10 80 psla 1.0 к, 0.1 0.01 0.1 10 Kcs ПT 1. ПL Distillate Component Ibmol/h iC4 пC4 iC5 пCs (12) 442 13 Feed Debutanizer Component Ibmol/h iC4 nCa (LK) ic5 (HK) (1) (468) 12 448 36 15 23 39.1 272.2 31.0 Св 876.3 Bottoms Component Ibmol/h 6 23 nC4 iC5 nC5 C6 (14) (23) (39.1) (272.2) (31.0) (408.3) Cg C9
10 80 psla 1.0 к, 0.1 0.01 0.1 10 Kcs ПT 1. ПL Distillate Component Ibmol/h iC4 пC4 iC5 пCs (12) 442 13 Feed Debutanizer Component Ibmol/h iC4 nCa (LK) ic5 (HK) (1) (468) 12 448 36 15 23 39.1 272.2 31.0 Св 876.3 Bottoms Component Ibmol/h 6 23 nC4 iC5 nC5 C6 (14) (23) (39.1) (272.2) (31.0) (408.3) Cg C9
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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Question
For the debutanizer shown in Figure and considered estimate the Nmin by the Fenske equation. Assume a uniform operating pressure of 80 psia (552 kPa) throughout and utilize the ideal K-values given by Bachelor [4] as plotted in Figure.
Transcribed Image Text:10
80
psla
1.0
к,
0.1
0.01
0.1
10
Kcs
ПT
1.
ПL
Transcribed Image Text:Distillate
Component Ibmol/h
iC4
пC4
iC5
пCs
(12)
442
13
Feed
Debutanizer
Component Ibmol/h
iC4
nCa (LK)
ic5 (HK)
(1)
(468)
12
448
36
15
23
39.1
272.2
31.0
Св
876.3
Bottoms
Component
Ibmol/h
6
23
nC4
iC5
nC5
C6
(14)
(23)
(39.1)
(272.2)
(31.0)
(408.3)
Cg
C9
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