• 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