420 9769
12700
0.14
oon
10085
PTU -16 50089200310000
GI
668150
Sand
12763-12908
7/18/2017
1056 SBHP 171
10022 9722
12700
0.14
omson
10094
PTU -16 50089200310000
GI
668150
Sand
12763-12908
9/24/2017
424 SBHP 171
10022 9722
12700
0.14
omson
_
10095
PTU -17 50089200330000
O
668150
Sand
12619-12823
7/18/2017
155 SBHP 199
10571 9734
12700
0.16
Thomson
10084
PTU -17 50089200330000
O
668150
Sand
12619-12823
9/24/2017
184 SBHP 197
10571 9732
12700
0.16
10083
23. All tests reported herein were made in accordance with the applicable rules, regulation
nd instructions of the Alaska Oil and Gas Conservation Commission.
hereby certify that the foregoing is true and correct to the best of my knowledge.
Signature Luke Motteram
_ Title
Production Engineer
Printed Name Luke Motteram
Date February 16, 2018
Form 10-412 Rev. 04/2009
INSTRUCTIONS ON REVERSE SIDE
STATE OF ALASKA
ALASKA OIL AND GAS CONSERVATION COMMISSION
ANNUAL REPORT OF INJECTION PROJECT
FOR THE YEAR: 2017
20 AAC 25.432 (2)
Name of Operator
Address
ExxonMobil Alaska Production Inc.
PO Box 196601 Anchorage, AK 99519-6601
Unit or Lease Name
Field and Pool
Po�t � hQm„con i Tnit
Point Thomson Field, `Thomson Oil Pool
Type of Injection Project
Name of Injection Project
Number of I nj ./Conservation Order Authorizing
Project
Enhanced Recovery (Gas -Cycling)
Initial Production System (IPS)
AIO # 38 and CO # 719
1. WATER INJECTION DATA
As of Jan. 1, active water inj.
Water inj. wells added or
As of Dec. 31, active water inj.
Annual volume water inj.
Cumulative water inj. to date
wells
subtracted
Wells
0
0 0
0
0
0
2. GAS INJECTION DATA
As of Jan. 1, active gas inj. wells
Gas inj. wells added or
As of Dec. 31, active gas inj.
Annual volume gas inj.
Cumulative gas inj. to date
subtracted
Wells
21
0 0
2
31,486,325
3854955500
3. LPG INJECTION DATA
As of Jan. 1, active LPG inj.
LPG inj. wells added or
As of Dec. 31, Active LPG inj.
Annual volume LPG inj.
Cumulative LPG inj. to date
wells
subtracted
wells
0
0 0
0
0
0
4. PRODUCTION DATA
As of Jan. 1, Total oil wells 10il
wells added or subtracted
As of Dec. 31, Total oil wells
Annualvolume oil and/or
Cumulative oil and/or
condensate produced
condensate to date
1
0 0
1
15746,301
Annual volume gas produced
212175946
Cumulative gas to date
As of Jan. 1, Total gas wells
Gas wells added or subtracted
As of Dec. 31, Total gas wells
0
0 0
0 (see above)
1 32065999
4155925128
5. INJECTION
VOLUMES (Reservoir Barrels)
Annual Volume
Cumulative since project start
Water (surface bbls.=reservoir bbls.) (A)
0
0
LPG (Surface bbls.=reservoir bbls.) Indicate type of LPG, Butane, Propane or other. (B)
Standard CF X volume factor v. where v=
Z (Compressibilty factor) X Tr (reservoir temperature, °F absolute) X 14.65
Gas
0
0
5.615 cf/bbl. X Pr. (reservoir pressure, psia) X 520 (absolute equivalent at 60°F) (C)
1551205402
18 484 024
TOTAL FLUIDS INJECTED (reservoir bbls.) (A)+(B)+(C)
155120,402
18,484,024
6. PRODUCED VOLUMES (Reservoir Barrels)
Oil (Stock tank Bbls. X formation volume factor) (D) 1,744,555
Free Total gas produced in standard cubic feet less solution gas
Gas produced (Stock tank bbls. Oil produced X solution gas oil
ratio) X volume factor v calculated for produced gas (E) 15,687,387
Water (surface bbis.=reservoir bbls.) (F) 22,310
TOTAL PRODUCED VOLUMES (reservoir barrels) (D)+(E)+(F) 1714541,252
NET INJECTED (+) OR PRODUCED (-) VOLUMES (5.)-(6.) -2,333,849
Year end reservoir pressure
psia
10,085
I hereby cerUly that the foregoing is true an orrect to the best of my knowledge.
Signature: Luke Motteram Lie Date:
16 -Feb -18
Printed Name: Luke Motteram Title:
Production Engi
Form 10-413 Rev. 12/2003
2,215,728
19,970,453
27,955
221214J36
-3,730,111
Datum feet
Subsea
-12,700
Submit Original and One Copy
Form 10-428 Rev. 05/2017
INSTRUCTIONS ON REVERSE SIDE
STATE OF ALASKA
ALASKA OIL AND GAS CONSERVATION COMMISSION
1. Operator:
ANNUAL RESERVOIR PROPERTIES REPORT
2. Address:
-
ExxonMobil Alaska Production Inc.
3. Field and Pool 4. Pool Name
5. Reference 6. Temperature 7. Porosity 8. Permeability
PO Box 196601 Anchorage, AK 99519-6601
9. Swi (%) 10. Oil 11, Oil
Code:
Datum (ft (°F) N (md)
12. Original 13. Bubble 14. Current 15. Oil 16. Gas 17. Gross 18. Net Pay
ViscosityViscosity
@ ity @ Pressure Point or Dew Reservoir
19. Original
20. Bubble Point 21. Gas 22. Original GOR 23. Current
g rent
TVDSS)
Gravity Specific Pay (ft) (ft)
Original Saturation (psi) Point Pressure ('API) Gravity (Air =
Formation
Formation Compressibility (SCF/STB) GOR (SCF/STB)
Pressure Pressure (cp) Pressure (psi) 1.0)
Volume
Volume Factor Factor (Z)
(cp) (psi)
Factor
(RB/STB)
Point Thomson
(RB/STB)
668150 Thomson Oil Pool
-12,700 230 15 100
42 1.81 1.81 10100 10100 10085 37 0.7
235 235
0.0029
p 1.5 20,000 20,000
I hereby certify that the foregoing is true and correct to the best of my knowledge.
Signature Luke Motteram
�
Title Production Engineer
Printed Name Luke Motteram
Date February 27, 2018
Form 10-428 Rev. 05/2017
INSTRUCTIONS ON REVERSE SIDE