(a) A gas-phase A+B system solvates A + B AB with K a = 0.5 at...
Question:
(a) A gas-phase A+B system solvates A + B ⇆ AB with Ka = 0.5 at 298.15 K. Calculate the compressibility factor, apparent fugacity coefficients, and the true vapor phase mole fractions in a mixture at 298.15 K and 2 bar when the apparent concentration is yA = 0.45 using ideal chemical theory.
(b) A liquid-phase A+B system solvates A + B ⇆ AB with Ka = 0.7 at 298.15 K. Calculate the true liquid-phase mole fractions in a mixture at 298.15 K and 1 bar when the apparent concentration is xA = 0.45 using ideal chemical theory.
(c) A gas-phase A+B system associates 2A ⇆ A2 with Ka = 0.5 at 298.15 K. Calculate the compressibility factor, apparent fugacity coefficients, and the true vapor phase mole fractions in a mixture at 298.15 K and 2 bar when the apparent concentration is yA = 0.45 using ideal chemical theory.
Step by Step Answer:
To solve these questions you can use ideal chemical theory which involves the concept of chemical equilibrium and fugacity The fugacity coefficient is a measure of the deviation from ideality in a mix...View the full answer
Introductory Chemical Engineering Thermodynamics
ISBN: 9780136068549
2nd Edition
Authors: J. Elliott, Carl Lira
