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Day 2 Pm - Probabilistic Evaluations
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Transcript of Day 2 Pm - Probabilistic Evaluations
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PROBABILISTIC RESERVE
ESTIMATIONS
DAY 2 AFTERNOON
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WHY PROBABILISTIC EVALUATION
Volumetrically we can easily calculate
the OOIP/OGIP from the followingevaluation:
But we are uncertain about:
Gross volume, porosity, NTGR,
hydrocarbon saturation, drainage,recovery factor
Due to
+ Lack of data
+ Lack of confidence
+ Irreducible uncertainty
Especially true in exploration G&Gactivities (pre-drill studies) without wellcontrol or very limited data
grossHA
A
Hgross
NTG, PHI,
Sw, Boi
Gross bulk volume
Net bulk volume
Total Pore volume
Hydrocarbon volume
Hydrocarbon-in-place
NTGHA gross
grossHA
PHINTGHA gro ss
)1( wgr os s SPHINTGHA
oiwgross BSPHINTGHA /)1(
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DRILLING CERTAINTY/UNCERTAINTY
Do we know what it looks like underground?
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WHY PROBABILISTIC EVALUATION
A Porosity Map
But we do not know it is indeed
porosity
We do not know what range the
porosity has
Nor do we know what fills theseporous rocks
Nor do we know the structural
quality
Nor do we know the areal
quality of the rock
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WHY PROBABILISTIC EVALUATION
Therefore, we need to assess all possible scenarios in any pre-drill prospect, & more importantly, various probable scenarios
Explore full range of Knowns and Unknowns
Specify the known values for some variables
List all possible values of other variables
Perform sensitivity studies with the input matrix Understand the range of outcome
Such a process allows us to look at not just one single number(only if we are certain), but an array of possibilities witheducated assessment
Probabilistic Assessments
Use all values in calculations
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WHY PROBABILISTIC EVALUATION
Objectives of Probabilistic Methods Quantify range and distribution of hydrocarbon in-place due
to ranges of input parameters
Min (downside), Max (upside), Most likely
Assess key variables which contribute significantly touncertainty and appraisal process
Uncertain variables vs. consequent risks
Identify interventions to mitigate risks
Defend on downsides and exploit upsides
Evaluate reservoir development plans, production lifecycle
and capital investment profitability
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COMMON PROBABILISTIC PRACTICE
Volumetric Assessment OOIP/OGIP
Monte Carlo simulation with distributional inputs
Acreage drainage
Pore volume
Net-to-gross ratio
Pay column Porosity
Hydrocarbon saturation
Fluid properties
Recovery factor
Performance/Analog Studies
Similar analogy field/pool/reservoir/formation/well performance
Regional analogy performance
IP rate, cum production, recovery factor, EUR
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Select all possible ranges of input variables in volumetricequation
Calculate a full range of hydrocarbon in-place (HIP)
Low end, high end, mean/medium
Advantages
Quick and easy
Disadvantages
Slot-machine game
WHY PROBABILISTIC EVALUATIONS
p
HIP
low mean high
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PROBABLISTIC EVALUATIONS
NTGR
PHI
A
Hgross
Boi
Hnet
Sw
p
p
OOIP
p: probability, or relative frequency
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PROBABLISTIC EVALUATIONS: MODELS
Normal
Triangular
Uniform
Histogram
Lognormal
Bi-model
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HOW TO USE EXCEL TO DO IT
MS Excel has numerous features that allow geoscientists andreservoir engineers to perform proper & reliable probabilistic
evaluations of oil/gas reserves/resources
Excel Data Analysis contains 19 applications:
Description Statistics Histogram
Random Number Generation & Rank & Percentile
Various math functions, macro & solver
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HOW TO USE EXCEL TO DO IT
Descriptive Statistics
Historgram
Rank and Percentile
Regression
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PROBABILISTIC DISTRIBUTIONS
Triangular Distribution
0.00
0.01
0.02
0.03
0.04
0.05
0.06
0.07
71 75 79 83 87 91 95 99 103
107
111
115
119
123
127
Net Pay, ft
Probability
Uniform Distribution
0.00
0.01
0.02
0.03
0.04
0.05
71
75
79
83
87
91
95
99
103
107
111
115
119
123
127
Net Pay, ft
Probability
Normal Distribution
0.00
0.02
0.04
0.06
0.08
0.10
71
75
79
83
87
91
95
99
103
107
111
115
119
123
127
Net Pay, ft
Pro
ba
bility
Lognormal Distribution
0
20
40
60
80
100
120
140
160
180
415
26
37
48
59
70
82
93
104
115
126
137
148
159
170
181
192
203
214
225
236
247
258
269
280
Net Pay, ft
P
robability
Bounded
Uniform
Triangular
Unbounded
Normal
Lognormal
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PROBABILISTIC EVALUATION: ANALOGY
Open the excel file histogram petrophysical exercises.xls, perform descriptive analysis
and construct histogram of the field petrophysical parameters.
