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. The process shown underneath removes benzene from air by adsorption onto the surfaces of porous solids called zeolites. The adsorption unit shown below has a countercurrent flow of zeolites, and 1.00 kg zeolite can adsorb 0.10 kg benzene. Stream 6 purges 2% of the zeolite in stream 5. 47.2 k g/min 86.0 wt % air 99.7 wt % air 14.0 w t% benzene 0.3 wt % benzene (2 adsorber zeolite 80 zeolite saturated (3 with benzene zeolite heater benzene Calculate the flow rates of streams 4 and 8.

. The process shown underneath removes benzene from air by adsorption onto the surfaces of porous solids called zeolites. The adsorption unit shown below has a countercurrent flow of zeolites, and 1.00 kg zeolite can adsorb 0.10 kg benzene. Stream 6 purges 2% of the zeolite in stream 5. 47.2 k g/min 86.0 wt % air 99.7 wt % air 14.0 w t% benzene 0.3 wt % benzene (2 adsorber zeolite 80 zeolite saturated (3 with benzene zeolite heater benzene Calculate the flow rates of streams 4 and 8.

Introduction to Chemical Engineering Thermodynamics
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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1. The process shown underneath removes benzene from air by adsorption onto the surfaces of porous solids called zeolites. The adsorption unit shown below has a countercurrent flow of zeolites, and 1.00 kg zeolite can adsorb 0.10 kg benzene. Stream 6 purges 2% of the zeolite in stream 5. 47.2 kg/min 86.0 wt % air 99.7 wt % air 0.3 wt % benzene 14.0 w t% benzene (1) adsorber zeolite 8. zeolite saturated (3 with benzene zeolite heater (5 benzene Calculate the flow rates of streams 4 and 8.
Transcribed Image Text:1. The process shown underneath removes benzene from air by adsorption onto the surfaces of porous solids called zeolites. The adsorption unit shown below has a countercurrent flow of zeolites, and 1.00 kg zeolite can adsorb 0.10 kg benzene. Stream 6 purges 2% of the zeolite in stream 5. 47.2 kg/min 86.0 wt % air 99.7 wt % air 0.3 wt % benzene 14.0 w t% benzene (1) adsorber zeolite 8. zeolite saturated (3 with benzene zeolite heater (5 benzene Calculate the flow rates of streams 4 and 8.
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