A continuous stirred tank reactor study on chromic acid removal by ion exchange

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DC Field	Value	Language
dc.contributor.author	Tan, HKS	en_US
dc.date.accessioned	2014-12-08T15:01:12Z	-
dc.date.available	2014-12-08T15:01:12Z	-
dc.date.issued	1998	en_US
dc.identifier.issn	0149-6395	en_US
dc.identifier.uri	http://hdl.handle.net/11536/106	-
dc.description.abstract	Dilute chromic acid removal by anion exchange was studied using a continuous stirred tank reactor (CSTR) system. A rate model based on film diffusion control was formulated for quantitative study on the chromate removal. For simplicity, the rate and mass balance equations were formulated for total Cr(VT) concentration. Equations were derived for the effluent concentration history as well as the time-dependent Cr(VI) concentration in the resin. The derived equations for solid and liquid phase Cr(VI) concentration variations were tested and verified by the experimental results obtained. Effects of various operating conditions, such as resin size, feed concentration, and flow rate, were also discussed.	en_US
dc.language.iso	en_US	en_US
dc.title	A continuous stirred tank reactor study on chromic acid removal by ion exchange	en_US
dc.type	Article	en_US
dc.identifier.journal	SEPARATION SCIENCE AND TECHNOLOGY	en_US
dc.citation.volume	33	en_US
dc.citation.issue	8	en_US
dc.citation.spage	1089	en_US
dc.citation.epage	1106	en_US
dc.contributor.department	應用化學系	zh_TW
dc.contributor.department	Department of Applied Chemistry	en_US
dc.identifier.wosnumber	WOS:000074352000002	-
dc.citation.woscount	6	-
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