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Q/ Amixture at a rate 150 kmol/hr of A & B containing 35 mol A % to be separated continuously in a distillation. The bottom product must not contain more than 5 mol A %. The reflux ratio is 1.8 and is a saturated liquid. Obtain the ideal tray. The operating line for rectifying section is: Yn+1 = 0.643 X₁ +0.33 And the vapour-liquid equilibrium data are: X 0 0.1 0.2 0.3 0.4 0.8 1.0 0.9 0.7 0.5 0.6 Y 0 0.22 0.4 0.54 0.66 1.0 0.96 0.92 0.88 0.82 0.75

Q/ Amixture at a rate 150 kmol/hr of A & B containing 35 mol A % to be separated continuously in a distillation. The bottom product must not contain more than 5 mol A %. The reflux ratio is 1.8 and is a saturated liquid. Obtain the ideal tray. The operating line for rectifying section is: Yn+1 = 0.643 X₁ +0.33 And the vapour-liquid equilibrium data are: X 0 0.1 0.2 0.3 0.4 0.8 1.0 0.9 0.7 0.5 0.6 Y 0 0.22 0.4 0.54 0.66 1.0 0.96 0.92 0.88 0.82 0.75

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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es XW Q/ Amixture at a rate 150 kmol/hr of A & B containing 35 mol A % to be separated continuously in a distillation. The bottom product must not contain more than 5 mol A %. The reflux ratio is 1.8 and is a saturated liquid. Obtain the ideal tray. The operating line for rectifying section is: Yn+1 = 0.643 X₂ + 0.33 And the vapour-liquid equilibrium data are: 2.8 X 0 0.1 0.2 0.3 0.4 0.5 1.0 0.7 0.6 0.8 0.9 Y 0 0.22 0.4 0.54 0.96 1.0 0.66 0.92 0.88 0.75 0.82
Transcribed Image Text:es XW Q/ Amixture at a rate 150 kmol/hr of A & B containing 35 mol A % to be separated continuously in a distillation. The bottom product must not contain more than 5 mol A %. The reflux ratio is 1.8 and is a saturated liquid. Obtain the ideal tray. The operating line for rectifying section is: Yn+1 = 0.643 X₂ + 0.33 And the vapour-liquid equilibrium data are: 2.8 X 0 0.1 0.2 0.3 0.4 0.5 1.0 0.7 0.6 0.8 0.9 Y 0 0.22 0.4 0.54 0.96 1.0 0.66 0.92 0.88 0.75 0.82
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