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Modelling and Variable Structure Control of Batch Process with External Heat Exchanger
外部に熱交換器をもつバッチ反応器のモデリングと可変構造制御
1990
Transactions of the Society of Instrument and Control Engineers
外部に熱交換器をもつバッチ反応器のモデリングと可変構造制御
The mathematical model of a semi-batch polymerization reactor is derived by considering the basic equations of reaction rate, mass balances and energy balances. Experimental result confirmed the justification of this model. The model still has several unknown parameters. Then the sliding-mode control strategy based on the mixer model is used. It is shown that this control system has good dynamic response and robustness to parameter deviations. Then, it is confirmed in the production reactor
doi:10.9746/sicetr1965.26.1399
fatcat:gwhs6uhd4jaftewzxtoys64cd4