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The vapour press Т, К 353.1 358 363 368 373 378 383 383.6 P, kPa P, kPa 101.3 116.9 135.4 155.7 179.1 204.2 233.0 240.0 39.6 46.0 54.0 63.3 74.2 86.0 99.0 101.3 Calculate the equilibrium data for the system at 101.3 kPa and formulate an equation for the equilibrium diagram in terms of average relative volatility. 3.5 At 303 K, the vapour pressures of benzene (A) and toluene (B) are 15.75 kPa and 4.89 kPa respectively. Determine the partial pressures and weight composition of the vapour i equilibrium with a liquid mixture consisting of equal weights of the two componems. orrongement

The vapour press Т, К 353.1 358 363 368 373 378 383 383.6 P, kPa P, kPa 101.3 116.9 135.4 155.7 179.1 204.2 233.0 240.0 39.6 46.0 54.0 63.3 74.2 86.0 99.0 101.3 Calculate the equilibrium data for the system at 101.3 kPa and formulate an equation for the equilibrium diagram in terms of average relative volatility. 3.5 At 303 K, the vapour pressures of benzene (A) and toluene (B) are 15.75 kPa and 4.89 kPa respectively. Determine the partial pressures and weight composition of the vapour i equilibrium with a liquid mixture consisting of equal weights of the two componems. orrongement

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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K.V.Narayanan book of thermodynamics

Chapter 8 Unsolved problem 8.4

vapour phase alone? At the given T, the vapour pressures of benzene and toluene are 8.6 An equimolar mixture of benzene and toluene is contained in a piston/cylinder arrangement 414 A Textbook of Chemical Engineering Thermodynamics ideal solution. At these conditions, Henry's law constant for methane in oil = 200 La fugacity coefficient of pure methane gas = 0.90 and mole fraction of methane in the %3D gas phase, yi = 0.95. 8,4 The vapour pressures of benzene and toluene are given below. Т, К 353.1 358 363 368 373 378 383 383.6 P, kPa 101.3 116.9 135.4 155.7 179.1 204.2 233.0 240.0 P, kPa 39.6 46.0 54.0 63.3 74.2 86.0 99.0 101.3 Calculate the equilibrium data for the system at 101.3 kPa and formulate an equation for the equilibrium diagram in terms of average relative volatility. 8.5 At 303 K, the vapour pressures of benzene (A) and toluene (B) are 15.75 kPa and 4.89 kPa respectively. Determine the partial pressures and weight composition of the vapour m in equilibrium with a liquid mixture consisting of equal weights of the two components. 8.6 An equimolar mixture of benzene and toluene is contained in a piston/cylinder arrangeme at a temperature T. What is the maximum pressure below which the mixture exists a u vapour phase alone? At the given T, the vapour pressures of benzene and toluene 203.9 kPa and 85.3 kPa, respectively. Assume that Raoult's law is valid.
Transcribed Image Text:vapour phase alone? At the given T, the vapour pressures of benzene and toluene are 8.6 An equimolar mixture of benzene and toluene is contained in a piston/cylinder arrangement 414 A Textbook of Chemical Engineering Thermodynamics ideal solution. At these conditions, Henry's law constant for methane in oil = 200 La fugacity coefficient of pure methane gas = 0.90 and mole fraction of methane in the %3D gas phase, yi = 0.95. 8,4 The vapour pressures of benzene and toluene are given below. Т, К 353.1 358 363 368 373 378 383 383.6 P, kPa 101.3 116.9 135.4 155.7 179.1 204.2 233.0 240.0 P, kPa 39.6 46.0 54.0 63.3 74.2 86.0 99.0 101.3 Calculate the equilibrium data for the system at 101.3 kPa and formulate an equation for the equilibrium diagram in terms of average relative volatility. 8.5 At 303 K, the vapour pressures of benzene (A) and toluene (B) are 15.75 kPa and 4.89 kPa respectively. Determine the partial pressures and weight composition of the vapour m in equilibrium with a liquid mixture consisting of equal weights of the two components. 8.6 An equimolar mixture of benzene and toluene is contained in a piston/cylinder arrangeme at a temperature T. What is the maximum pressure below which the mixture exists a u vapour phase alone? At the given T, the vapour pressures of benzene and toluene 203.9 kPa and 85.3 kPa, respectively. Assume that Raoult's law is valid.
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