329 K 90 kmol/hr 0.6 atm 17.4 Water 4.4 MW 23.2 Ethanol 364 K 200 kmol/hr 49.3 Ethyl acetate 1.9 atm 46.15 Water 97,57 Ethanol 11.93 MW 56.26 Ethylacetate RR = 4 Acetic Acid ID-2m CSTR Mixer RR = 5 ID = 2m Feed 343 K Eihyl Alcohol 388 kmol/h 0.55 MW 140 Liters 449.5 K 110 knol/hr 298 K 343 K 6.9 atm 17 atm 28.6 Water 4.63 MW 74.3 Ethanol 469.5 K 188 kmol/hr 6.9 Ethyl acetate 10 atm 24.6 Water 13 MW 27.15 Ethanol 130.7 Acetic acid 5.59 Ethyl acetate Distillation Distillation

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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Propose and show the solution for the entire material balance of the given flow diagram.'

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329 K
90 kmol/hr
0.6 atm
17.4 Water
4.4 MW
23.2 Ethanol
364 K
200 kmol/hr
49.3 Ethyl acetate
1.9 atm
46.15 Water
97.57 Ethanol
11.93 MW
56.26 Ethylacetate
RR = 4
Acetic
Acid
ID = 2m
CSTR
Mixer
RR = 5
ID = 2m
Feed
343 K
Ethyl
Alcohol
388 kmol/h
0.55 MW
140 Liters
449.5 K
110 knol/hr
298 K
343 K
6.9 atm
17 atm
28.6 Water
4.63 MW
74.3 Ethanol
469.5 K
188 kmol/hr
6.9 Ethyl acetate
10 atm
24.6 Water
27.15 Ethanol
13 MW
130.7 Acetic acid
5.59 Ethyl acetate
Distillation Colunn
Distillation
Transcribed Image Text:329 K 90 kmol/hr 0.6 atm 17.4 Water 4.4 MW 23.2 Ethanol 364 K 200 kmol/hr 49.3 Ethyl acetate 1.9 atm 46.15 Water 97.57 Ethanol 11.93 MW 56.26 Ethylacetate RR = 4 Acetic Acid ID = 2m CSTR Mixer RR = 5 ID = 2m Feed 343 K Ethyl Alcohol 388 kmol/h 0.55 MW 140 Liters 449.5 K 110 knol/hr 298 K 343 K 6.9 atm 17 atm 28.6 Water 4.63 MW 74.3 Ethanol 469.5 K 188 kmol/hr 6.9 Ethyl acetate 10 atm 24.6 Water 27.15 Ethanol 13 MW 130.7 Acetic acid 5.59 Ethyl acetate Distillation Colunn Distillation
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