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A BENZENE-METHYL ISOO BUTYL KETONE solution containing 60% benzene as mole will be separated at a pressure of 760mmHg in a shelf separation distillation arm, 3/4 of which is saturated liquid, will be given to the nutrition intake arm as a liquid vapor mixture and 97% of the benzene in the diet will be gained, and a top product containing 95% benzene will be obtained as moles. RD=1.30*According to the speed of the RDmin feed flow was 400kmol/ h; a) Lower and upper productflowrates(D,W),? b) Calculate the theoretical number of stages x 0. 0.1. 0.2 0.3. 0.5. 0.8. 0.90 1.0 y 0.0.26. 0.44 0.59. 0.77 0.93.0.96. 1.0

A BENZENE-METHYL ISOO BUTYL KETONE solution containing 60% benzene as mole will be separated at a pressure of 760mmHg in a shelf separation distillation arm, 3/4 of which is saturated liquid, will be given to the nutrition intake arm as a liquid vapor mixture and 97% of the benzene in the diet will be gained, and a top product containing 95% benzene will be obtained as moles. RD=1.30*According to the speed of the RDmin feed flow was 400kmol/ h; a) Lower and upper productflowrates(D,W),? b) Calculate the theoretical number of stages x 0. 0.1. 0.2 0.3. 0.5. 0.8. 0.90 1.0 y 0.0.26. 0.44 0.59. 0.77 0.93.0.96. 1.0

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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A BENZENE-METHYL ISOO BUTYL KETONE solution containing 60% benzene as mole will be separated at a pressure of 760mmHg in a shelf separation distillation arm, 3/4 of which is saturated liquid, will be given to the nutrition intake arm as a liquid vapor mixture and 97% of the benzene in the diet will be gained, and a top product containing 95% benzene will be obtained as moles. RD=1.30* According to the speed of the RDmin feed flow was 400kmol/ h; a) Lower and upper productflowrates(D,W),? b) Calculate the theoretical number of stages x 0. 0.1. 0.2 0.3. 0.5. 0.8. 0.90 1.0 y 0. 0.26. 0.44 0.59. 0.77 0.93, 0.96. 1.0 Mi Notlar ile oluşturuldu
Transcribed Image Text:A BENZENE-METHYL ISOO BUTYL KETONE solution containing 60% benzene as mole will be separated at a pressure of 760mmHg in a shelf separation distillation arm, 3/4 of which is saturated liquid, will be given to the nutrition intake arm as a liquid vapor mixture and 97% of the benzene in the diet will be gained, and a top product containing 95% benzene will be obtained as moles. RD=1.30* According to the speed of the RDmin feed flow was 400kmol/ h; a) Lower and upper productflowrates(D,W),? b) Calculate the theoretical number of stages x 0. 0.1. 0.2 0.3. 0.5. 0.8. 0.90 1.0 y 0. 0.26. 0.44 0.59. 0.77 0.93, 0.96. 1.0 Mi Notlar ile oluşturuldu
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