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EXCEL HISTOGRAMPorosity vs. Core Permeability
0.01
0.1
1
10
0.05 0.06 0.07 0.08 0.09 0.10 0.11 0.12 0.13 0.14 0.15 0.16 0.17 0.18 0.19
Porosity
CorePermeability(md)
Core Permeability vs. Water Saturation
0.01
0.1
1
10
0.00 0.10 0.20 0.30 0.40 0.50 0.60 0.70 0.80 0.90 1.00
Water Saturation
Permea
bility(md)
Porosity vs. Water Saturation
0
0.1
0.2
0.3
0.4
0.5
0.6
0.7
0.8
0.9
0.05 0.06 0.07 0.08 0.09 0.10 0.11 0.12 0.13 0.14 0.15 0.16 0.17 0.18 0.19 0.20
Porosity
WaterSaturation
Regional Wells Porosity Distribution of Notikewin Target
0
10
20
30
40
50
60
70
0.075 0.082 0.088 0.095 0.101 0.108 0.114 0.121 0.128 0.134 0.141 0.147 0.154 0.160 0.167 0.173 0.200
Porosity
WellCounts
0%
10%
20%
30%
40%
50%
60%
70%
80%
90%
100%
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MONTE CARLO EVALUATIONS
Monte Carlo simulation method basically generates many
possible outcomes from (almost) all the possibilities of the
input matrix. The greater the number of the simulation runs,
the more reliable of the outcome
Practically 400~500 runs on Excel spreadsheet are ok for the
basic Monte Carlo simulations
If you have a desktop computer from 2007-2008, you can generate 1000
runs in 5 minutes
Remember, the reliability of the results will not increase dramatically.
According to the centre limit theorem, the accuracy of the result is:
N
1
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DISTRIBUTION ANALYSIS PROCEDURES
You have to start from somewhere
Past experience
Analog data
You can generate theoretical distribution by selecting a
distribution type and/or setting a range for each parameter
understanding of geology, geophysics, petrophysics, reservoir concepts
is necessary:
You do not allocate the reservoir pressure range at [14.7, 5000] psi, unless
you are convinced the pool is possibly depletedso your lower bound does
not make sense
Find and ensure the range and the distribution make sense
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DISTRIBUTION ANALYSIS PROCEDURES3050
3051
3052
3053
3054
3055
3056
3057
3058
3059
3060
3061
3062
3063
3064
3065
3066
3067
3068
3069
3070
0 0.02 0.04 0.06 0.08 0.1 0.12 0.14 0.16
Porosity
MeasuredDepth(m)
3057.7 m
3069.3 m
H=11.6 m
3060
3061
3062
3063
3064
3065
3066
3067
3068
3069
3070
3071
0.00 0.02 0.04 0.06 0.08 0.10 0.12 0.14 0.16
Porosity (fraction)
Depth(m)
0
5
10
15
20
25
30
35
40
0.01 0.02 0.03 0.04 0.05 0.06 0.07 0.08 0.09 0.10 0.11 0.12 0.13 0.14 0.15 0.16 0.17 0.18 0.19 0.20
Porosity
Frequency
0%
10%
20%
30%
40%
50%
60%
70%
80%
90%
100%
CumulativeProbability
Frequency
Cumulative %
0
100
200
300
400
500
600
0.01 0.02 0.03 0.04 0.05 0.06 0.07 0.08 0.09 0.10 0.11 0.12 0.13 0.14 0.15 0.16 0.17 0.18 0.19 0.20
Porosity
Frequency
0%
10%
20%
30%
40%
50%
60%
70%
80%
90%
100%
Frequency
Cumulative %
composite N/D porosity log
verified by core analysis
The displayed porositydistribution of the maininterval
The displayed porositydistribution for all thegas column from top to
base
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19
Input
Bulk Rock Volume lognormal distribution
Drainage Area lognormal
Gross Pay normal or lognormal
Petrophysics normal distribution
Porosity normal
Water Saturation normal
NTGR normal
FVF (Bo or Bg) normal
Recovery Factor generally normal but complicated Drive mechanism
Infill drilling / downspacing
PROBABILISTIC EVALUATIONS
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MONTE CARLO SIMULATION RUNS
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HOW TO READ THE RESULTS
Mean
Mean
1.064
1.064
2.527
2.527
0.474
0.474
0%
10%
20%
30%
40%
50%
60%
70%
80%
90%
100%
0.00 0.25 0.50 0.75 1.00 1.25 1.50 1.75 2.00 2.25 2.50 2.75 3.00 3.25 3.50 3.75 4.00
Raw Recoverable Reserve (bcf)
Probability(%)
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PROBABLISTIC EVALUATIONS
PROVED
Min. Max.P90
Median P50
P10Mode Mean
Reserves
Relative
Frequ
ency
PROVED +PROBABLE +
POSSIBLE
PROVED +PROBABLE
Upside Potential
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PROBABILITY
The extent to which an event is likely to occur, expressed as a ratio of the
number of favourable cases to the total number of cases
BEST ESTIMATE
A general term with no definitive statistical meaning
When a single discreet value with no optimism or conservatism is used thisrepresents the expected outcome
It may often be considered to be the mean.
