Modelling of a simulated counter-current adsorption process

Please use this identifier to cite or link to this item: https://scholarbank.nus.edu.sg/handle/10635/67490

DC Field	Value
dc.title	Modelling of a simulated counter-current adsorption process
dc.contributor.author	Ching, C.B.
dc.contributor.author	Hidajat, K.
dc.contributor.author	Ho, C.
dc.contributor.author	Ruthven, D.M.
dc.date.accessioned	2014-06-17T10:01:52Z
dc.date.available	2014-06-17T10:01:52Z
dc.date.issued	1987-06
dc.identifier.citation	Ching, C.B.,Hidajat, K.,Ho, C.,Ruthven, D.M. (1987-06). Modelling of a simulated counter-current adsorption process. Reactive Polymers, Ion Exchangers, Sorbents 6 (1) : 15-20. ScholarBank@NUS Repository.
dc.identifier.issn	01676989
dc.identifier.uri	http://scholarbank.nus.edu.sg/handle/10635/67490
dc.description.abstract	The operation of a simulated counter-current adsorption system for glucose-fructose separation has been studied experimentally and simulated numerically by treating each column as equivalent to ten ideal theoretical stages. Predicted concentration profiles show good agreement with the measured profiles under both transient and cyclic steady-state conditions. Introduction of flow distributors had only a minor effect on the profile, suggesting that poor flow distribution does not contribute significantly to dispersion within the system. © 1987.
dc.source	Scopus
dc.type	Article
dc.contributor.department	CHEMICAL ENGINEERING
dc.description.sourcetitle	Reactive Polymers, Ion Exchangers, Sorbents
dc.description.volume	6
dc.description.issue	1
dc.description.page	15-20
dc.identifier.isiut	NOT_IN_WOS
Appears in Collections:	Staff Publications

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