Optimal PIP Control of a pH Neutralization Process Based on State-Dependent Parameter Model

被引:3
|
作者
Ogun, Oluwaseyi A. [1 ]
Festus, Mbetobong U. [2 ]
Inyang, Isonguyo J. [3 ]
机构
[1] Coventry Univ, Control Theory & Applicat Ctr, Coventry CV1 5FB, W Midlands, England
[2] Akwa Ibom State Univ, Elect & Elect Engn Dept, Mkpat Enin, Akwa Ibom State, Nigeria
[3] Cranfield Univ, Sch Aerosp Transport & Mfg, Cranfield MK43 0AL, Beds, England
来源
IFAC PAPERSONLINE | 2017年 / 50卷 / 02期
关键词
Proportional-Integral-Plus (PIP); Linear Quadratic (LQ); State Variable Feedback (SVF); State-Dependent Parameter (SDP); pH Neutralization; FEEDBACK POLE ASSIGNMENT; SYSTEMS; CLIMATE; DESIGN; TIME;
D O I
10.1016/j.ifacol.2017.12.007
中图分类号
TP [自动化技术、计算机技术];
学科分类号
0812 ;
摘要
In this paper, an optimal Proportional-Integral-Plus (PIP) controller based on State Dependent Parameter (SDP) model is developed to control a highly nonlinear and time-varying pH neutralization process. Since the reaction invariants of the pH process are unavailable for direct measurement, a state observer is required for their estimation. Unfortunately, a closed-loop state observer cannot be designed for the pH process due to the decoupled nature of the reaction invariant dynamics. However, this problem is circumvented by engaging the power of State Variable Feedback (SVF) in the context of a Non-Minimum State Space (NMSS) framework. Furthermore, to compensate for process nonlinearities and unmeasured disturbances, an SDP model is identified using data collected from open-loop experiment, and a straightforwardly tuned optimal PIP controller is subsequently designed based on the SDP model to obtain the SDP-PIP controller. For benchmark purposes, a digital PI controller is designed and results are compared with those from the SDP-PIP controller. Simulation results show that SDP-PIP outperforms PI both in set point and disturbance changes. (C) 2017, IFAC (International Federation of Automatic Control) Hosting by Elsevier Ltd. All rights reserved.
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页码:37 / 42
页数:6
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