In deterministic usage, it may be the mean, median, or mode (or some other
value).
Widely used and meant to represent the Proved Plus Probable reserves
CONFIDENCE OR CONFIDENCE LEVEL
The qualitative degree of certainty associated with an estimate
UNCERTAINTY AND STATISTICAL CONCEPTS
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UNCERTAINTY AND STATISTICAL CONCEPTS
MEAN
Synonymous with expected value
Arithmetic mean MEDIAN
The value for which there is an equal probability that the outcome will be higher
or lower
The definition of Proved Plus Probable corresponds with the statistical median
MODE
Synonymous with most likely
In statistics, the mode is the value that occurs most frequently Avoid the use of this term, not particularly useful in reserves estimationPete
Rose MOST LIKELY
Synonymous with the mode
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UNCERTAINTY-BASED RESERVES ESTIMATES
A discrete value for each parameter is selected based on the evaluators
determination of the value that is most appropriate for the reserves
category
The resulting range of estimates prepared for the various reserves
categories reflects the associated degree of uncertainty Proved (1p) = high degree of confidence
Proved plus Probable (2p)= best estimate
Proved plus Probable plus Possible (3p) = Upside Case
This is a scenario based approach to deterministic reserves
Most commonly used internationally
UNCERTAINTY AND STATISTICAL CONCEPTS
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UNCERTAINTY AND STATISTICAL CONCEPTS
MINIMUM, BEST ESTIMATE AND MAXIMUM VALUES USING DETERMINISTIC
METHODS
REMINDER:
The use of most conservative parameters for proved will result in unrealistically low
estimates
Aggregating them results in even further conservatism
Conversely, use of most optimistic parameters for Proved plus Probable plus Possible
will result in unrealistically high estimates
In general, when reserves are estimated as a product of several
parameters, BEST ESTIMATE (neither conservative or optimistic),
should first be determined for all parameters
Appropriate constraints should then be imposed (i.e. LKH, or drainage)
1 or 2 of the key parameters may be varied from the BEST ESTIMATE as
appropriate.
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UNCERTAINTY AND STATISTICAL CONCEPTS
DETERMINE BEST ESTIMATE AS PROVED PLUS PROBABLE (2p)
Determine practical minimum and practical maximum that brackets the
quantities the evaluator believes with high confidence (P90 and P10)
The above order is unimportant is left to the particular evaluator
The proved estimate should generally lie in the range of 1/3 to 2/3 of the
difference between the Proved plus Probable estimate and the minimum The Proved plus Probable plus Possible estimate should generally lie in
the range of 1/3 to 2/3 of the difference between the Proved plus
Probable estimate and the maximum
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28
ORMEN LANGE VOLUMETRICS
Pressure 4263 psia
Depth 2750 m
Temp 62.8 C
145.04 F
Acre 302 million m2
Gross Pay 36.3 m
NTGR 0.909
Phi 0.281
Sg 0.704
Bg 266
RF 0.7
V= 1971.317 mm m3
Gas-in-plac 18609901 mm scf
Reserve= 13026931 mmcf
13026.93 bcf
13.0 tcf
Class Exercise:
Use the above reservoir parametersas the mean values and performprobabilistic estimates of IGIP &Reserves
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DETERMINISTIC VS. PROBABILISTIC
6-28-2
9-10
4-14
2-11
8-912-10
6-35
14-36
13-11
6-28-2
9-10
4-14
2-11
8-912-10
6-35
14-36
13-11
RESOURCE/RESERVE ESTIMATES
Volumetric MatrixNet Pay: 12.4 m
Porosity: 10.4%
Sw: 49.6%
Pressure: 8.3 MPa (1200 psi)
Bg: 72 scf/rescf
RF: 75%
Drainage: ~ 1/2 sect. (160 ~ 320 acres)
OGIP: 1.1 ~ 2.2 bcf
Reserves:Analogy/Probabilistic Estimates
Net Pay: 4 ~ 18 m
Porosity: 8.6% ~ 13.2%
Sw: 32% ~ 67%
Pressure: 1100 ~ 1650 psi
Bg: 65 ~ 100 scf/rescf
