Please use this identifier to cite or link to this item: https://doi.org/10.1016/j.bej.2007.01.026
DC FieldValue
dc.titleModified reactive SMB for production of high concentrated fructose syrup by isomerization of glucose to fructose
dc.contributor.authorZhang, Y.
dc.contributor.authorHidajat, K.
dc.contributor.authorRay, A.K.
dc.date.accessioned2014-10-09T06:54:03Z
dc.date.available2014-10-09T06:54:03Z
dc.date.issued2007-08-01
dc.identifier.citationZhang, Y., Hidajat, K., Ray, A.K. (2007-08-01). Modified reactive SMB for production of high concentrated fructose syrup by isomerization of glucose to fructose. Biochemical Engineering Journal 35 (3) : 341-351. ScholarBank@NUS Repository. https://doi.org/10.1016/j.bej.2007.01.026
dc.identifier.issn1369703X
dc.identifier.urihttp://scholarbank.nus.edu.sg/handle/10635/89462
dc.description.abstractThis work presents modifications to the Hashimoto's hybrid simulated moving bed reactor (SMBR) system which was used to produce 55% high fructose syrup (HFS55). The purpose of this study is to develop a new SMBR system to overcome the disadvantages of Hashimoto system (3-zone SMB with seven reactors), i.e., low utility of reactors when feed being a 50/50 blend of glucose and fructose. Two different configurations of modified system were presented in this paper: the first configuration is 4-zone SMB with one reactor, while the other one consists of one additional reactor. Both of these configurations aim at improving the concentration and purity of glucose at the inlet of the reactor, which will lead to both high productivity and high purity of fructose in the product. A state-of-the-art optimization technique, viz., non-dominated sorting genetic algorithm (NSGA) is used in finding the optimal design and operating parameters for the modified reactive SMB and Varicol processes. Compared with the Hashimoto's system, high productivity and purity of fructose can be achieved in these new systems using less number of reactors. © 2007 Elsevier B.V. All rights reserved.
dc.description.urihttp://libproxy1.nus.edu.sg/login?url=http://dx.doi.org/10.1016/j.bej.2007.01.026
dc.sourceScopus
dc.subjectBioprocess design
dc.subjectFructose
dc.subjectMoving bed bioreactor
dc.subjectOptimization
dc.subjectPareto
dc.subjectVaricol
dc.typeArticle
dc.contributor.departmentCHEMICAL & BIOMOLECULAR ENGINEERING
dc.description.doi10.1016/j.bej.2007.01.026
dc.description.sourcetitleBiochemical Engineering Journal
dc.description.volume35
dc.description.issue3
dc.description.page341-351
dc.description.codenBEJOF
dc.identifier.isiut000247896100012
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