A 200 mol / h liquid mixture containing %35 mol A and %65 mol B into a distillation column It is fed at 101.3 kPa pressure and 25ºC. The feed is 50% vapor phase. Distillation the resulting distillate contains %95 mol A and the bottom product contains %5 mol A is requested. In this case; a) Distillate and bottom product flow rates, b) Minimum reflux rate, c) Minimum number of shelves, d) The actual reflux rate is 1.5 times the minimum reflux rate. Find the theoretical number of racks and from which rack the feeding is made.

Introduction to Chemical Engineering Thermodynamics
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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
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A 200 mol / h liquid mixture containing %35 mol A and %65 mol B into a distillation column It is fed at 101.3 kPa pressure and 25ºC. The feed is 50% vapor phase. Distillation the resulting distillate contains %95 mol A and the bottom product contains %5 mol A is requested. In this case;

a) Distillate and bottom product flow rates,

b) Minimum reflux rate,

c) Minimum number of shelves,

d) The actual reflux rate is 1.5 times the minimum reflux rate. Find the theoretical number of racks and from which rack the feeding is made.

 

0.10
0.20
0.30
0.40
0.50
0.60
0.80
1
y
0.30
0.58
0.71
0.79
0.84
0.88
0.95
Transcribed Image Text:0.10 0.20 0.30 0.40 0.50 0.60 0.80 1 y 0.30 0.58 0.71 0.79 0.84 0.88 0.95
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