5.1 The following table gives the mole fraction of methylbenzene (A) in liquid and gaseous mixtures with butanone at equilibrium at 303.15 K and the total pressure p. Take the vapour to be perfect and calculate the partial pressures of the two components. Plot them against their respective mole fractions in the liquid mixture and find the Henry's law constants for the two components. XA 0.0898 0.2476 0.3577 0.5194 0.6036 YA 0.0410 0.1154 0.1762 0.2772 0.3393 p/kPa 36.066 34.121 30.900 28.626 25.239 23.402 XA 0.7188 0.8019 0.9105 1 YA 0.4450 0.5435 0.7284 1 p/kPa 20.6984 18.592 15.496 12.295
5.1 The following table gives the mole fraction of methylbenzene (A) in liquid and gaseous mixtures with butanone at equilibrium at 303.15 K and the total pressure p. Take the vapour to be perfect and calculate the partial pressures of the two components. Plot them against their respective mole fractions in the liquid mixture and find the Henry's law constants for the two components. XA 0.0898 0.2476 0.3577 0.5194 0.6036 YA 0.0410 0.1154 0.1762 0.2772 0.3393 p/kPa 36.066 34.121 30.900 28.626 25.239 23.402 XA 0.7188 0.8019 0.9105 1 YA 0.4450 0.5435 0.7284 1 p/kPa 20.6984 18.592 15.496 12.295
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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