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Systematic Design of Chemical Reactors with Multiple Stages via Multi-Objective Optimization Approach

机译:通过多目标优化方法进行多级化学反应器的系统设计

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The purpose of this study is to extend the approach that was introduced by Hillestad (2010) to handle chemical reactor design problem with multiple stages. Specifically, multi-objective optimization method will be used to generate Pareto optimal solutions that characterize the non-inferior solutions set for the problem. Following the identification of path-dependent design variables, several (possibly conflicting) design objectives will be selected and solutions of the corresponding problem will be generated from multi-objective optimization algorithm. This approach is investigated for two industrially important reactor systems: ethylene oxide and phthalic anhydride synthesis. By using reference-point based multi-objective evolutionary algorithm (R-NSGA-II), Pareto-optimal solutions are successfully generated within the region of user-specified reference points, thus facilitating in the selection of final optimal designs. Apart from the extensive selection of optimal candidate reactor designs, this approach also enables further insights to be obtained regarding the optimal arrangement of the path-dependent design variables along the reactor length.
机译:本研究的目的是扩展由Hillestad(2010)引入的方法,以处理多个阶段的化学反应器设计问题。具体地,将使用多目标优化方法来生成据表征用于问题的非劣液解决方案的Pareto最佳解决方案。在识别依赖于依赖的设计变量之后,将选择几个(可能冲突)的设计目标并且将从多目标优化算法生成相应的问题的解决方案。对两辆工业上重要的反应堆系统进行​​了研究方法:环氧乙烷和邻苯二甲酸酐合成。通过使用基于参考点的多目标进化算法(R-NSGA-II),在用户指定的参考点的区域内成功地生成了Pareto-Optimal解决方案,从而促进了最终最佳设计的选择。除了广泛选择的最佳候选反应器设计外,这种方法还可以实现关于沿反应器长度的路径依赖性设计变量的最佳布置的进一步见解。

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