A liquid mixture at boiling point is fed to a distillation column. As a result of the distillation process, 50 kg/h distillate and 50 kg/h bottom product are obtained. In the enrichment section, the liquid flow rate is 200 kg/h and the vapor flow rate is 250 kg/h. What is the slope of the stripping-section operating line?

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
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5
F3
A liquid mixture at boiling point is fed to a distillation column. As a result of the distillation process, 50
kg/h distillate and 50 kg/h bottom product are obtained. In the enrichment section, the liquid flow rate
is 200 kg/h and the vapor flow rate is 250 kg/h. What is the slope of the stripping-section operating line?
3 r
$E4
A
B
C
D
F4
1.20
0.12
0.83
$
4 {
1.00
F5
R$
50
F6
FH
Q Search
F7
61
TY Y !
FB
Or
&
7 Y
F9
*
L
DELL
a
F10
(
8 A 99
F11
)
O
F12
OF
P:
O
PrtScr
K
Transcribed Image Text:5 F3 A liquid mixture at boiling point is fed to a distillation column. As a result of the distillation process, 50 kg/h distillate and 50 kg/h bottom product are obtained. In the enrichment section, the liquid flow rate is 200 kg/h and the vapor flow rate is 250 kg/h. What is the slope of the stripping-section operating line? 3 r $E4 A B C D F4 1.20 0.12 0.83 $ 4 { 1.00 F5 R$ 50 F6 FH Q Search F7 61 TY Y ! FB Or & 7 Y F9 * L DELL a F10 ( 8 A 99 F11 ) O F12 OF P: O PrtScr K
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