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