Please use this identifier to cite or link to this item: https://scholarbank.nus.edu.sg/handle/10635/67494
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dc.titleModified continuous countercurrent flow model for a PSA separation process
dc.contributor.authorFarooq, S.
dc.contributor.authorRathor, M.N.
dc.contributor.authorHidajat, K.
dc.date.accessioned2014-06-17T10:01:54Z
dc.date.available2014-06-17T10:01:54Z
dc.date.issued1994-01
dc.identifier.citationFarooq, S.,Rathor, M.N.,Hidajat, K. (1994-01). Modified continuous countercurrent flow model for a PSA separation process. Chemical Engineering Research and Design 72 (A1) : 114-118. ScholarBank@NUS Repository.
dc.identifier.issn02638762
dc.identifier.urihttp://scholarbank.nus.edu.sg/handle/10635/67494
dc.description.abstractThe continuous countercurrent flow (CCF) model for pressure swing adsorption (PSA) systems has so far been validated for Skarstrom cycle in which the pressurization and blowdown steps and adsorption and purge steps have equal durations. The mass balance was written in such a way that the total volumes of feed and purge were kept constant between the actual operation and the steady state CCF representation. By relaxing this restriction on the mass balance, it is shown that the usefulness of the CCF model may be extended to cycles in which the durations of the individual steps are different.
dc.sourceScopus
dc.typeArticle
dc.contributor.departmentCHEMICAL ENGINEERING
dc.description.sourcetitleChemical Engineering Research and Design
dc.description.volume72
dc.description.issueA1
dc.description.page114-118
dc.description.codenCERDE
dc.identifier.isiutNOT_IN_WOS
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