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Closed-loop Implementation of OptimalTrajectories in Batch Distillation

机译:分批蒸馏中最优轨迹的闭环实现

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In order to implement a quasi-optimal trajectory derived from pinch theory[1,2], a temperature tracking control system composed by an open-loop refluxratio control plus a closed-loop correction for disturbance rejection is proposed.To adjust the closed-loop controller we use the referential dynamic reaction ofthe process [3] and tuning rules [4] that, though they were originally developedfor dynamics valid in the neighborhood of stationary operating points, underthis strategy they are useful in the neighborhood of a reference transientevolution like those occurring in batch distillation columns. The separation ofthe light component from its ternary mixture of alcohols is studied here.
机译:为了实现从捏理论推导的准最优轨迹 [1,2],由开环回流组成的温度跟踪控制系统 提出了比率控制和抑制干扰的闭环校正方法。 为了调整闭环控制器,我们使用参考动态响应 流程[3]和调整规则[4],尽管它们最初是开发的 对于在固定工作点附近有效的动力学,在 这种策略在参考瞬态附近很有用 像间歇式蒸馏塔中发生的那样演变。分离 本文研究了其三元醇混合物中的轻组分。

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