For the process shown below a) Carry out a full DFA around each equipment and the overall system. b) Calculate the values of m2, m3, ma, ms, m6 m3 Air 0.995 Water 0.005 Acctone 0,99 Water 0.01 Water (100%) m2 P-1 P-2 100 kg/h Acetone 0.19 Bottom Air 0.95 Acctone 0.03 Water Water 0.81 Acetone 0.04 > Water 0,96 0.02 my

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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5
For the process shown below
a) Carry out a full DFA arouhd each equipment and the overall system.
b) Calculate the values of m2, m3, m4, ms, m6
m3
Air
0.995
Water 0.005
Acetone 0,99
Water
0.01
Water (100%) m2
P-1
P-2
m4
100 kg/h
Acetone 0.19
Bottom
Air
0.95
Acetone 0,03
Water
0.81
Acetone 0,04
m6
> Water
0.96
Water
0.02
Transcribed Image Text:For the process shown below a) Carry out a full DFA arouhd each equipment and the overall system. b) Calculate the values of m2, m3, m4, ms, m6 m3 Air 0.995 Water 0.005 Acetone 0,99 Water 0.01 Water (100%) m2 P-1 P-2 m4 100 kg/h Acetone 0.19 Bottom Air 0.95 Acetone 0,03 Water 0.81 Acetone 0,04 m6 > Water 0.96 Water 0.02
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