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(a) x). y, for the equilibrium phases at 54°C, 65 kPa (b) t and y,, for P = 65 kPa and x, = 0.4. (c) P and y, for t= 54°C and x, 0.4

(a) x). y, for the equilibrium phases at 54°C, 65 kPa (b) t and y,, for P = 65 kPa and x, = 0.4. (c) P and y, for t= 54°C and x, 0.4

Introduction to Chemical Engineering Thermodynamics
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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Q3. For the system of acetone(1)/acetonitrile(2) the vapor pressure of pure species are given by: 2940.46 In Pa / kPa = 14.5463 1/° C+237.22 2945.47 1/° C+224.00 Assuming Raoult's law to describe the vapor/liquid equilibrium states of this system, In P/kPa = 14.2724- determine: (a) x1, y, for the equilibrium phases at 54°c, 65 kPa (b) t and y,, for P= 65 kPa and x, = 0.4. (c) P and y, for t = 54°C and x, = 0.4 (d) P and x, for t= 54°C and y,= 0.4 (e) The fraction of the system that is liquid and vapor at 54°C and 65kPa, when the overall composition of the system is 70 mole percent acetone.
Transcribed Image Text:Q3. For the system of acetone(1)/acetonitrile(2) the vapor pressure of pure species are given by: 2940.46 In Pa / kPa = 14.5463 1/° C+237.22 2945.47 1/° C+224.00 Assuming Raoult's law to describe the vapor/liquid equilibrium states of this system, In P/kPa = 14.2724- determine: (a) x1, y, for the equilibrium phases at 54°c, 65 kPa (b) t and y,, for P= 65 kPa and x, = 0.4. (c) P and y, for t = 54°C and x, = 0.4 (d) P and x, for t= 54°C and y,= 0.4 (e) The fraction of the system that is liquid and vapor at 54°C and 65kPa, when the overall composition of the system is 70 mole percent acetone.
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