Drainage: ~ sect. (160 ~ 480 acres)
Reserves P50:
Production Forecast
IP rate: 500 mcf/d
Abandon rate: 50 mcf/d
Decline: hyperbolic (n=0.5)
Annual decline: 7% (final); 19% (initial)
Permeability: 0.19 ~ 0. 35 md
Shrinkage:
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PROBABILISTIC EXAMPLE
0
500
1,000
1,500
2,000
2,500
3,000
3,500
4,000
4,500
Jun-1994 Oct-1995 Mar-1997 Jul-1998 Dec-1999 Apr-2001 Sep-2002 Jan-2004 May-2005 Oct-2006 Feb-2008 Jul-2009
Date
GasRate(mcfd)
13-11 Commingled
8-2 NTKN
6-35 Comingled
2-11 NTKN
9-10 NTKN12-10 NTKN
14-36 Commingled
4-14 NTKN
8-2
13-11
4-14 6-35
14-36
2-11
9-10
12-10
0
200
400
600
800
1,000
1,200
1,400
Jun-1994 Oct-1995 Mar-1997 Jul-1998 Dec-1999 Apr-2001 Sep-2002 Jan-2004 May-2005 Oct-2006 Feb-2008 Jul-2009
Date
GasRate(mcfd
)
8-2 NTKN
2-11 NTKN
9-10 NTKN
12-10 NTKN
4-14 NTKN
8-2
12-10
9-10
4-14
2-11
0
200
400
600
800
1000
1200
1400
1600
1800
3 1-Ja n-19 93 2 8-Oc t-19 95 2 4-Ju l- 19 98 1 9-Ap r-20 01 1 4-Ja n-20 04 1 0-Oc t-20 06 6 -Jul -2 00 9
DATE
DATUMPRESSURES(psia)
13-11 Commingled
8-2 NTKN
6-35 Commingled
2-11 NTKN
9-10 NTKN4-14 NTKN
8-2
13-11
6-35
2-11
9-10
4-14
NTKN Gas C1 C2 C3
9-10 8 4. 94 7 .8 4 3. 35
8 7. 59 7 .4 7 2. 52
8 4. 97 7 .8 2 3. 57
4-14 83.05 7.6 2.84
8 6. 1 7 .7 8 3. 12
13-11 8 5. 55 7 .9 4 3. 21
8 5. 59 7 .7 3 3. 18
8 6. 31 7 .9 1 3. 03
8 8. 39 5 .6 5 3. 26
8-2 8 5. 87 7 .9 3 3. 01
2-11 8 4. 73 7 .9 7 3. 22
6-35 8 6. 08 7 .7 0 3. 22
Average= 8 5. 76 7 .6 1 3. 13
Co n d itio n s Res u lt s
Temp. Pressure Z Factor P/Z Density Cg Bg Bg Viscosity
F psia psia g /c c 1 /p si * 1 E6 bbl/MSCF SCF/cu ft cp
161 1800 0.851 2116.1 0.096 603.0 1.478 120.5 0.0158
161 1700 0.855 1988.4 0.090 642.6 1.573 113.3 0.0154
161 1600 0.860 1860.7 0.084 686.0 1.681 106.0 0.0151
161 1500 0.865 1733.2 0.079 733.9 1.804 98.7 0.0148
161 1400 0.872 1606.3 0.073 787.4 1.947 91.5 0.0145
161 1300 0.878 1480.3 0.067 847.7 2.112 84.3 0.0142
161 1200 0.885 1355.4 0.062 916.8 2.307 77.2 0.0139161 1100 0.893 1231.9 0.056 997.0 2.538 70.2 0.0137
161 1000 0.901 1109.9 0.050 1091.9 2.817 63.2 0.0135
161 900 0.909 989.6 0.045 1206.6 3.160 56.4 0.0133
161 800 0.918 871.1 0.040 1348.6 3.590 49.6 0.0131
161 600 0.937 640.2 0.029 1770.3 4.884 36.5 0.0128
161 500 0.947 528.0 0.024 2105.6 5.922 30.1 0.0127
161 400 0.957 417.9 0.019 2607.2 7.482 23.8 0.0126
161 1630 0.858 1899.0 0.086 672.6 1.647 108.2 0.0152
161 300 0.968 310.1 0.014 3441.9 10.084 17.7 0.0125
161 200 0.978 204.5 0.009 5109.6 15.293 11.6 0.0124
161 100 0.989 101.1 0.005 10110.5 30.924 5.8 0.0123
161 14.7 0.998 14.7 0.001 68137.8 212.367 0.8 0.0123
Upside Most likely Risk
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Brazeau River Nisku A PoolRecovery Options & STOIIP
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West Pembina Brazeau River Nisku A Pool
wabamungroup
winterburngroup
beaverhill
lake group
woodbendgroup
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West Pembina Brazeau River Nisku A Pool
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West Pembina Brazeau River Nisku A Pool
Nisku A Pool
Original OOIP Estimate:33.34 mmbblYE 2009 Cum Oil Volume:27.16 mmbblRecovery Factor: 82%
Original GOR1000 scf/bblOSGIP based on GOR33.34 bcf
2009 YE Cum Gas Volume:122.55 bcfCycled Gas Volume:82.08 bcfNet Gas Production:40.46 bcf
The Cum Gas deficit40.46 33.34 = 7.12 bcf(if assume little remaininggas is remaining today)
PHH modeling studysuggested in 2007:OOIP = 40.8 mmbbl(reached a good historymatch with the corrected oilcompressibility for theunder-saturated oil case;PHH did not complete thefinal history match work)
Recovery Factor: 67%
Nisku A Pool History
Discovered in 1977
Original Pressure46,581 kPaReservoir Temperature102 oCGas Cycling Soak-Pressure37,500 kPaCurrent Pool Pressure900 kPa
Wells:100/5-6-49-12W5 (injector)100/15-31-48-12W5100/11-31-48-12W5102/11-31-48-12W5 HZ SUSP.
