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