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Presentation OutlinePresentation Outline
• Project Overview
• Resource Characterization
• Stratigraphic Test Results
Reservoir Simulation
• Production Testing
• Conclusions / Future Plans
Schematic Reservoir ModelSchematic Reservoir ModelDevelopment Scenario OptionsDevelopment Scenario Options
3 miles2 m
iles
95ft
Methane Hydrate Free Gas
WaterCalculate Recovery FactorsEvaluate/Contrast Single/Multiple Methods
Simple Model: Simple Model: Depressurization Under Hydrate Depressurization Under Hydrate
Significant Production Increase (~2X) due toFree Gas Dissociation from Gas HydrateSignificant Uncertainties Remain
0
5,000
10,000
15,000
20,000
25,000
30,000
2005
2006
2007
2008
2009
2010
2011
2012
2013
2014
2015
2016
2017
2018
2019
2020
2021
0.0E+00
1.0E+10
2.0E+10
3.0E+10
4.0E+10
5.0E+10
6.0E+10Gas Rate : Base Description
Gas Rate : No Hydrates
Cumulative Gas : Base Description
Cumulative Gas : No Hydrates
Gas
Rat
e (m
scfp
d)
Cum
ulat
ive
Gas
(scf
)
Typical Production Profiles
OGIPINCREMENTAL GAS
UPPER STAINES TONGUE HYDRATE ZONE
UPPER STAINES FREE GAS ZONE
Geologic Description Geologic Description Simulation ModelSimulation Model
~ Free Gas
Gas Hydrate
175 Meter Horizontal Well 175 Meter Horizontal Well 3 3 ½”½” TubingTubing
CMG STARS Reservoir Model ResultsCMG STARS Reservoir Model ResultsGas Production & Gas Hydrate Dissociation Gas Production & Gas Hydrate Dissociation
5 miles3 miles
~ Free Gas
Gas Hydrate
201 x 340 x 2 cells = 136,680 total cells201 x 340 x 2 cells = 136,680 total cells82.5 foot grid spacing82.5 foot grid spacing
5 miles3 miles
CMG STARS Reservoir Model ResultsCMG STARS Reservoir Model ResultsGas Hydrate Dissociation after 15 yearsGas Hydrate Dissociation after 15 years
Moving front hydrate dissociationMoving front hydrate dissociation
Reactions at the hydrate/gas interface cause local cooling.Reactions at the hydrate/gas interface cause local cooling.
High net pressure is left behind the reaction frontHigh net pressure is left behind the reaction front
Well Placement: In Hydrate zone where Well Placement: In Hydrate zone where initial initial SSww greater than or equal to irreducible greater than or equal to irreducible SSww
• 40 % init Sw
IntraIntra--Hydrate Production ScenariosHydrate Production Scenarios
60% Shyd, 40 % Sw includes 20 % Swirr
80% Shyd, 20 % Swirr
IntraIntra--Hydrate Production ScenariosHydrate Production Scenarios
< Gas Hydrate, > Water> Productivity
> Gas Hydrate, No Mobile Water< Productivity
A
A/B/C/D/E
B/C/D/E
A/B/C/D
C/D/E
C/D/EE
E
B/C/D
C/D
C/D D/E
Base PermafrostTruncation
Base Gas Hydrate
Truncation
ZoneGIP
(TCF)
Risked GIP
(TCF)ABCDE
Total
18 69 911 86 66 4
50 33
Stage 2: Multi-Well Pilot Testing
Stage 2: MultiStage 2: Multi--well testing/calibrationwell testing/calibration
Stage 3: Limited Initial DevelopmentStage 3: Limited Initial Development
Similar in scope to WSak 1E/1J pilot in
KRU viscous oil
Filters applied to reduce wellcount to ~148 at 640 Acre Spacing in C & D sands > 0’ thickness
Stage 4: FullStage 4: Full--field developmentfield development
North Slope Hydrate Forecasts Type Well Gas Production Forecasts
0
500
1000
1500
2000
2500
0 10 20 30 40 50 60 70 80 90
Years from Start-up
Gas
Rat
e (m
scfp
d)
160 Acre High Sw640 Acre High Sw640 Acre Low Sw
North Slope Hydrate ForecastsType Well Cumulative Production Forecasts
-
10,000,000
20,000,000
30,000,000
40,000,000
50,000,000
60,000,000
0 10 20 30 40 50 60 70 80 90
Years from Start-up
Cum
ulat
ive
Gas
(msc
f)
160 Acre High Sw640 Acre High Sw640 Acre Low Sw
North Slope Hydrate Forecasts Type Well Water Production Forecasts
0
