DocumentCode :
2841512
Title :
Simulation of Simulated Moving Bed process model
Author :
Li, Ling ; Yuan, De-Cheng ; Jing, Yuan-Wei
Author_Institution :
Dept. of Inf. Eng., Shenyang Inst. of Chem. Technol., Shenyang, China
fYear :
2010
fDate :
26-28 May 2010
Firstpage :
3961
Lastpage :
3965
Abstract :
Based on the single column partial differential equation model for the industry chromatographic separation, the mathematical model of the Simulated Moving Bed chromatographic separation process is established from the flow and mass conservation relations of the SMB process. Method of line is used for the numeric model computations. Computerized simulation results show that compared with the true moving bed model, the established model takes into consideration the periodic switch at the feed inlets and outlets, hence reflects the conditions in a true SMB process.
Keywords :
chemical engineering; chromatography; partial differential equations; separation; computerized simulation; industry chromatographic separation; mass conservation; numeric model computations; simulated moving bed process model; single column partial differential equation model; Chemical technology; Computational modeling; Educational institutions; Electronic mail; Finite element methods; Information science; Mathematical model; Partial differential equations; Separation processes; Switches; Chromatography separation process; Mathematical model; Method of line; Simulated Moving Bed;
fLanguage :
English
Publisher :
ieee
Conference_Titel :
Control and Decision Conference (CCDC), 2010 Chinese
Conference_Location :
Xuzhou
Print_ISBN :
978-1-4244-5181-4
Electronic_ISBN :
978-1-4244-5182-1
Type :
conf
DOI :
10.1109/CCDC.2010.5498455
Filename :
5498455
Link To Document :
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