1. Consider a feed stream consisting of the three components and flowing at 1 mol/min as in the following figure. The stream is separated into two streams D and R. Suppose it is known that xfA= 0.3, xfB= 0.45, xfC+ 0.25, and xC=0.35, yA= 0.35, and yB=0.55. What are the values of the remaining process variables? Do the degree of freedom analysis on the ternary still. 1 mol/min xfA(mol A/min) xfB(mol B/min) xfC(mol C/min) STILL a) Degree of Freedom Analysis Unknowns Balances Constraints b) Find value of unknowns: D(mol/min) yA(mol A/min) yB(mol B/min) yC(mol C/min) R(mol/min) xA(mol A/min) xB(mol B/min) xC(mol C/min)

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
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1. Consider a feed stream consisting of the three components and flowing at 1 mol/min as
in the following figure. The stream is separated into two streams D and R. Suppose it is
known that xfA= 0.3, xfB= 0.45, xfC+ 0.25, and xC=0.35, yA= 0.35, and yB=0.55. What
are the values of the remaining process variables? Do the degree of freedom analysis
on the ternary still.
1 mol/min
xfA(mol A/min)
xfB(mol B/min)
xfC(mol C/min)
STILL
a) Degree of Freedom Analysis
Unknowns
Balances
Constraints
b) Find value of unknowns:
D(mol/min)
yA(mol A/min)
yB(mol B/min)
yC(mol C/min)
R(mol/min)
xA(mol A/min)
xB(mol B/min)
xC(mol C/min)
Transcribed Image Text:1. Consider a feed stream consisting of the three components and flowing at 1 mol/min as in the following figure. The stream is separated into two streams D and R. Suppose it is known that xfA= 0.3, xfB= 0.45, xfC+ 0.25, and xC=0.35, yA= 0.35, and yB=0.55. What are the values of the remaining process variables? Do the degree of freedom analysis on the ternary still. 1 mol/min xfA(mol A/min) xfB(mol B/min) xfC(mol C/min) STILL a) Degree of Freedom Analysis Unknowns Balances Constraints b) Find value of unknowns: D(mol/min) yA(mol A/min) yB(mol B/min) yC(mol C/min) R(mol/min) xA(mol A/min) xB(mol B/min) xC(mol C/min)
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