Tray Tray j+ 1 Tar Snip 20 15 10 Region of unsatisfactory operation 2000 4000 6000 Liquid flow rate, gal/min Column diameter, feet, Dr Single-pass Two-pass Three-pass Four-pass
Tray Tray j+ 1 Tar Snip 20 15 10 Region of unsatisfactory operation 2000 4000 6000 Liquid flow rate, gal/min Column diameter, feet, Dr Single-pass Two-pass Three-pass Four-pass
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
The absorber of Examples is being scaled up by a factor of 15, so a column with an 11.5-ft diameter will be needed. Because of the 30% efficiency for the original tray, a new design has been developed and tested in an Oldershaw column. The resulting Murphree vapor-point efficiency, EOV, for the new tray design for this system is 55%. Estimate EMV and Eo. To estimate the length of the liquid flow path, ZL, use Figure. Assume that u/DE =6 ft-1.
Transcribed Image Text:Tray
Tray
j+ 1
Tar Snip
Transcribed Image Text:20
15
10
Region of
unsatisfactory operation
2000
4000
6000
Liquid flow rate, gal/min
Column diameter, feet, Dr
Single-pass
Two-pass
Three-pass
Four-pass
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