.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
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
Related questions
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](/v2/_next/image?url=https%3A%2F%2Fcontent.bartleby.com%2Fqna-images%2Fquestion%2F17fd2fce-4672-4611-b0ca-b59276015485%2Ff91bd8e1-a0b8-4cb1-af1e-1267fcdaa951%2F9zr72u_processed.png&w=3840&q=75)
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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