Modeling and parametric analysis of hollow fiber membrane system for carbon capture from multicomponent flue gas
KAUST DepartmentAdvanced Membranes and Porous Materials Research Center
Biological and Environmental Sciences and Engineering (BESE) Division
Chemical Engineering Program
Physical Science and Engineering (PSE) Division
Online Publication Date2011-08-12
Print Publication Date2012-05
Permanent link to this recordhttp://hdl.handle.net/10754/575550
MetadataShow full item record
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).
SponsorsThe authors gratefully acknowledge Delta Electricity's sponsorship of this project.