Gas Liquid Out Feed Gas Absorbent Out Flow rate, Ibmol/h: Air 687 687 Acetone 15 0.1 14.9 Water 1,733 22 1,711 Temperature, °F Pressure, psia 78 90 80 15 15 14 15 Phase Vapor Liquid Vapor Liquid Concern has been expressed about a possible feed-gas explosion hazard. The lower and upper flammability limits for acetone in air are 2.5 and 13 mol%, respectively. Is the mixture within the explo- sive range? If so, what can be done to remedy the situation?
Gas Liquid Out Feed Gas Absorbent Out Flow rate, Ibmol/h: Air 687 687 Acetone 15 0.1 14.9 Water 1,733 22 1,711 Temperature, °F Pressure, psia 78 90 80 15 15 14 15 Phase Vapor Liquid Vapor Liquid Concern has been expressed about a possible feed-gas explosion hazard. The lower and upper flammability limits for acetone in air are 2.5 and 13 mol%, respectively. Is the mixture within the explo- sive range? If so, what can be done to remedy the situation?
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
Related questions
Question
Transcribed Image Text:Acetone can be recovered from air by absorption in water. The
conditions for the streams entering and leaving are listed below. If
the absorber operates adiabatically, obtain the temperature of the
exiting liquid phase using a simulation program.
Transcribed Image Text:Gas
Liquid
Out
Feed
Gas
Absorbent
Out
Flow rate, Ibmol/h:
Air
687
687
Acetone
15
0.1
14.9
Water
1,733
22
1,711
78
Temperature, °F
Pressure, psia
90
80
15
15
14
15
Phase
Vapor
Liquid
Vapor
Liquid
Concern has been expressed about a possible feed-gas explosion
hazard. The lower and upper flammability limits for acetone in air
are 2.5 and 13 mol%, respectively. Is the mixture within the explo-
sive range? If so, what can be done to remedy the situation?
SC
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