• DocumentCode
    1645455
  • Title

    The Application of Model PID or IMC-PID Advanced Process Control to Refinery and Petrochemical Plants

  • Author

    Xinping, Zhen ; Quanshan, Li ; Huan, Wei ; Wenxin, Wang ; Qibing, Jin ; Lideng, Pan

  • Author_Institution
    Beijing Univ. of Chem. Technol., Beijing
  • fYear
    2007
  • Firstpage
    699
  • Lastpage
    703
  • Abstract
    An advanced process control algorithm, namely, model PID or IMC-PID based on internal model control (IMC), is developed. They can be implemented on DCS. The original PID parameters need to be modified into IMC-PID parameters, which are calculated by the process models. It significantly increases the control speed and the accuracy, and also has good tracking ability for the set-point control, combining with improved robustness for disturbance and model´s time-varying character. It had successfully applied to refinery and petro-chemical plants, and has potential wide applications on other plants also.
  • Keywords
    petrochemicals; process control; refining; three-term control; IMC-PID advanced process control; IMC-PID parameters; internal model control; model PID advanced process control; petrochemical plants; refinery; set-point control; tracking; Automatic control; Control systems; Design optimization; Distributed control; Equations; Petrochemicals; Process control; Robust control; Three-term control; Transfer functions; IMC PID control; NLJ optimization algorithm; closed loop process model identification; model PID control;
  • fLanguage
    English
  • Publisher
    ieee
  • Conference_Titel
    Control Conference, 2007. CCC 2007. Chinese
  • Conference_Location
    Hunan
  • Print_ISBN
    978-7-81124-055-9
  • Electronic_ISBN
    978-7-900719-22-5
  • Type

    conf

  • DOI
    10.1109/CHICC.2006.4347098
  • Filename
    4347098