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Investigating control schemes for an Ideal Thermally Coupled Distillation Column (ITCDIC)

机译:理想热耦合蒸馏塔(ITCDIC)的研究控制方案

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The control schemes of an ITCDIC are addressed. A modified IMC scheme (M-IMC) is proposed to overcome model/plant mismatch of the Internal Model Control scheme (IMC). Predictive PID control (P-PID) and Adaptive Predictive control (AP-PID) schemes are also presented to improve effectively the response speed of the multi-loop PID control (M-PID) and eliminate its residual error. A detailed comparative investigation on the above five control schemes was performed. Simulation results demonstrate all the schemes are able to keep two end products within their specifications. M-IMC is the best one with the fastest response speed. AP-PID is the second choice since it is better at dealing with sudden set-point transitions and complex external disturbances than P-PID. M-PID cannot compete with AP-PID and P-PID due to its slow servo response speed and large residual error. IMC ranks last as it is extremely sensitive to changes in the operating conditions.
机译:解决了ITCDIC的控制方案。提出了一种改进的IMC方案(M-IMC),以克服内部模型控制方案(IMC)的模型/工厂不匹配问题。还提出了预测PID控制(P-PID)和自适应预测控制(AP-PID)方案,以有效提高多回路PID控制(M-PID)的响应速度并消除其残留误差。对以上五个控制方案进行了详细的比较研究。仿真结果表明,所有方案都可以将两个最终产品保持在其规格范围内。 M-IMC是响应速度最快的最佳产品。 AP-PID是第二选择,因为它比P-PID更好地处理突然的设定点转换和复杂的外部干扰。 M-PID伺服响应速度慢且残留误差大,因此无法与AP-PID和P-PID竞争。 IMC排名第二,因为它对运行条件的变化极为敏感。

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