PETE 310 - Petroleum Engineering k...PETE 310 Lecture # 29 ... For black oils simple K-value...
Transcript of PETE 310 - Petroleum Engineering k...PETE 310 Lecture # 29 ... For black oils simple K-value...
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PETE 310
Lecture # 29
Chapter 14
Equilibrium Ratio Correlations (K-values)
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Gas-Liquid Equilibrium Non Ideal Behavior
When evaluating VLE we use models for the equilibrium ratios (Ki-values)
Simpler models Ki = f (P,T)
low pressure applications
explicit
More complex models Ki = f(P,T,xi,yi) use equations of state EOS (current), or convergence pressure methods (earlier)
apply lo low and high pressures
implicit, highly iterative
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What’s a “low” or a “high” pressure?
Separator pressures for a black oil are usually considered low
Reservoir pressures considered high are > 1000 psia, but this limit depends upon type of fluid
For black oils simple K-value correlations do a good job
Volatile oils and gas condensates have a more complex behavior
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K-values
Compositionally independent correlations assume that k-values depend upon pressure and temperature only
In fact Ki values depend upon the type and proportions of other molecules in the mixture
Example: Your behavior is different when you are surrounded by people of your same age than when you are surrounded by professors, or potential employers
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Statement of Equilibrium
Only component 3 has a vapor pressure for the selected T – 2 & 1 are supercritical
iii Kxy
P
T
1
2 3
3P
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Bubble Point & Dew Point Evaluations
The bubble point pressure at a given T is
The dew point pressure at a given T is
,...)T,pKzy bpiii,...T,pKz1 bpii
,...)T,p(Kxz
Kxy
dpiii
iii
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Flash Calculations
Objective function (flash function) is
01fKf1
Kz)f(F
viv
iiv
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One of the Models for Equilibrium Ratios
T
T1137.5exp
p
pK ci
ici
i
Requires critical properties & acentric factors
We need other models for higher pressures
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For higher pressures and temperatures
Equilibrium ratio charts for different convergence pressures
Tedious but…
Illustrate fundamental concepts
Equations of State (mainly cubic)
Tedious by hand
Suitable for computers
More in later lectures
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Convergence Pressure Equilibrium Ratio Charts
Plot Ki vs p in a log-log scale
K-values converge to a unique pressure called convergence pressure
But this ‘convergence pressure’ depends upon type of fluid
Black oils have convergence pressures of about 10000 psia
Observed experimental behavior (see Fig. 14-1 and 14-2) of text book
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Convergence Pressure Highlights
Is a property that takes into account the compositional effect
When the mixture is a volatile oil the K-values of their components have convergence pressures of about 7000 psia
When the mixture is a gas condensate the K-values of their components have convergence pressures of about 5000 psia
Book contains only charts for convergence pressure (pk) of 5,000 psia
90 Convergence pressure charts are tabulated for pk’s of 800, 1000, 1500, 2000, 3000, 5000, and 10000
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Convergence Pressure Highlights
Convergence pressure is found iteratively
Some interpolation may be needed among charts
Charts have not been digitized and no publicly available equations have been generated from these charts (GPSA have computer codes at a cost)
Procedure is lengthy and tedious
For repetitive computations (reservoir simulation), Equations of State (EOS) have replaced this methodology
Still a good approach for few calculations
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Other Uses of Convergence Pressure Charts
To determine the pressure range of ideal behavior
To have a quick comparison among K-values of different components
To estimate vapor pressures
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Convergence Pressure Equilibrium Ratio Charts
Note the slope for low pressures…
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Errors: Black Oil at Surface Conditions
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Errors: Black Oil at Surface Conditions
What would be the percent error in the evaluated liquid produced at 65 psia and 120 oF if the K-value for methane is
15% higher than the actual value
15% lower than the actual value
How about the effects of the other components in the mixture?
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Errors: Retrograde Gas at Reservoir Conditions
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Errors: Retrograde Gas at Reservoir Conditions
What would be the percent error in the evaluated liquid volume at 2650 psia and 195 oF if the K-value for C7
+ is
15% higher than the actual value
15% lower than the actual value
Which are the most ‘influential’ components
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Equilibrium Ratios for Methane Convergence Pressure = 5000 psia
Note the slope and dotted lines
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Equilibrium Ratios for Ethane Convergence Pressure = 5,000 psia
Given a temperature lower than the Tc
of C2, How can we estimate the vapor pressure of C2 from this chart?
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Equilibrium Ratios for Octane Convergence Pressure = 5,000 psia
According to this chart, what is the pressure range for which we could have used the Raoult’s law model for KC8 as a very good approximation?
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Standings K-value Correlation (SPE 7903)
Correlation good for Pressures up to 1000 psia
Observed behavior
F is a component characterization factor
Number in chart indicates compound
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Standings K-value Correlation (SPE 7905, JPT - September 1979)
Correlation is
With
p
10K
cFa
i
T
1
T
1bF
bi
i
cibi
ci
i
T
1
T
1
7.14
plog
b
(T in oR and p in psia)
biTIs the normal boiling point temperature of the component
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Standings K-value Correlation (SPE 7905, JPT - September 1979)
Correlation is (F already defined)
With
p
10K
cFa
i
284
284
p105.3p107.189.0c
p1015p105.42.1a
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Values for bi and Tb (from SPE paper)
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For heptanes and heavier we can use…
We will use the following approach
Other approaches include using an equivalent carbon number that determines a normal boiling point for the heavy fraction (paper)
77CC
K15.0K
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Modified Homework
Use the data from problem 14-1 and determine the K-value for each component at T = 160oF and p = 1500 psia
Compare the K-values with the K-values provided in the book – Indicate the % differences
Calculate the initial oil composition if the fraction of gas produced with the ‘old K-values’ is 10%
Use the recently obtained reservoir composition with the new K-values, run a flash and determine the new gas fraction.
Compare with the previously reported one and discuss
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