pete 310 - petroleum engineering reservoir... · pete 310 lecture # 8: five reservoir fluids...
TRANSCRIPT
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PETE 310
Review Lecture # 7
Three & Multicomponent Mixtures…
Plus
Lecture # 8 – Chapter 5
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Ternary Diagrams: Review
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Ternary Diagrams: Review
Pressure Effect
C3C3
nC5 C3
C1
Gas
p=14.7 psia
C1
nC5
2-phase
Liquid
p=380 psiaC3 nC5
C1
C3
2-phase
Liquid
p=500 psia
C1
2-phase
Liquid
nC5p=1500 psia
2-phase
Liquid
C1
nC5p=2000 psia
C1
nC5 C3
Liquid
p=2350 psia
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Ternary Diagrams: Review
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C1
C10 n-C4
x
Dilution Lines
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Ternary Diagrams: Review
Quantitative Representation of Phase Equilibria - Tie (or equilibrium) lines
Tie lines join equilibrium conditions of the gas and the liquid at a given pressure and temperature
Bubble point curve gives the liquid composition
Dew point curve gives the gas composition
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Ternary Diagrams: Review
Quantitative Representation of Phase Equilibria - Tie (or equilibrium) lines
All mixtures whose overall composition (zi) is along a tie line have the SAME equilibrium gas (yi) and liquid composition (xi), but the relative amounts on a molar basis of gas and liquid (fvand fl) change linearly (0 – vapor at B.P., 1 –liquid at B.P.).
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Illustration of Phase Envelope and Tie Lines
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C1
C10 n-C4
CP
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Uses of Ternary Diagrams
Representation of Multi-Component Phase Behavior with a Pseudoternary DiagramTernary diagrams may approximate phase behavior of multi-component mixtures by grouping them into 3 pseudocomponents
heavy (C7+)
intermediate (C2-C6)
light (C1, CO2 , N2- C1, CO2-C2, ...)
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Uses of Ternary Diagrams
Miscible Recovery Processes
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1
C1
C2-C6C7+
A
O
Solvent1
oil
Solvent2
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ExerciseFind overall composition of mixture made with 100 moles oil "O" + 10 moles of mixture "A".
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C1
C2-C6C7+
A
O
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Mixture C1-nC4-C10
@ p=2500 psi, T=160 oF
0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 1
liquid phase
gas phase
gridlines
triangle
equilibrium
C1
nC4C10
liquid phase
xC1 xC4 xC10 x y
0.494 0.000 0.506 0.247 0.427816
0.496 0.101 0.403 0.349 0.429548
0.509 0.197 0.294 0.4515 0.440807
0.534 0.280 0.186 0.547 0.462457
0.600 0.320 0.080 0.62 0.519615
0.670 0.310 0.020 0.645 0.580237
gas phase
yC1 yC4 yC10
0.994 0.000 0.006 0.497 0.860829
0.965 0.028 0.007 0.5105 0.835714
0.927 0.064 0.009 0.5275 0.802805
0.874 0.115 0.011 0.552 0.756906
0.800 0.186 0.014 0.586 0.69282
0.740 0.247 0.013 0.617 0.640859
http://www.pe.tamu.edu/barrufet/public_html/PETE310/index.html
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Practice Ternary Diagrams
Pressure Effect
T=180F
P=14.7 psiaPressure Effect
O
T=180F
P=200 psia
C1-C3-C10
Pressure Effect
O
T=180F
P=400 psia
Pressure Effect
O
T=180F
P=600 psia
Pressure Effect
O
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Practice Ternary DiagramsPressure Effect
T=180F
P=1000 psia
Pressure Effect
O
T=180F
P=1500 psia
Pressure Effect
O
T=180F
P=2000 psia
O
T=180F
P=3000 psia
O
T=180F
P=4000 psia
O
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Practice Ternary Diagrams
Temperature Effect
T=100F
P=2000 psia
Temperature Effect
O
T=150F
P=2000 psia
Temperature Effect
O
T=200F
P=2000 psia
Temperature Effect
O
T=300F
P=2000 psia
Temperature Effect
O
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Practice Ternary Diagrams
Temperature Effect
T=350F
P=2000 psia
Temperature Effect
O
T=400F
P=2000 psia
Temperature Effect
O
T=450F
P=2000 psia
Temperature Effect
O
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Pressure-Temperature Diagram for Multicomponent Systems
Reserv
oir
Pre
ssu
re
Reservoir Temperature
60%
20%0%
2-Phase
1-Phase 1-Phase
CP
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Changes During Production and Injection
Temperature
t1
Pre
ssu
re
t3
t2
Gas
Injection
Production
t
t3
2
Gas
Injection
Production
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PETE 310
Lecture # 8: Five Reservoir Fluids (Chapter 5)
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Pressure vs. Temperature Diagrams
Used to visualize the fluids production path from the reservoir to the surface
To classify reservoir fluids
Visualize miscible processes
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Pressure-Temperature Diagram for Multicomponent SystemsR
eserv
oir
Pre
ssu
re
Reservoir Temperature
60%
20%0%
2-Phase
1-Phase 1-Phase
CP
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Why do we need to classify Reservoir Fluids?
