Handling Model Plant Mismatch in State Estimation Using a Multiple Model-Based Approach

被引:9
作者
Arulmaran, Kevin [1 ]
Liu, Jinfeng [1 ]
机构
[1] Univ Alberta, Dept Chem & Mat Engn, Edmonton, AB T6G 2V4, Canada
关键词
PREDICTIVE CONTROL; SYSTEMS; OBSERVER; STRATEGY; REACTOR; FAULT;
D O I
10.1021/acs.iecr.7b00234
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Accurate state estimates are important for the success of model predictive control (MPC). State estimates are obtained using a model, but, in real plants, there will always be model plant mismatch (MPM), which affects these estimates. In this work, we present a multiple-model (MM)-based approach to obtain unbiased state estimates in the presence of MPM. Necessary assumptions on the source of mismatch and models used are presented. It is shown that unbiased output estimates do not guarantee unbiased state estimates. Our approach is shown to provide unbiased state estimates when all the assumptions are met using a froth flotation system. A model identification -based control approach using our multiple model estimation approach with a conventional MPC was tested on the froth flotation system and was found to successfully provide offset-free reference tracking when all the necessary assumptions for unbiased state estimation were met. A nonlinear offset-free MPC was also tested on the froth flotation system but was not able to provide offset-free reference tracking, because some necessary conditions were not met.
引用
收藏
页码:5339 / 5351
页数:13
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