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Decoupling based predictive control analysis of a continuous stirred tank reactor

机译:连续搅拌釜反应器的基于解耦的预测控制分析

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This paper presents a decoupling based model predictive control strategy for a process of continuous stirred tank reactor (CSTR). The MPC strategy when used along with decoupling compensation technique seem to suffer from increase in the computational complexity of the predictive control algorithm because of the additional dynamics of decoupling compensator. In this paper, we seek to reduce the computational burden on predictive control algorithm utilizing a simple decoupling technique for a process with loop interactions. A CSTR MIMO process is a benchmark problem for studying loop interactions. We compensate for loop interactions by directly modifying the plant model without changing its response characteristics provided plant and model mismatch is at minimum. The proposed strategy is compared for its simplicity with multi-variable decoupling control strategies with application to MPC in process industry. Simulations show that proposed technique efficiently reduces loop interactions in CSTR process.
机译:本文提出了一种基于解耦的连续搅拌釜反应器模型预测控制策略。 MPC策略与去耦补偿技术一起使用时,由于去耦补偿器的附加动态特性,似乎会增加预测控制算法的计算复杂度。在本文中,我们力求通过对循环相互作用的过程使用简单的解耦技术来减少预测控制算法的计算负担。 CSTR MIMO过程是研究环路相互作用的基准问题。我们通过直接修改工厂模型而不改变其响应特性来补偿回路交互,只要工厂和模型的不匹配最小即可。将所提出的策略的简单性与多变量解耦控制策略进行比较,并将其应用于过程工业中的MPC。仿真表明,所提出的技术有效地减少了CSTR过程中的回路相互作用。

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