Primary DrainageJan 1978 ~ March 1980P res. at 1980 = 20 mPa
Dry Gas Cycling FloodingInjection Began: Sept 1980
Injector: 5-6-49-12W5 (topstructure)Injection Stopped: Aug 1995Total Injection Gas: 80.08 bcf
Oil Pbubble = 21 mPaMiscible Flood OperatingPressures: 37 mPa
Oil API Gravity: 45 oAPISweet gas
7-31
11-31
(300 m)
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West Pembina Brazeau River Nisku A PoolBrazeau River Nisku "A" Pool Production
0
1
10
100
Aug-76 May-79 Feb-82 Nov-84 Aug-87 May-90 Jan-93 Oct-95 Jul-98 Apr-01 Jan-04 Oct-06 Jul-09 Apr-12
Year
GasRate(mmscf/d)
0
1,000
2,000
3,000
4,000
5,000
6,000
7,000
8,000
9,000
10,000
CondyOilRate(bbl/d)
11-31
5-6
5-6 dry gas injection; 82 bcf
11-31 HZ online
jan 1991
15-31
drilled
Brazeau River Nisku "A" Pool Pressure History
0
500
1,000
1,500
2,000
2,500
3,000
3,500
4,000
4,500
5,000
5,500
6,000
6,500
Aug-76 May-79 Feb-82 Nov-84 Aug-87 May-90 Jan-93 Oct-95 Jul-98 Apr-01 Jan-04 Oct-06 Jul-09 Apr-12
Year
Poo
Presures
(psia)
15-31
5-6
11-31
Series4
5-6 dry gas injection; 82 bcfPi = 45 MPa
Pcycling = 38 MPa
primary
production
final
depletionPbubble = 21 MPa
Brazeau River Nisku "A" Pool GOR Trend
100
1,000
10,000
100,000
1,000,000
10,000,000
100,000,000
8/28/76 5/25/79 2/18/82 11/14/84 8/11/87 5/7/90 1/31/93 10/28/95 7/24/98 4/19/01 1/14/04 10/10/06 7/6/09 4/1/12
Date
GOR(scfd/bbl)
11-31 HZ
5-615-31
11-31 02
5-6 injector 82.08 bcf
Initial Gas SolubilityProduction GOR
Reservoir Engineering Highlights
It is very probable that A pool has 40.8 mmbbl oil, 7.5 mmbblmore than the historical estimates on the book The higher OOIP is supported by the original GOR 1000 scf/bbl,the early pressure history data, and the PHH study based on thecorrection of the oil compressibility (undersaturated reservoirduring its primary production, and the cum gas volume (40 bcf) Areal/volumetric swept efficiency is the most challenginguncertainty to implement future enhanced oil recovery operation;the current well pattern/spacing, the 15-y high pressure injectionplus the subsequent years depletion drive, have swept mostsweepable oil; any new EOR scheme of less degrees is likely notto produce any significant amount of oil A substantial amount of cycling gas is required to raise the poolpressure level to 38 MPa in order to reach the miscible pressurecondition toward better miscible flooding
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Probabilistic Reserve Evaluations
West Pembina Brazeau River Nisku A Pool
Brazeau River Nisku "A" Pool Pressure History
0
500
1,000
1,500
2,000
2,500
3,000
3,500
4,000
4,500
5,000
5,500
6,000
6,500
7,000
7,500
Aug-76 May-79 Feb-82 Nov-84 Aug-87 May-90 Jan-93 Oct-95
Year
PooPresures(psia)
15-31
5-6
11-31
11-31 02
5-6 dry gas injection; 82 bcfPi = 45 MPa
Pcycling = 38 MPa
primary
production
final
depletion
Pbubble = 21 MPa
7-31
5-6injector
11-31producer
15-31producer
7-31 HZproducer
GOC
gas coning
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West Pembina Brazeau River Nisku A Pool
To evaluate gas storage project prospect, BPhired PHH to build a numerical model &
history match the performance (2008)
In order to make up the cum gas deficit, PHH
had to add an invisible cache vaguely
attached to the A pool, which contained
40 bcf of gas slowly leaking into the pool
over 15 years
In the end, they found that they paid too
much attention to the gas cycling part of the
history, and ignored the early production,
which gives the correct oil compressibility
during the primary depletion drive
