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Lecture # 26 Chapter 12 Gas-Liquid Equilibrium Non-ideal VLE
PETE 310 Lecture # 26 Chapter 12 Gas-Liquid Equilibrium Non-ideal VLE
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Gas-Liquid Equilibrium Non Ideal Behavior
Applications to low & high pressures Use models for the equilibrium ratios (ki-values) Simpler models ki = f (P,T) More complex models ki = f(P,T,compositions) use equations of state EOS, convergence pressure
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VLE general (same) The equilibrium criteria between 2 phases a and b is,
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Statement of Equilibrium
Most general case is that Ki is a function of P, T, and compositions 1 P 2 3 T
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Mathematical Relationships
with In general
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Bubble Point Evaluation (Non-Ideal Behavior Model)
The bubble point pressure at a given T is
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Bubble Point T s P 1 zi=xi s P 2 x ,y 1 1
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Dew Point Calculation At the dew point the overall fluid composition coincides with the gas composition. That is.
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Dew Point Calculation (Non-Ideal Behavior Model)
Find DP pressure and equilibrium liquid compositions
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Dew Point T s P 1 s P zi=yi 2 x ,y 1 1
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Flash Calculations In this type of calculations the objective is to:
find fraction of vapor vaporized (fv) and equilibrium gas and liquid compositions given the overall mixture composition, P and T.
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Flash Calculations (Non-Ideal Behavior Calculations)
Start with the equilibrium equation Material balance
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Flash Calculations Now replace either liquid or gas compositions using Ki values (exercise derive the expression)
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Flash Calculations Objective function (flash function) is
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Flash Calculations There are several equivalent expressions for the flash function (a) (b) (c)
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One of the Models for Equilibrium Ratios
1. Require critical properties & acentric factors
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Example calculations in excel file VLE_310
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