Modeling and parametric analysis of hollow fiber membrane system for carbon capture from multicomponent flue gas

Handle URI:
http://hdl.handle.net/10754/575550
Title:
Modeling and parametric analysis of hollow fiber membrane system for carbon capture from multicomponent flue gas
Authors:
Khalilpour, Rajab; Abbas, Ali; Lai, Zhiping ( 0000-0001-9555-6009 ) ; Pinnau, Ingo ( 0000-0003-3040-9088 )
Abstract:
The modeling and optimal design/operation of gas membranes for postcombustion carbon capture (PCC) is presented. A systematic methodology is presented for analysis of membrane systems considering multicomponent flue gas with CO 2 as target component. Simplifying assumptions is avoided by namely multicomponent flue gas represented by CO 2/N 2 binary mixture or considering the co/countercurrent flow pattern of hollow-fiber membrane system as mixed flow. Optimal regions of flue gas pressures and membrane area were found within which a technoeconomical process system design could be carried out. High selectivity was found to not necessarily have notable impact on PCC membrane performance, rather, a medium selectivity combined with medium or high permeance could be more advantageous. © 2011 American Institute of Chemical Engineers (AIChE).
KAUST Department:
Advanced Membranes and Porous Materials Research Center; Physical Sciences and Engineering (PSE) Division; Chemical and Biological Engineering Program
Publisher:
Wiley-Blackwell
Journal:
AIChE Journal
Issue Date:
12-Aug-2011
DOI:
10.1002/aic.12699
Type:
Article
ISSN:
00011541
Sponsors:
The authors gratefully acknowledge Delta Electricity's sponsorship of this project.
Appears in Collections:
Articles; Advanced Membranes and Porous Materials Research Center; Physical Sciences and Engineering (PSE) Division; Chemical and Biological Engineering Program

Full metadata record

DC FieldValue Language
dc.contributor.authorKhalilpour, Rajaben
dc.contributor.authorAbbas, Alien
dc.contributor.authorLai, Zhipingen
dc.contributor.authorPinnau, Ingoen
dc.date.accessioned2015-08-24T08:32:37Zen
dc.date.available2015-08-24T08:32:37Zen
dc.date.issued2011-08-12en
dc.identifier.issn00011541en
dc.identifier.doi10.1002/aic.12699en
dc.identifier.urihttp://hdl.handle.net/10754/575550en
dc.description.abstractThe modeling and optimal design/operation of gas membranes for postcombustion carbon capture (PCC) is presented. A systematic methodology is presented for analysis of membrane systems considering multicomponent flue gas with CO 2 as target component. Simplifying assumptions is avoided by namely multicomponent flue gas represented by CO 2/N 2 binary mixture or considering the co/countercurrent flow pattern of hollow-fiber membrane system as mixed flow. Optimal regions of flue gas pressures and membrane area were found within which a technoeconomical process system design could be carried out. High selectivity was found to not necessarily have notable impact on PCC membrane performance, rather, a medium selectivity combined with medium or high permeance could be more advantageous. © 2011 American Institute of Chemical Engineers (AIChE).en
dc.description.sponsorshipThe authors gratefully acknowledge Delta Electricity's sponsorship of this project.en
dc.publisherWiley-Blackwellen
dc.subjectCarbon captureen
dc.subjectMembraneen
dc.subjectModelingen
dc.subjectMulticomponent gasen
dc.subjectParametric analysisen
dc.titleModeling and parametric analysis of hollow fiber membrane system for carbon capture from multicomponent flue gasen
dc.typeArticleen
dc.contributor.departmentAdvanced Membranes and Porous Materials Research Centeren
dc.contributor.departmentPhysical Sciences and Engineering (PSE) Divisionen
dc.contributor.departmentChemical and Biological Engineering Programen
dc.identifier.journalAIChE Journalen
dc.contributor.institutionSchool of Chemical and Biomolecular Engineering, The University of Sydney, Sydney, Australiaen
kaust.authorLai, Zhipingen
kaust.authorPinnau, Ingoen
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