Consider a feed stream consisting of three components and flowing at 1 mol/min as in the following figure. The stream is separated into two streams D and R. D (mol/min) YA (mol A/mol) YB (mol B/mol) Yc (mol C/mol) 1 mo/min STILL XA (mol A/mol) XfB (mol B/mol) Xc (mol C/mol) *A = 0.3 with xg = 0311 *c = 0.389 R (mo/min) XA (mol A/mol) Xg (mol B/mol) Xc (mol C/mol) How many process variables in the figure are unknown? (Do not do any calculations yet) How many balances may be written? Perform a degree of freedom analysis. Suppose it is known that D = 0.568 mol/min, ya = 0.211, and xB= 0.416. What are the values of the remaining process variables? i. R (mol/min) ii. ХА iii. XC iv. Ув V. Ус
Consider a feed stream consisting of three components and flowing at 1 mol/min as in the following figure. The stream is separated into two streams D and R. D (mol/min) YA (mol A/mol) YB (mol B/mol) Yc (mol C/mol) 1 mo/min STILL XA (mol A/mol) XfB (mol B/mol) Xc (mol C/mol) *A = 0.3 with xg = 0311 *c = 0.389 R (mo/min) XA (mol A/mol) Xg (mol B/mol) Xc (mol C/mol) How many process variables in the figure are unknown? (Do not do any calculations yet) How many balances may be written? Perform a degree of freedom analysis. Suppose it is known that D = 0.568 mol/min, ya = 0.211, and xB= 0.416. What are the values of the remaining process variables? i. R (mol/min) ii. ХА iii. XC iv. Ув V. Ус
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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