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ConocoPhillips’ East Vacuum Field CO2 Update
Doug Pecore
Staff Reservoir Engineer
SENM Permian Conventional
Presented at the 24th Annual CO2 & ROZ Conference
Midland, Texas
Dec 6th 2018
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Presentation Topics
• Background
• Performance Update
• Flexibility in Operation – new WAG methodology
• Compression Expansion
• New Development – TZ/ROZ Phase 1
• Compression Optimization
• 2018 Foam Pilot
• Summary
EVGSAU Background• Vacuum Field developed in 1938
• GB/SA unitized 1978
• Waterflooding began in 1980
• CO2 Injection commenced in 1985
• Overall RF = 48%
• Earlier Projects include Liquids Plant (1992), 1st Foam Pilot (1992), OH Laterals (2001), Compression Replacement (2010-2011)
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After LeMay, 1972
EVGSAU“East Vacuum”
Vacuum Field
EVGSAU Geology and Properties4
2944-003 2913-010 VGEU 05-18 2913W11 VGEU 02-11 VGEU 02-27Hoover 32-4 3202-0013202-020 3202W09 0546-001 VA 13-5
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GUAD_9_3
SNDR
SNDR
GUAD_9_2
GUAD_9_1
GUAD_9_1
LVTN
GUAD_8_2
GUAD_8_2
GUAD_8_1
GUAD_4_UNC
SubseaDepth(ft)
SubseaDepth(ft)
-350 -350
-450 -450
-550 -550
-650 -650
-750 -750
-850 -850
-950 -950
-1050 -1050
-1150 -1150
-1250 -1250
-1350 -1350
PERMIAN_NW_SHELF
HS=112
PETRA 8/13/2012 7:42:37 PM
Grayburg
Upper San Andres
Lower San Andres
Lovington
N S
-700 OWC-700 OWC
Main Pay
TZ/ROZ
TZ/ROZPilot
EVGSAU Cross Section
EVGSAUAverage Producing Depth, feet 4,500
Original Reservoir Pressure, psia 1,613
Reservoir Temperature, o F 105
Average Porosity, % 11.7
Average Permeability, md. 11
Average Net Pay. Feet 71
Oil Gravity, o API 38
Original Formation Volume Factor, RB/STB 1.29
Original Oil Viscosity, cp. 1.00
Initial Solution GOR, SCF/STB 465
EVGSAU Reservoir Properties
Performance Update5
Oil Production Rate 3,150 BOPDGas Production Rate 27,000 MscfdWater Production Rate 39,200 BWPD
Gas Injection Rate 43,000 MscfdWater Injection Rate 54,600 BWPD
Total RF 48 %WF RF 16 %CO2 RF 14 %
Current VRR 1.12 RB/RBGross CO2 Utilization Rate 12.9 MCF/BBL
HCPVI CO2 0.47HCPVI Water 1.67HCPVI Total 2.14
Current Production Metrics
Performance Update6
Projects
• Compression expansion has added WAG flexibility
• Increased water production handled by other COP operated WFs nearby
• TZ/ROZ Pilot (2011) - large amounts of producible gas found
• TZ/ROZ Phase 1 (2016) – similar high CO2 cut wells found
Added Flexibility in Operation7
Active WAG ManagementPrevious Strategy: Line Drive
• Line Drive strategy implemented in 2007 out of operational necessity; no noticeable production benefit
• With compression expansion, EVGSAU returned to pattern by pattern injection based on the process of . . .
• first ranking each pattern using eight pattern health metrics weighted for importance or impact
• then CO2 utilization further adjusts scales the Individual pattern slug size and WAG ratio
Pattern Surveillance using Spotfire8
Pattern Surveillance using Spotfire9
Compression Expansion• Total Installed Capacity:
44 MMscfd
• Liquid Recovery Technology: Ryan-Holmes
• Compression Expansion: completed for 15% under AFE due to timing and contracting strategy
• Train 1 remains fully loaded to maximize NGL recovery
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Train 1
Train 2
Field Inlet
Unit 510 MMscfd
Unit 610 MMscfd
Unit 26 MMscfd
Unit 16 MMscfd
Unit 46 MMscfd
Unit 36 MMscfd
By-Pass
3 MMscfd
EVLRPRyan Holmes
Liquids Recovery Plant
21 MMscfd
Field Re-injection
TZ/ROZ Phase 1: Development11
December 14, 2018
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LegendUnit BoundaryProducerInjector
P&A’d
New Producer
New Injector
Phase 1 Expansion Phase 1a ExpansionOrder Phase 1 D&C
drilled EVGSAU 2739-W525
drilled EVGSAU 2738-W523
drilled EVGSAU 2721-W527
drilled EVGSAU 2739-W522
drilled EVGSAU 3202-W513
drilled EVGSAU 3202-W512
1 EVGSAU 2739-524
2 EVGSAU 2739-526
3 EVGSAU 3328-W520
4 EVGSAU 3345-W521
5 EVGSAU 3373-529
6 EVGSAU 3373-518
7 EVGSAU 3332-519
8 EVGSAU 3374-W517
9 EVGSAU 3374-W516
10 EVGSAU 3202-514
11 EVGSAU 3366-528
12 EVGSAU 3308-510
13 EVGSAU 3308-W511
New Drill Order• TZ/ROZ Pilot started in 2011. 4 injectors and 2 producers
• 1 producer has cum. production = 300 MBO
• Other producer can make 5,000 MCFD gas likely from fracture
• Performed 2 conformance projects to remedy unbalanced injection vertically and high GOR
• Phase 1 sanctioned in 2015
TZ/ROZ Phase 1: Drilling Redesign12
Pros:• Eliminate trouble time associated with
controlling the well and POOH to run casing.