Like in PTA analysis, compressibility terms
are often ignored and many times it makes a
big difference
7-31
Nisku A Pool
Original OOIP Estimate:33.34 mmbblYE 2009 Cum Oil Volume:27.16 mmbblRecovery Factor: 82%
Original GOR1000 scf/bblOSGIP based on GOR33.34 bcf
2009 YE Cum Gas Volume:122.55 bcfCycled Gas Volume:82.08 bcfNet Gas Production:40.46 bcf
The Cum Gas deficit40.46 33.34 = 7.12 bcf(if assume little remaininggas is remaining today)
PHH modeling studysuggested in 2007:OOIP = 40.8 mmbbl(reached a good historymatch with the corrected oilcompressibility for theunder-saturated oil case;PHH did not complete thefinal history match work)
Recovery Factor: 67%
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Probabilistic Reserve Evaluations
West Pembina Brazeau River Nisku A Pool
(1 )
w wi f p o o oi oi
wi
c S cN B N B B NB p
S
(1 )
o oi w wi f p o oi
oi wi
B B c S cN B NB p
B S
o oio
oi
B Bc
B p
(1 )w wi f p o oi o
wi
c S cN B NB c pS
(1 )
o o w wi f p o oi
wi
c S c S cN B NB p
S
p o oi eN B NB c p
o oi eV V c p
p oie
o
N BRF c p
N B
Undersaturated Oil Reservoirs
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Brazeau River Nisku "A" Pool Pressure History
0
500
1,000
1,500
2,000
2,500
3,000
3,500
4,000
4,500
5,000
5,500
6,000
6,500
7,000
7,500
Aug-76 May-79 Feb-82 Nov-84 Aug-87 May-90 Jan-93 Oct-95
Year
PooPresures
(psia)
15-31
5-6
11-31
11-31 02
5-6 dry gas injection; 82 bcfPi = 45 MPa
Pcycling = 38 MPa
primary
production
inal
depletion
Pbubble = 21 MPa
West Pembina Brazeau River Nisku A Pool
Muhammad Ali Al-Marhoungas specific gravity = 0.652
a1 = -14.1042 Pi= 112,000 kPa 16244.1 psia surface oil relative density = 0.850
a2 = 2.7314 P bubble = 20,995 kPa 3045.0 psia relative oil density at Pb = 0.668
a3 = -5.60605E-05 T = 110oC 230
oF original GOR = 240 m3/m3a4 = -580.8778 oil FVF at Pb = 1.560 resm3/m3
Vasquez and Beggs
O ri gi nal M id dl e E ast
a1 = -1.43300E-02 0.0023386
a2 = 5.00000E-05 3.69769E-05
a3 = 1.72000E-04 5.53945E-05 Al-Marhoun Result Vasquez & Beggs Resulta4 = -1.18000E-02 -0.0081716
a5 = 1.26100E-04 5.82514E-05 ln (Co) = -13.34122171
Oil Compressibility Co = 1.6069E-06 1/psi Oil Compressibility Co = 8.9806E-06 1/psi
Poros i ty Nisku "A"
Nisku Water Salinity 11% Pressures Vasquez&Beggs Al-Marhoun T ot al S w i= 10 %, S o =9 0%
200,000 ppm 1000 ppm Cr (1/psi) (psia) (1/psia) (1/psia) Compress ibi l i ty
Co ln(Co) Co V&B Al-M C o/C t C r/C t
2.08204E-06 2.91220E-06 4.66745E-06 6780.9 1.3174E-05 -11.559 9.5521E-06 1.68151E-05 1.35556E-05 70.47% 34.43%
2.08321E-06 2.91385E-06 4.66745E-06 6757.9 1.3219E-05 -11.554 9.5936E-06 1.68556E-05 1.35931E-05 70.58% 34.34%
2.08582E-06 2.91749E-06 4.66745E-06 6706.9 1.3319E-05 -11.545 9.6862E-06 1.69465E-05 1.36768E-05 70.82% 34.13%
2.09664E-06 2.93263E-06 4.66745E-06 6494.9 1.3754E-05 -11.505 1.0081E-05 1.73393E-05 1.40335E-05 71.83% 33.26%
2.09679E-06 2.93284E-06 4.66745E-06 6491.9 1.3760E-05 -11.504 1.0087E-05 1.73450E-05 1.40386E-05 71.85% 33.25%
2.10154E-06 2.93948E-06 4.66745E-06 6399.0 1.3960E-05 -11.487 1.0265E-05 1.75255E-05 1.41995E-05 72.29% 32.87%
2.10172E-06 2.93973E-06 4.66745E-06 6395.4 1.3968E-05 -11.486 1.0272E-05 1.75326E-05 1.42058E-05 72.31% 32.86%
2.10249E-06 2.94081E-06 4.66745E-06 6380.3 1.4001E-05 -11.483 1.0301E-05 1.75624E-05 1.42322E-05 72.38% 32.79%
2.11071E-06 2.95230E-06 4.66745E-06 6219.4 1.4363E-05 -11.453 1.0618E-05 1.78896E-05 1.45187E-05 73.13% 32.15%
2.12057E-06 2.96609E-06 4.66745E-06 6026.3 1.4823E-05 -11.417 1.1011E-05 1.83052E-05 1.48740E-05 74.03% 31.38%
