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Please use this identifier to cite or link to this item: https://scholarbank.nus.edu.sg/handle/10635/91513
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dc.titleIMPROVED ADSORPTION PROCESS FOR THE PRODUCTION OF HIGH-FRUCTOSE SYRUP.
dc.contributor.authorChing, C.B.
dc.contributor.authorHo, C.
dc.contributor.authorRuthven, D.M.
dc.date.accessioned2014-10-09T08:18:57Z
dc.date.available2014-10-09T08:18:57Z
dc.date.issued1986-11
dc.identifier.citationChing, C.B.,Ho, C.,Ruthven, D.M. (1986-11). IMPROVED ADSORPTION PROCESS FOR THE PRODUCTION OF HIGH-FRUCTOSE SYRUP.. AIChE Journal 32 (11) : 1876-1880. ScholarBank@NUS Repository.
dc.identifier.issn00011541
dc.identifier.urihttp://scholarbank.nus.edu.sg/handle/10635/91513
dc.description.abstractBy applying a temperature profile to the system, the concentration of the extract product in a countercurrent adsorption separation process may be increased relative to the maximum concentration attainable under isothermal conditions. To achieve the required temperature profile in a simulated countercurrent system it is necessary to heat and cool the columns in sequence as the feed and product draw-off points are switched through the bed. The practical feasibility of operating the system in this way has been demonstrated experimentally for the separation of glucose-fructose mixtures.
dc.sourceScopus
dc.typeArticle
dc.contributor.departmentCHEMICAL ENGINEERING
dc.description.sourcetitleAIChE Journal
dc.description.volume32
dc.description.issue11
dc.description.page1876-1880
dc.description.codenAICEA
dc.identifier.isiutNOT_IN_WOS
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