• Casing on bottom when well TD.• Smear Effect – Less chances of severe
losses or diff sticking
Cons:• Require TXP BTC connections &
Centralization – Increase Csg Cost.• Susceptible to buckling, casing wear and
fatigue – Twist-Off.• Slower ROP with non-motor assist and
packed/stabilized assemblies.• Cannot run OH logs
TD WELL @ 5100’
800’ of Severe Loss /
Charged Zones
9-5/8”; 40.0#; J-55; BTC
CSG @ 1630’ ; Inside
“RUSTLER Form”
CONDUCTOR:
16”; 65.0#; H-
40; @ 100’
Drilled 6 wells in late 2015. Half the wells in the program encountered severe losses and flows at the same time. Halted the drilling in early 2016
TZ/ROZ Phase 1: Drill with Casing (DwC)13
Tangible solution to support future development activity at EVGSAU and
other EOR fields
• No trouble time associated with casing drilling encountered during DwC program
• Clear learning curve – continued to innovate during program
• No flows or losses encountered
• QC of tubulars imperative to prevent over-torque downside
• 31% improvement in Days from Spud over 2011 program
• 10% improvement in drilling costs over 2011 program
TZ/ROZ Phase 1: Performance14
Recent Pay Adds
• Producers on track with AFE
• Hindered by lack of OH logs
• Locating “sweet spots” through pay adds
• 3 other producers have encountered high gas rates due to fractures in lower San Andres
• Plan to run IPL logs to measure vertical conformance
Best performance in Phase 1 TZ/ROZ wells are on the flank as reservoir drops into Delaware Basin
Compression Optimization15
Below the line: 5% had flows or losses
Above the line: 31% had flows or losses
High GOR Producers
Phase 1 Expansion Area
• Revisit execution performance
• Examined 131 well files
• Found a pattern of drilling related issues
• Seismic confirms apparent facies change form N-S
• Coincides with high GOR producers
Compression Optimization
1. Lower production and operating expenses by 20% by 2020 through utilization of banked CO2
2. Construct high CO2 content satellite (#7) facility south of EVLRP and pipe to Train 2
3. Re-pipe EVLRP inlet to concentrate rich gas to Train 1
4. Install isolation valve in common inlet to direct gas to desired train
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Facilities Re-piping
Train 1
Train 2
From Sat #1, 4, 5, 7
Unit 510 MMscfd
Unit 610 MMscfd
Unit 26 MMscfd
Unit 16 MMscfd
Unit 46 MMscfd
Unit 36 MMscfd
By-Pass
3 MMscfd
EVLRPRyan Holmes
Liquids Recovery Plant
21 MMscfd
Field Re-injection
From Sat #3, 6
Foam Pilot17
From SPE 190312, “CO2-Foam Field Pilot Test in Sandstone Reservoir: Complete Analysis of Foam-Pilot Response” Dow Chemical, et al
Vertical Profile Modification
Baseline
Post Foam -
4 mo
Post Foam -
8 mo
Post Foam -
9 mo
Upper San Andres 23% 38% 40% 46%
Lovington SS 0% 0% 0% 0%
Lower San Andres 77% 62% 60% 54%
Zonal % Gas Distribution
Foam Pilot Pattern
Improved Run Time
CO2-Foam Process
Summary
• Strong production response from dynamic WAG and use of Spotfire-based data analytics tool in pattern optimization and problem diagnosis
• Drill-with-Casing (DwC) technology allows for low-cost infill and TZ/ROZ development in future
• Upside from flank ROZ projects in possible Phase 2
• Upside from compression utilization via production and operating cost reduction
• Encouraging results from foam trial
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