2.12151E-06 2.96742E-06 4.66745E-06 6007.8 1.4869E-05 -11.413 1.1049E-05 1.83464E-05 1.49087E-05 74.11% 31.31%
2.12243E-06 2.96870E-06 4.66745E-06 5989.8 1.4914E-05 -11.410 1.1087E-05 1.83867E-05 1.49426E-05 74.20% 31.24%
2.12592E-06 2.97358E-06 4.66745E-06 5921.5 1.5086E-05 -11.397 1.1231E-05 1.85420E-05 1.50723E-05 74.51% 30.97%
2.12608E-06 2.97380E-06 4.66745E-06 5918.4 1.5094E-05 -11.396 1.1237E-05 1.85491E-05 1.50782E-05 74.53% 30.95%
2.12721E-06 2.97538E-06 4.66745E-06 5896.3 1.5150E-05 -11.392 1.1284E-05 1.86002E-05 1.51206E-05 74.63% 30.87%
2.12868E-06 2.97744E-06 4.66745E-06 5867.5 1.5225E-05 -11.387 1.1345E-05 1.86674E-05 1.51760E-05 74.76% 30.76%
2.13106E-06 2.98077E-06 4.66745E-06 5820.8 1.5347E-05 -11.378 1.1446E-05 1.87776E-05 1.52666E-05 74.97% 30.57%
2.13464E-06 2.98578E-06 4.66745E-06 5750.6 1.5534E-05 -11.365 1.1598E-05 1.89467E-05 1.54042E-05 75.29% 30.30%
2.13522E-06 2.98659E-06 4.66745E-06 5739.3 1.5565E-05 -11.363 1.1623E-05 1.89743E-05 1.54265E-05 75.34% 30.26%
2.18121E-06 3.05091E-06 4.66745E-06 4838.7 1.8462E-05 -11.193 1.3771E-05 2.15880E-05 1.73668E-05 79.30% 26.88%
2.20877E-06 3.08946E-06 4.66745E-06 4298.9 2.0780E-05 -11.091 1.5245E-05 2.36783E-05 1.86971E-05 81.54% 24.96%
2.21645E-06 3.10021E-06 4.66745E-06 4148.4 2.1534E-05 -11.063 1.5684E-05 2.43578E-05 1.90927E-05 82.14% 24.45%
2.21648E-06 3.10025E-06 4.66745E-06 4147.8 2.1537E-05 -11.063 1.5685E-05 2.43606E-05 1.90943E-05 82.15% 24.44%
2.21741E-06 3.10155E-06 4.66745E-06 4129.7 2.1631E-05 -11.059 1.5739E-05 2.44457E-05 1.91427E-05 82.22% 24.38%
2.21782E-06 3.10212E-06 4.66745E-06 4121.7 2.1673E-05 -11.058 1.5763E-05 2.44836E-05 1.91641E-05 82.25% 24.36%
2.21909E-06 3.10390E-06 4.66745E-06 4096.7 2.1805E-05 -11.053 1.5837E-05 2.46028E-05 1.92312E-05 82.35% 24.27%
2.21939E-06 3.10432E-06 4.66745E-06 4090.9 2.1836E-05 -11.052 1.5854E-05 2.46306E-05 1.92469E-05 82.37% 24.25%2.23764E-06 3.12984E-06 4.66745E-06 3733.5 2.3927E-05 -10.985 1.6958E-05 2.65145E-05 2.02431E-05 83.77% 23.06%
2.24609E-06 3.14166E-06 4.66745E-06 3568.0 2.5037E-05 -10.954 1.7495E-05 2.75145E-05 2.07275E-05 84.41% 22.52%
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Nisku "A" Pool Total Compressibility Estimates
0.0E+00
5.0E-06
1.0E-05
1.5E-05
2.0E-05
2.5E-05
3.0E-05
3,000 3,500 4,000 4,500 5,000 5,500 6,000 6,500 7,000
Pool Pressures (psia)
Oil&TotalCompressibilities(1/ps
ia)
Vasquez&Beggs
Total Compressibility (V&B)
West Pembina Brazeau River Nisku A Pool
gas specific gravity = 0.652
Pi = 46,439 kPa 6735.4 psia surface oil relative density = 0.807 43.78 oAPI
P bubble = 20,995 kPa 3045.0 psia relative oil density at Pb = 0.609
T = 103oC 217
oF original GOR = 178 m3/m3 1000 scf/bbl
oil FVF at Pb = 1.560 resm3/m3 1.560 resb/stb
Brazeau River Nisku "A" Pool Cum Oil Match
0.0
0.5
1.0
1.5
2.0
2.5
Oct-77 Jan-78 Apr-78 Jul-78 Nov-78 Feb-79 May-79 Sep-79 Dec-79 Mar-80 Jun-80 Oct-80
year
cumoil(mmbbl)&cumgas(bcf)
0
1,000
2,000
3,000
4,000
5,000
6,000
7,000
8,000
averagepoolpressure(psia)
Cum Oi (actual)l
Cum Gas (actual)
Cum Oil Estimates (40.8 mmbbl)
Cum Oil Estimates (33.3 mmbbl)
Pool Pressures History
40.8 mmbbl
33.3 mmbbl
pool pressure history
The most popular Vasquez&Beggs correlation is used to estimate
Nisku A oil compressibility & the total compressibility, which is
then used to estimate the cum oil production for each step of the
pools pressure decline. 40 mmbbl OOIP seems to be a better
match with the actual production. Al-Marhoun correlation seems
to over-estimate the oil production.