Determine fluid sampling
Determine types and sizes of surface equipment
Dictate depletion strategy
Determine selection of EOR method
Determine techniques to predict oil & gas reserves
Determine Material Balance calculations
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Phase Envelopes
CriticalPoint
Cricondenbar
Cricondentherm
BubblepointCurve
Dew Point Curve
QualityLines
Temperature
Pre
ssu
re 75%
50%
25%
Fixed
Composition
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Classification of Reservoirs based on Phase Diagram
Gas Reservoirs (Single Phase)
Gas Condensate Reservoirs (Dew-Point Reservoirs):
Undersaturated Solution-Gas Reservoirs (Bubble-Point Reservoirs):
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Phase Diagram of a Dry Gas Reservoir
Temperature
Pre
ssu
re
Path of Production
Initial Reservoir
Conditions
Separator Conditions
CP
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Phase Diagram of a Wet Gas Reservoir
Temperature
Pre
ss
ure
Path of Production
Initial Reservoir
Conditions
Separator Conditions
CP
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Phase Diagram of a Retrograde Gas Reservoir
Temperature
Pre
ss
ure
Initial Reservoir
Conditions
CP
Path of Production
Separator Conditions
Temperature
Pre
ss
ure
Initial Reservoir
Conditions
CP
Path of Production
Separator Conditions
Temperature
Pre
ss
ure
Initial Reservoir
Conditions
CP
Path of Production
Separator Conditions
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Phase Diagram of a Volatile Oil Reservoir
Temperature
Pre
ss
ure
Initial Reservoir
Conditions
CP
Path of Production
Separator Conditions
75%
50%25%
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Phase Diagram of a Black Oil Reservoir
Temperature
Pre
ss
ure
Initial Reservoir
Conditions
CPPath of Production
Separator Conditions
25%
50%75%
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Phase envelopes of different mixtures with different proportions of same HC
components
0
1000
2000
3000
4000
5000
6000
7000
Pre
ssu
re (
psia
)
-200 -100 0 100 200 300 400 500 600 700 800
Temperature o
F
Critical Points
Dry Gas
Wet Gas
Condensate
Volatile I
Black Oil
TR
Volatile I
Volatile II
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Typical Reservoir Fluid CompositionsComponent Black Oil Volatile Oil Gas Condensate Wet Gas Dry Gas
C1 48.83 64.36 87.07 95.85 86.67
C2 2.75 7.52 4.39 2.67 7.77
C3 1.93 4.74 2.29 0.34 2.95
C4 1.60 4.12 1.74 0.52 1.73
C5 1.15 3.97 0.83 0.08 0.88
C6 1.59 3.38 0.60 0.12
C7+
42.15 11.91 3.80 0.42
MwC7+
225 181 112 157
GOR 625 2000 18,200 105,000 -
Tank oAPI 34.3 50.1 60.8 54.7 -
Liquid
Color
Greenish
Black
Medium
Orange
Light
Straw
Water
White
-
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Compositional Distribution ofReservoir Fluids
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Classification of Reservoirs based on Production and PVT
data
GAS CONDENSATE RESERVOIRS:
GOR between 70,000-100,000 SCF/STB
Density greater than 60 ºAPI
Light in color
C7+ composition < 12.5%
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Classification of Reservoirs based on Production and PVT
data
VOLATILE OIL RESERVOIRS:
GOR between1,000-8,000 SCF/STB
Density between 45-60 ºAPI
Oil FVF greater than 2.00 (high shrinkage oils)
Light brown to green in color
C7+ composition > 12.5%
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Classification of Reservoirs based on Production and PVT data
BLACK OIL RESERVOIRS:GOR less than 1,000 SCF/STB
Density less than 45 ºAPI
Reservoir temperatures less than 250 ºF
Oil FVF less than 2.00 (low shrinkage oils)
Dark green to black in color
C7+ composition > 30%
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Assignment
Read and make a summary of revised & newer criteria for classification of Reservoir Fluids from given paper by William D. McCain in JPT September 1994
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JPT paper Study Guide
What are the distinctive features of black oils in terms of
Initial GOR & GOR vs time
Initial API & API vs time
Compositions
Color
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JPT paper Study Guide
What are the distinctive features of volatile oils in terms of
Initial GOR & GOR vs time
Initial API & API vs time
Compositions
Color
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JPT paper Study Guide
What are the distinctive features of Condensate gases in terms of
Initial GOR & GOR vs time
Initial API & API vs time
Compositions
Color
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JPT paper Study Guide
What are the distinctive features of Dry gases in terms of
Initial GOR & GOR vs time
Compositions