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Tracking-error-based control of a chemical reactor using decoupled dynamic variables

机译:解耦动态变量对化学反应器的基于跟踪误差的控制

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This work proposes an advanced control strategy for an open non-isothermal homogeneous reactor by integrating alternative model of the system dynamics based on variant and invariant states with the tracking-error-based control method in the framework of port-Hamiltonian representation. More precisely, a linear transformation is used to transform the original dynamics into a new model, where the enthalpy, reaction variant and reaction invariant are the state variables. Then, the transformed model is formulated into the port-Hamiltonian structure before the tracking-error-based approach is applied to design the controllers for the purpose of stabilization. The numerical simulations for the first order reaction modelled with the continuous stirred tank reactor having the multiplicity behavior subsequently show that the proposed feedback law is able to stabilize the system at the desirable equilibrium point.
机译:这项工作提出了一种开放的非等温均质反应堆的高级控制策略,该方法通过将基于变异和不变状态的系统动力学的替代模型与基于哈密顿量表示的框架中基于跟踪误差的控制方法相集成。更准确地说,使用线性变换将原始动力学变换为新模型,其中焓,反应变量和反应不变量是状态变量。然后,在基于跟踪误差的方法被用于设计控制器以达到稳定的目的之前,将转换后的模型公式化为哈密尔顿港结构。随后,以具有多重行为的连续搅拌釜反应器为模型进行的一阶反应的数值模拟表明,所提出的反馈定律能够将系统稳定在所需的平衡点。

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