首页> 外文会议>34th European Symposium of the Working Party on Computer Aided Process Engineering, 34th, May 27-30, 2001, Kolding, Denmark >On-line optimal operating policy and control of a batch free-radical polymerization process
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On-line optimal operating policy and control of a batch free-radical polymerization process

机译:间歇自由基聚合过程的在线最佳操作策略和控制

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An on-line optimizing control scheme that ensures the satisfaction of polymer property specifications under the influence of time-varying model parameters and unknown initial conditions is developed for the free-radical polymerization of methyl-methacrylate in a batch reactor. The control scheme combines a state/parameter estimation step based on on-line measurements of process variables that updates the values of model parameters with an optimization step that calculates the optimal operating policy. The control objectives require the satisfaction of quality specifications based on molecular weight properties (e.g. average molecular weights) of the final polymer product subject to time-varying kinetic parameters and unknown initial level of impurities in the reactor.
机译:针对间歇反应器中甲基丙烯酸甲酯的自由基聚合反应,开发了一种在线优化控制方案,以确保在时变模型参数和未知初始条件的影响下满足聚合物性能指标。该控制方案将基于过程变量在线测量的状态/参数估计步骤与更新模型参数值的优化步骤相结合,该优化步骤计算最佳操作策略。控制目标要求基于最终聚合物产物的分子量特性(例如平均分子量)的质量规格的满足,所述最终聚合物产物受到时变动力学参数和反应器中杂质的未知初始水平的影响。

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