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The composition of vapor entering a tray in a distillation column is 0.57. T composition of the vapor leaving the tray is 0.65. The equilibrium composition corresponding to the liquid leaving this tray is 0.60. All the compositions are e mole fraction of the more volatile component. Calculate the Murphree efficien the vapor phase is -----% a)150 b)280 c)120 d)266

The composition of vapor entering a tray in a distillation column is 0.57. T composition of the vapor leaving the tray is 0.65. The equilibrium composition corresponding to the liquid leaving this tray is 0.60. All the compositions are e mole fraction of the more volatile component. Calculate the Murphree efficien the vapor phase is -----% a)150 b)280 c)120 d)266

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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The composition of vapor entering a tray in a distillation column is 0.57. The average composition of the vapor leaving the tray is 0.65. The equilibrium composition of the vapor corresponding to the liquid leaving this tray is 0.60. All the compositions are expressed in mole fraction of the more volatile component. Calculate the Murphree efficiency based on the vapor phase is -----% a)150 b)280 c)120 d)266
Transcribed Image Text:The composition of vapor entering a tray in a distillation column is 0.57. The average composition of the vapor leaving the tray is 0.65. The equilibrium composition of the vapor corresponding to the liquid leaving this tray is 0.60. All the compositions are expressed in mole fraction of the more volatile component. Calculate the Murphree efficiency based on the vapor phase is -----% a)150 b)280 c)120 d)266
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