100
200
300
400
500
600
700
800
0 10 20 30 40 50 60 70 80 90
Years from Start-up
Wat
er R
ate
(bpd
)
160 Acre High Sw640 Acre High Sw640 Acre Low Sw
Reference Case High Upside CaseNorth Slope Hydrate Forecasts
Type Well Gas Production ForecastsIncluding Upside Type Wells
0
5000
10000
15000
20000
25000
0 10 20 30 40 50 60 70 80 90
Years from Start-up
Gas
Rat
e (m
scfp
d)
160 Acre High Sw640 Acre High Sw640 Acre Low SwUpside 640 Acre Low SwUpside 640 Acre High Sw
North Slope Hydrate ForecastsType Well Cumulative Production Forecasts
Including Upside Type Wells
-
10,000,000
20,000,000
30,000,000
40,000,000
50,000,000
60,000,000
70,000,000
0 10 20 30 40 50 60 70 80 90
Years from Start-upC
umul
ativ
e G
as (m
scf) 160 Acre High Sw
640 Acre High Sw640 Acre Low SwUpside 640 Acre Low SwUpside 640 Acre High Sw
North Slope Hydrate Forecasts Type Well Water Production Forecasts
Including Upside Type Wells
0
1000
2000
3000
4000
5000
6000
7000
8000
9000
0 10 20 30 40 50 60 70 80 90
Years from Start-up
Wat
er R
ate
(bpd
) 160 Acre High Sw640 Acre High Sw640 Acre Low SwUpside 640 Acre Low SwUpside 640 Acre High Sw
Type WellsType Wells
0
2,000,000,000
4,000,000,000
6,000,000,000
8,000,000,000
10,000,000,000
12,000,000,000
1/14/2004 9/22/2017 6/1/2031 2/7/2045 10/17/2058 6/25/2072 3/4/2086 11/11/2099 7/21/21130
500,000,000
1,000,000,000
1,500,000,000
2,000,000,000
2,500,000,000
3,000,000,000
Reference Case Cumulative Gas Production reference Case Cumulative Water Production
Cumulative gas & water
MCF Gas Bbls Water
Reference CaseReference Case
STAGE 1 2 43
1 2 43
0
2,000,000,000
4,000,000,000
6,000,000,000
8,000,000,000
10,000,000,000
12,000,000,000
14,000,000,000
1/14/2004 9/22/2017 6/1/2031 2/7/2045 10/17/2058 6/25/2072 3/4/2086 11/11/2099 7/21/21130
500000000
1000000000
1500000000
2000000000
2500000000
3000000000
3500000000
4000000000
Upside Case Cumulative Gas Production Upside Case Cumulative Water Production
Upside CaseUpside Case
MCF Gas Bbls Water
0
1,000,000,000
2,000,000,000
3,000,000,000
4,000,000,000
5,000,000,000
6,000,000,000
7,000,000,000
8,000,000,000
9,000,000,000
10,000,000,000
1/14/2004 9/22/2017 6/1/2031 2/7/2045 10/17/2058 6/25/2072 3/4/2086 11/11/2099 7/21/21130
500,000,000
1,000,000,000
1,500,000,000
2,000,000,000
2,500,000,000
3,000,000,000
Extreme upside Case Cumulative Gas Production Extreme Upside Case Cumulative Water Production
Extreme Upside CaseExtreme Upside Case
MCF Gas Bbls Water
Mount Elbert MDT Mount Elbert MDT Key ResultsKey Results
• Confirmation of gas release via depressurization
• Clear indication that depressurization alone may not be sufficient in select (T) settings
• Confirmation of mobile water phase • Sgh = 65%; 25% = Swirr• Sgh = 75%; 10% = Swirr
• Determination of intrinsic K• 0.12 – 0.17 mD
• Reformation kinetics may be important
• Detailed reservoir heterogeneity may control productivity
Fluids ProducedFluids Produced
0.0
0.1
0.2
0.3
0.4
0.5
0.6
0.7
0.8
0.9
1.0
0.0 1.0 2.0 3.0 4.0 5.0 6.0 7.0 8.0 9.0 10.0 11.0 12.0
Test Time, hours
Cum
ulat
ive
Gas
Pro
duct
ion,
sm
3
0
0.01
0.02
0.03
0.04
0.05
Cum
ulat
ive
Wat
er, s
m3
Measured-cumulative gas
Measured-cumulative water
Smoothed! Gas and Liquid Production
0
0.5
1
1.5
2
2.5
3
3.5
4
4.5
5
0 5000 10000 15000 20000 25000 30000 35000 40000
Elapsed Seconds
BLP
D in
-situ
0
100
200
300
400
500
600
700
800
900
QG
(scf
/d)
QlblPD BH
QGSCFPD
MDT Testing MDT Testing Pulse pressures through the Pulse pressures through the system : measure responsessystem : measure responses
6”6”
9”7”
2”8” 19
”
Packer inflatesto full contactwith borehole
IntakeScreen
How much gas is How much gas is 1.0 1.0 cfcf downhole?downhole?
