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For a feed rate of 100 mol/min, calculate all quantities in the partially filled flowchart for the system at steady-state. V = D mol/min YB = E mol Bz/mol F= A mol/min XB = B mol Bz/mol XTC mol Tol/mol SEPARATION PROCESS y+ G mol Tol/mol L= H mol/min XB =/mol Bz/mol x+= Jmol Tol/mol Feed Vapor Liquid A = i D= i H= i B= i E=i 1 = C=i G= J = A stream consisting of 36.0 mole% benzene (B) and 64.0% toluene (T) is fed at a constant rate to a process unit that produces two product streams, one a vapor and the other a liquid. The vapor flow rate is initially zero and asymptotically approaches two thirds of the molar flow rate of the feed stream. Throughout this entire period, no material accumulates in the unit. When the vapor flow rate has become constant, the liquid is analyzed and found to be 25.7 mole% benzene.

For a feed rate of 100 mol/min, calculate all quantities in the partially filled flowchart for the system at steady-state. V = D mol/min YB = E mol Bz/mol F= A mol/min XB = B mol Bz/mol XTC mol Tol/mol SEPARATION PROCESS y+ G mol Tol/mol L= H mol/min XB =/mol Bz/mol x+= Jmol Tol/mol Feed Vapor Liquid A = i D= i H= i B= i E=i 1 = C=i G= J = A stream consisting of 36.0 mole% benzene (B) and 64.0% toluene (T) is fed at a constant rate to a process unit that produces two product streams, one a vapor and the other a liquid. The vapor flow rate is initially zero and asymptotically approaches two thirds of the molar flow rate of the feed stream. Throughout this entire period, no material accumulates in the unit. When the vapor flow rate has become constant, the liquid is analyzed and found to be 25.7 mole% benzene.

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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For a feed rate of 100 mol/min, calculate all quantities in the partially filled flowchart for the system at steady-state. V = D mol/min YB = E mol Bz/mol F= A mol/min XB = B mol Bz/mol XTC mol Tol/mol SEPARATION PROCESS y+ G mol Tol/mol L= H mol/min XB =/mol Bz/mol x+= Jmol Tol/mol Feed Vapor Liquid A = i D= i H= i B= i E=i 1 = C=i G= J =
Transcribed Image Text:For a feed rate of 100 mol/min, calculate all quantities in the partially filled flowchart for the system at steady-state. V = D mol/min YB = E mol Bz/mol F= A mol/min XB = B mol Bz/mol XTC mol Tol/mol SEPARATION PROCESS y+ G mol Tol/mol L= H mol/min XB =/mol Bz/mol x+= Jmol Tol/mol Feed Vapor Liquid A = i D= i H= i B= i E=i 1 = C=i G= J =
A stream consisting of 36.0 mole% benzene (B) and 64.0% toluene (T) is fed at a constant rate to a process unit that produces two product streams, one a vapor and the other a liquid. The vapor flow rate is initially zero and asymptotically approaches two thirds of the molar flow rate of the feed stream. Throughout this entire period, no material accumulates in the unit. When the vapor flow rate has become constant, the liquid is analyzed and found to be 25.7 mole% benzene.
Transcribed Image Text:A stream consisting of 36.0 mole% benzene (B) and 64.0% toluene (T) is fed at a constant rate to a process unit that produces two product streams, one a vapor and the other a liquid. The vapor flow rate is initially zero and asymptotically approaches two thirds of the molar flow rate of the feed stream. Throughout this entire period, no material accumulates in the unit. When the vapor flow rate has become constant, the liquid is analyzed and found to be 25.7 mole% benzene.
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