Adaptive temperature control in a tubular chemical reactor

P. Dostál, V. Bobál, J. Vojtesek
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引用次数: 3

Abstract

The paper deals with adaptive control of a tubular chemical reactor. As a part of the control design, preliminary steady-state and dynamic analysis of the process is incorporated. A nonlinear model of the process is approximated by a continuous-time external linear model with parameters estimated using a corresponding delta model. The controller design is based on the polynomial approach. The adaptive control is tested on the nonlinear model of the tubular chemical reactor with a consecutive exothermic reaction.
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管式化学反应器的自适应温度控制
本文研究了管式化工反应器的自适应控制问题。作为控制设计的一部分,对过程进行了初步的稳态和动态分析。该过程的非线性模型由连续时间外部线性模型近似,参数估计使用相应的delta模型。控制器的设计基于多项式方法。对具有连续放热反应的管式化学反应器的非线性模型进行了自适应控制试验。
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