Nisku rock compressibility remains the least known input, which
makes 20~30% of the total compressibility. It is estimated by the
correlation developed in SPE 88464.
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Brazeau River Nisku "A" Pool Production
0
1,000
2,000
3,000
4,000
5,000
6,000
7,000
8,000
Aug-76 May-79 Feb-82 Nov-84 Aug-87 May-90 Jan-93 Oct-95 Jul-98 Apr-01 Jan-04 Oct-06 Jul-09 Apr-12 Dec-14
Year
OilRate(bblf/d)
0
2
4
6
8
10
12
14
16
18
CumO
il(mmbbl)
5-6 Oil Rate
11-31 Oil Rate
15-31 Oil Rate
11-31 HZ Oil Rate
5-6 Cum Oil
11-31 Cum Oil
15-31 Cum Oil
11-31 HZ Cum Oil
11-31
11-31 HZ
15-31
16.75 mmbbl
7.66 mmbbl
1.75 mmbbl
1.00 mmbbl
4 wells combined
27.16 mmbbl
5-6
gas injection ended
blowdown began
West Pembina Brazeau River Nisku A Pool
Cum Oil at Aug 1995 = 25.56 mmbbl
oil incremental between Aug 95 & Dec 09 = 1.6 mmbbl
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Brazeau River Nisku "A" Pool Production
1
10
100
1,000
10,000
Aug-76 May-79 Feb-82 Nov-84 Aug-87 May-90 Jan-93 Oct-95 Jul-98 Apr-01 Jan-04 Oct-06 Jul-09 Apr-12 Dec-14
Year
OilRate(bblf/d)
0
2
4
6
8
10
12
14
16
18
CumO
il(mmbbl)
11-31 HZ
11-31: 16.75 mmbbl
11-31 HZ: 1.75 mmbbl
11-31gas injection ended
blowdown began
West Pembina Brazeau River Nisku A Pool
Nisku "A" Pool Performa nce betwee n 11-31 and 11-31 HZ
1
10
100
1000
10000
May-90 Sep-91 Jan-93 Jun-94 Oct-95 Mar-97 Jul-98 Dec-99 Apr-01 Sep-02 Jan-04 May-05 Oct-06
Year
OilRateDifferential(bbl/day)
0.0
0.1
0.2
0.3
0.4
0.5
0.6
0.7
0.8
0.9
1.0
IncrementalCumOil(mmbb
Rate Differencel
Cum Incremental
injection ended;blowdown began
0.75 mmbbl0.94 mmbbl
If we assume 15-31 was not affected
The net incremental oil production fromdrilling 11-31 horizontal well seems to bemuch less than the projected/recorded 1.75mmbbl oil due to the competitive drainage
with the original 11-31 vertical well. The netcum oil incremental was most likely less than0.84 mmbbl, or 2% additional recovery ofthe total OOIP (40.8 mmbbl)
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West Pembina Brazeau River Nisku A PoolBrazeau River Nisku "A" Pool
0
1000
2000
3000
4000
5000
6000
7000
8000
9000
10000
0 2 4 6 8 10 12 14 16 18 20 22 24 26 28 30
Cum Oil Production (mmbbl)
OilRate(bbl/d)
11-31
11-31 HZ
15-31
5-6
Nisku "A" Pool
he entire pool
25.558 mmbbl
before blowdown
11-31 well
16.419 mmbbl
before blowdown
15-31 well
7.209 mmbbl
before blowdown
11-31 HZ well caused 15-31/11-31 production loss
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West Pembina Brazeau River Nisku A Pool
2010
Depleted pressures
Wells are dying
1~2 bcf remaining gas
Remaining bbl oils
Options Decommision the pool
Convert to gas storage
Re-initiate gas cycling
Partners wanted to do both
storage/EOR
Questions?
STOIIP, RF, & remaining for EOR Gas storage alone?