Please use this identifier to cite or link to this item: http://scholarbank.nus.edu.sg/handle/10635/67550
Title: Simulated Moving-Bed Reactor: Application in Bioreaction and Separation
Authors: Ching, C.B. 
Lu, Z.P. 
Issue Date: Jan-1997
Source: Ching, C.B.,Lu, Z.P. (1997-01). Simulated Moving-Bed Reactor: Application in Bioreaction and Separation. Industrial and Engineering Chemistry Research 36 (1) : 152-159. ScholarBank@NUS Repository.
Abstract: The performance of simulated moving-bed reactor for two semicontinuous chromatographic reaction-separation processes, namely, isomerization of glucose to fructose (Hashimoto et al., 1993) and inversion of sucrose to glucose and fructose (Ganetsos et al., 1993), has been studied by mathematical modeling and numerical simulations. Simulation results agreed well with the published experimental results. The process performance, which is stated in terms of the process performance parameters defined in this paper, was also studied for various operating conditions, for both the processes. Since the reaction was introduced in the process, reaction conversion becomes a process performance parameter of importance, which was considered along with product purity and recovery. The criteria of the operating parameter (Ruthven and Ching, 1989) for linear systems for a simulated moving-bed process is not applicable for a simulated moving-bed reactor process in some cases.
Source Title: Industrial and Engineering Chemistry Research
URI: http://scholarbank.nus.edu.sg/handle/10635/67550
ISSN: 08885885
Appears in Collections:Staff Publications

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