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PID Controller Design Based on the Time Domain Information of Robust IMC Controller Using Maximum Sensitivity 被引量:14

PID Controller Design Based on the Time Domain Information of Robust IMC Controller Using Maximum Sensitivity
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摘要 The IMC(Internal Model Control) controller based on robust tuning can improve the robustness and dynamic performance of the system.In this paper,the robustness degree of the control system is investigated based on Maximum Sensitivity(Ms) in depth.And the analytical relationship is obtained between the robustness specification and controller parameters,which gives a clear design criterion to robust IMC controller.Moreover,a novel and simple IMC-PID(Proportional-Integral-Derivative) tuning method is proposed by converting the IMC controller to PID form in terms of the time domain rather than the frequency domain adopted in some conventional IMC-based methods.Hence,the presented IMC-PID gives a good performance with a specific robustness degree.The new IMC-PID method is compared with other classical IMC-PID rules,showing the flexibility and feasibility for a wide range of plants. The IMC(Internal Model Control) controller based on robust tuning can improve the robustness and dynamic performance of the system.In this paper,the robustness degree of the control system is investigated based on Maximum Sensitivity(Ms) in depth.And the analytical relationship is obtained between the robustness specification and controller parameters,which gives a clear design criterion to robust IMC controller.Moreover,a novel and simple IMC-PID(Proportional-Integral-Derivative) tuning method is proposed by converting the IMC controller to PID form in terms of the time domain rather than the frequency domain adopted in some conventional IMC-based methods.Hence,the presented IMC-PID gives a good performance with a specific robustness degree.The new IMC-PID method is compared with other classical IMC-PID rules,showing the flexibility and feasibility for a wide range of plants.
出处 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2013年第5期529-536,共8页 中国化学工程学报(英文版)
基金 Supported by the National Natural Science Foundation of China(61273132) Doctoral Fund of Ministry of Education of China(20110010110010)
关键词 PID控制器 设计标准 IMC 鲁棒性 灵敏度 时域信息 控制系统 PID方法 internal model control-PID robustness parameter tuning maximum sensitivity function
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参考文献19

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同被引文献53

  • 1王全良,甄新平,潘立登,闻光辉.多变量系统解耦内模控制及其PID转化应用方法的研究[J].北京化工大学学报(自然科学版),2005,32(6):87-89. 被引量:12
  • 2刘涛,张卫东,欧林林.双输入输出时滞过程解耦控制的解析设计[J].控制理论与应用,2006,23(1):31-37. 被引量:16
  • 3Panda R C.Synthesis of PID controller for unstable and integrating processes[J].Chemical Engineering Science,2009,64(12):2807-2816.
  • 4Nasution A A,Jeng J C,Huang H P.Optimal H 2IMC-PID controller with set-point weighting for time-delayed unstable processes[J].Industrial&Engineering Chemistry Research,2011,50(8):4567-4578.
  • 5Alcantara S,Vilanova R,Pedret C.PID control in terms of robustness/performance and servo/regulator trade-offs:A unifying approach to balanced autotuning[J].Journal of Process Control,2013,23(4):527-542.
  • 6Shamsuzzoha M,Lee M.Analytical design of enhanced PID filter controller for integrating and first order unstable processes with time delay[J].Chemical Engineering Science,2008,63(10):2717-2731.
  • 7Normey-Rico J E,Camacho E F.Simple robust dead-time compensator for first-order plus dead-time unstable processes[J].Industrial&Engineering Chemistry Research,2008,47(14):4784-4790.
  • 8Tan W.Analysis and design of a double two-degree-of-freedom control scheme[J].ISA Transactions,2010,49(3):311-317.
  • 9Liu T,Gao F.Enhanced IMC design of load disturbance rejection for integrating and unstable processes with slow dynamics[J].ISA Transactions,2011,50(2):239-248.
  • 10Shamsuzzoha M,Skliar M,Lee M.Design of IMC filter for PID control strategy of open-loop unstable processes with time delay[J].Asia-Pacific Journal of Chemical Enginee-ring,2012,7(1):93-110.

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