546.2 Ibmol/h y, mol% 6.192 cfs C2 Сз nC4 60.2573 nc5 32.5874 0.0006 0.4817 ReCt пСs 6.6730 Bottom tray 230.5° F 1 150 psia x, mol% C2 0.0001 C3 nC4 39.1389 nC5 43.0599 nCg 17.6563 0.1448 621.3 Ibmo/h 171.1 gpm
546.2 Ibmol/h y, mol% 6.192 cfs C2 Сз nC4 60.2573 nc5 32.5874 0.0006 0.4817 ReCt пСs 6.6730 Bottom tray 230.5° F 1 150 psia x, mol% C2 0.0001 C3 nC4 39.1389 nC5 43.0599 nCg 17.6563 0.1448 621.3 Ibmo/h 171.1 gpm
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
Conditions at the bottom tray of a reboiled stripper are in Figure. If valve trays are used with 24-inch tray spacing, estimate column diameter for 80% of flooding.
Transcribed Image Text:546.2 Ibmol/h
y, mol%
6.192 cfs
C2
Сз
nC4 60.2573
nc5 32.5874
0.0006
0.4817
ReCt
пСs
6.6730
Bottom tray
230.5° F
1 150 psia
x, mol%
C2
0.0001
C3
nC4 39.1389
nC5 43.0599
nCg 17.6563
0.1448
621.3 Ibmo/h
171.1 gpm
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