The red annular area The red annular area to the left is 1.5 to the left is 1.5 cfcf
38”Tool
Zero
Gridding that recognizes Gridding that recognizes the wellbore annulusthe wellbore annulus
MDT
Well
2149.5 ft
1 m
10 m
Fluid Production Point
2152.5 ft
0.06 m
0.111 m
MDT Testing MDT Testing Annular Space is critical Annular Space is critical in this low rate casein this low rate case
MDT Results Reservoir ModelingMDT Results Reservoir ModelingInternational Code Comparison GroupInternational Code Comparison Group
A
B D
E
A: Stomp-HYD (M. White – PNNL)
B: STARS (S. Wilson – RyderScott)
C: MH-21 (M. Kurihara – JOE)
D: STARS (M. Pooladi-Darvish – Fekete)
E: Tough+/HYDRATE (G. Moridis – LBNL)
0
2
4
6
8
10
12
0.000 2.000 4.000 6.000 8.000 10.000 12.000
Time (hour)
Pressure (M
Pa)
-3.000
-1.000
1.000
3.000
5.000
Tem
perature (C)
Pressure (mesured)
Pressure (calc : Case A)
Temperature(mesured)
Temperature (calc : Case A)
C
0
250
500
750
1000
1250
1500
1750
2000
0.0 1.0 2.0 3.0 4.0 5.0 6.0 7.0 8.0 9.0 10.0 11.0 12.0
Test Time, hours
FBH
P, p
si
30.0
31.0
32.0
33.0
34.0
35.0
36.0
37.0
38.0
39.0
40.0
FBH
T, o F
FBHP actualsimpressFBHT actualSimTemp
NW Eileen St-2
PBU L-106
W Kuparuk St 1
W Kuparuk 7-11-12
W Sak 24
KRU 1H-6
KRU 1C-8
KRU 1D-8
Beechy St-1
Mount Elbert 01
PBU V-107
1
2
3
4
DOWNDIP
Site Comparisons Reservoir ModelingSite Comparisons Reservoir Modeling
50-year Production Scenarios:1. Mt. Elbert-like formation
2.5-3.0°C, Sh = 65%, P ~ 6.7 MPa
2. PBU L-Pad5.0-6.5°C, Sh = 75%, P ~ 7.3-7.7 MPa, 2 zones
3. Down-dip formation10-12°C, Sh = 75%, P ~ 8-9 MPa,2 zones, near base of GHSZ
Simulation of Alternative LocationsSimulation of Alternative Locations
J Pad Pressure and Temperature
Mt. Elbert Location
Simulation of Alternative LocationsSimulation of Alternative Locations
Area 2 (Warmer Location)
Mt. Elbert
Area 3 (Warm Location)
Warmest LocationAt Hydrate/Gas Interface
CC--Unit Heterogeneity Affects Unit Heterogeneity Affects Simulation Saturation ProfilesSimulation Saturation Profiles
0
1000
2000
3000
4000
5000
6000
0 2000 4000 6000 8000 10000 12000 14000 16000 18000 20000time, days
Gas
rate
, m3 /d
ay
homogenousheterogenous
Effect of permeability & porosity Effect of permeability & porosity heterogeneity on predicted production ratesheterogeneity on predicted production rates
Affects of Reservoir HeterogeneityAffects of Reservoir HeterogeneityDetail time ScaleDetail time Scale
50-layer log data modelProblem 7a base case
Typical Flow Rates in Commercial wellsTypical Flow Rates in Commercial wellsthis well also takes a long time to show its full potentialthis well also takes a long time to show its full potential
C2 MDT rate (0.3 mscf/d)C2 MDT rate (0.3 mscf/d)
An example of publishedsimulation study rates
(8 mmscf/d average)
An example of publishedsimulation study rates
(8 mmscf/d average)
Mallik Flow Test * (~70 to 140 mscf/d)
Mallik Flow Test * (~70 to 140 mscf/d)
* Yamamoto and Dallimore (2008)Dallimore et al. (2008)
Note long clean-up timesNote long clean-up times
Presentation OutlinePresentation Outline
• Project Overview
• Resource Characterization
• Stratigraphic Test Results
• Reservoir Simulation
Production Testing
• Conclusions / Future Plans
Year84 86 88 90 92 94 96 98
A LT U D A
20000
2
4
6
8
10
12
14
16
COALBED METHANE WELLS IN U.S.COALBED METHANE WELLS IN U.S.
