控制理论(社会学)
解耦(概率)
自抗扰控制
非线性系统
分馏塔
内部模型
国家观察员
蒸馏
模型预测控制
过程控制
控制工程
过程(计算)
计算机科学
工程类
控制(管理)
化学
物理
操作系统
人工智能
量子力学
有机化学
作者
Yun Cheng,Zengqiang Chen,Mingwei Sun,Qinglin Sun
标识
DOI:10.1177/0142331220908989
摘要
Although the heat integrated distillation is an energy-efficient and environment-friendly separation technology, it has not been commercialized. One of the reasons is that the nonlinear dynamics and the interactions between various control loops have limited the performance of the traditional control strategy. To achieve a high-purity product concentration, a dynamic decoupling control strategy based on active disturbance rejection control (ADRC) is proposed. The effects of interactions, uncertainties and external disturbances can be estimated and rejected by using extended state observer. Considering the constraints on manipulated variables, an optimized ADRC is designed for the first-order system. Moreover, a concentration observer based on a nonlinear wave model is formulated to reduce the number of sensors. In the simulation research, the related internal model control (IMC), multi-loop ADRC and model predictive control (MPC) are compared with the proposed control scheme. The simulation results demonstrate the advantages of the proposed control scheme on tight control, decoupling performance and disturbance rejection for the high-purity heat integrated distillation column.
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