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.ર્દ 0.03 kg B/kg 0.97 kg C/kg 5,300 kg/hr (1-x₂) kg A/kg X2 kg B/kg M3 1.0 kg A/kg 1,200 kg/hr 0.70 kg A/kg (0.3-x4) kg B/kg X4 kg C/kg m5

.ર્દ 0.03 kg B/kg 0.97 kg C/kg 5,300 kg/hr (1-x₂) kg A/kg X2 kg B/kg M3 1.0 kg A/kg 1,200 kg/hr 0.70 kg A/kg (0.3-x4) kg B/kg X4 kg C/kg m5

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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Question

(m3 is half the flowrate of m1), (90% of C in m1 exits in m5)                                                                 

Determine the value of m1.

Answer: 

A. 1218 kg/hr
B. 2437 kg/hr
c. 3256 kg/hr
D. 5318 kg/hr
m₁ 0.03 kg B/kg 0.97 kg C/kg 5,300 kg/hr (1-x₂) kg A/kg X₂ kg B/kg m3 1.0 kg A/kg 1,200 kg/hr 0.70 kg A/kg (0.3-x4) kg B/kg X4 kg C/kg m5 0.60 kg B/kg 0.40 kg C/kg
Transcribed Image Text:m₁ 0.03 kg B/kg 0.97 kg C/kg 5,300 kg/hr (1-x₂) kg A/kg X₂ kg B/kg m3 1.0 kg A/kg 1,200 kg/hr 0.70 kg A/kg (0.3-x4) kg B/kg X4 kg C/kg m5 0.60 kg B/kg 0.40 kg C/kg
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