4538
583364286785
725878388094
9029
2992
284 384 513 477 6571445
10,927
13,986
COALBED METHANE PRODUCTION IN U.S.COALBED METHANE PRODUCTION IN U.S.
Year85 87 89 91 93 95 97 99
0
200
400
600
800
1,000
1,200
1,400
A L T U D AEnergy InformationAdministration (1992,1995,1999, 2002)
1,600
2001
1,800
539
752851
956 10031090
11941252
348
10 17 24 40 91196
1379
1562
PROVED COALBED METHANE RESERVES AS PROVED COALBED METHANE RESERVES AS OF 2001OF 2001
1,000
2,000
3,000
4,000
5,000
0
6,000
7,000
A LT U DA
Energy InformationAdministrat ion (1992,1995,1999, 2002)
New Mexico
EXPLANATION
Colorado
Alabama
Other
1989
1991
1993
1995
1997
1999
2001
2003
2005
Virg in ia
Utah
Alabama
Wyoming
New Mexic o
Colorado
010002000
3000
4000
5000
6000
7000
Virginia
Utah
Alabama
Wyoming
New Mexico
Colorado
US CBM Reserves
Source : EIA 10/2008
BCF Reserves
PROVED COALBED METHANE PROVED COALBED METHANE RESERVES AS OF 2006RESERVES AS OF 2006
Technical Resource
Design and run short term test with Rig
Short term test promising stimulation
options
Implement medium term test
Proved Reserves
Rig off / design medium term
test
Quantify Resource
Long-term tests
Shut-down
Predicted short depressurization test
volumes are measurable+
-
+
+
+
-
+
+
- +
Short
Long
Time Scale
Medium
-
Gas Hydrate Flow Test DecisionGas Hydrate Flow Test DecisionScenario & Contingency PlanningScenario & Contingency Planning
Evaluate Stimulation OptionsSalt Water flushMatrix Acid jobCavitationFracPropped Frac
MDT
Potential issues1.Solids create production problems:
1.Install Gravel pack2.Produce sand 3.(Pump) Frac sand back into fm 4.Cavitation (CBM Model) 5.Resin coat 6.Some combination of the above 7.Other
2.Wellbore freezes off:1.Inject methanol down capillary2.Circulate hot gas 3.Add electrical well heating:
Radiant or Induction 4.Add downhole combustion
3.Production volumes very small but increasing slowly:
1.Evaluate stimulation options 2.Soak with destabilizing agents3.Hydraulic Fracture with conventional or unconventional fluids 4.Evaluate sidetrack option
Drill and Test Vertical Well Drill and Test Vertical Well
Failure path 1: Evaluate Stimulation Failure path 1: Evaluate Stimulation Options in Vertical Well Options in Vertical Well
1. Evaluate secondary methods as a huff-n-puff (inject-soak-produce) to measure stimulation/extraction benefits
1.Hot and cold, liquid and gas, slow and fast, matrix and fracture pressure 1.Water/Steam 2.Methane 3.CO24.PBU gas = 12% CO25.Inhibitors, solvents, biological
2.Continue until not successful
Design with expectation of severe sand production including dedicated circulation strings, sand capable pumps from toe and heel. Take advantage of significant experience in both West Sakand Steam Assisted Gravity Drainage (SAGD) operations.
1.Progress through prior technology sequence using the horizontal well.
Failure Path 2: Sidetrack Existing Well Failure Path 2: Sidetrack Existing Well Drill Horizontal SectionDrill Horizontal Section