Problem 3. Estimate the bubble point pressure and the vapor phase composition of a liquid mixture at 361 K with the composition given in the table below. For each species, the parameters A, B and Cof 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 0.40 9.1325 2766.63 50.55 2 0.20 9.2806 2788.51 52.36 0.25 9.3935 3096.52 53.76 0.15 9.2535 2911.32 56.51 Antoine's equation: In Pot- A where piet is in bars and Tis in K. T+C
Problem 3. Estimate the bubble point pressure and the vapor phase composition of a liquid mixture at 361 K with the composition given in the table below. For each species, the parameters A, B and Cof 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 0.40 9.1325 2766.63 50.55 2 0.20 9.2806 2788.51 52.36 0.25 9.3935 3096.52 53.76 0.15 9.2535 2911.32 56.51 Antoine's equation: In Pot- A where piet is in bars and Tis 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
Section: Chapter Questions
Problem 1.1P
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Transcribed Image Text:Problem 3. Estimate the bubble point pressure and the vapor phase composition of a liquid
mixture at 361 K with the composition given in the table below. For each species, the
parameters A, B and Cof 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 c
1
0.40
9.1325 2766.63 50.55
0.20
9.2806 2788.51 52.36
0.25
9.3935 3096.52 53.76
0.15
9.2535 2911.32 56.51
B
Antoine's equation: In P- A
where pet is in bars and Tis in K.
T+C
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