A model predictive functional control based on proportional-integral-derivative (PID) and proportional-integral-proportional-derivative (PIPD) using extended non-minimal state space: Application to a molten carbonate fuel cell process

作     者：Kim, Beom Seok Kim, Tae Young Park, Tae Chang Yeo, Yeong Koo 

作者机构：Hanyang Univ Dept Chem Engn Seoul 04763 South Korea 

出 版 物：《KOREAN JOURNAL OF CHEMICAL ENGINEERING》 (韩国化工杂志)

年 卷 期：2018年第35卷第8期

页      面：1601-1610页

核心收录：

学科分类：081704[工学-应用化学] 0817[工学-化学工程与技术] 08[工学] 0703[理学-化学] 

基　　金：Korea Research Foundation Grant - Korean Government [NRF-2017R1A2B1005649] 

主　　题：PID Control PIPD Control Extended Non-minimal State Space Model Predictive Functional Control Molten Carbonate Fuel Cell Numerical Simulation 

摘      要：The performance of most controllers, including proportional-integral-derivative (PID) and proportional-integral-proportional-derivative (PIPD) controllers, depends upon tuning of control parameters. In this study, we propose a novel tuning strategy for PID and PIPD controllers whose control parameters are tuned using the extended non-minimal state space model predictive functional control (ENMSSPFC) scheme based on the auto-regressive moving average (ARMA) model. The proposed control method is applied numerically in the operation of the MCFC process with the parameters of PID and PIPD controllers being optimized by ENMSSPFC based on the ARMA model for the MCFC process. Numerical simulations were carried out to assess the set-point tracking performance and disturbance rejection performance both for the perfect plant model, which represents the ideal case, and for the imperfect plant model, which is usual in practical applications. When there exists uncertainty in the plant model, the PIPD controller exhibits better overall control performance compared to the PID controller.