Problem 2. Estimate the bubble point pressure and the vapor phase composition of a liquid mixture at 250 K with the composition given in the table below. For each species, the parameters A, B and C of Antoine's equation are also given in the same table. Assume ideal solution/mixture behavior in both the liquid and vapor phases. Species Mole fraction A в 1 0.50 9.0825 1807.53 -26.15 2 0.50 9.2131 2477.07 -39.94 B Antione' equation: In P sat = A where Psat is in bars and T is in K. T +C
Problem 2. Estimate the bubble point pressure and the vapor phase composition of a liquid mixture at 250 K with the composition given in the table below. For each species, the parameters A, B and C of Antoine's equation are also given in the same table. Assume ideal solution/mixture behavior in both the liquid and vapor phases. Species Mole fraction A в 1 0.50 9.0825 1807.53 -26.15 2 0.50 9.2131 2477.07 -39.94 B Antione' equation: In P sat = A where Psat is in bars and T is in K. T +C
Introduction to Chemical Engineering Thermodynamics
8th Edition
ISBN:9781259696527
Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Publisher:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Chapter1: Introduction
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Transcribed Image Text:Problem 2. Estimate the bubble point pressure and the vapor phase composition of a liquid
mixture at 250 K with the composition given in the table below. For each species, the
parameters A, B and C of Antoine's equation are also given in the same table. Assume ideal
solution/mixture behavior in both the liquid and vapor phases.
Species Mole fraction
A
B
1
0.50
9.0825 1807.53 -26.15
2
0.50
9.2131 2477.07 -39.94
B
Antione' equation: In P sat = A –
where Psat is in bars and T is in K.
T +C
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