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CO-PrOx reactor design by model-based optimization

机译:通过基于模型的优化设计CO-PrOx反应器

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This work analyzes the CO-PrOx reactor design as a component of the CO clean-up system of the ethanol processor for H_2 production applied to PEM fuel cells. The operating conditions of the processor require compact and lightweight pieces of equipment and efficient operation at different conditions. An eggshell catalyst type of Pt/Al_2O_3 is considered. One-dimensional heterogeneous catalytic reactor model accounting for interfacial gradients is used to optimize the PrOx reactor. Different reactor components are added gradually to illustrate how the system dimensions and configuration change after optimization. The optimization problem determines the optimal reactor length, reactor diameter, catalyst particle diameter, inlet reactants temperature and insulating material thickness that minimize the total system volume. On these model-based results, the final reactor design is mainly governed by the presence of hemispherical heads (distributor and collector). Different inlet CO compositions and power generation targets are analyzed. According to the inlet CO level, more than one catalytic stage is required to meet design goals and fulfill process constraints. The model-based reactor optimization of the pseudo-adiabatic operation allows obtaining both designs for reducing volumes and optimal operating conditions that allows conventional reactor technology. Afterwards, simulation runs based on a rigorous one-dimensional heterogeneous catalytic reactor model accounting for intra-particle gradients are performed using data obtained from model-based optimization results. The aim of these simulations is to verify feasibility of the optimal design obtained from the proposed one-dimensional heterogeneous catalytic reactor model without intra-particle gradients, which is intended to approximate an egg-shell catalyst behavior. The present work reflects clearly the advantages of applying mathematical programming techniques to optimize both design and operation conditions of the PrOx reactor.
机译:这项工作分析了CO-PrOx反应堆的设计,将其作为应用于PEM燃料电池的H_2生产乙醇处理器的CO净化系统的组成部分。处理器的工作条件要求紧凑轻巧的设备,以及在不同条件下的有效运行。考虑了蛋壳催化剂类型为Pt / Al_2O_3。考虑界面梯度的一维非均相催化反应器模型用于优化PrOx反应器。逐步添加不同的反应堆组件,以说明优化后系统尺寸和配置如何变化。最优化问题决定了最佳的反应器长度,反应器直径,催化剂粒径,入口反应物温度和绝缘材料厚度,它们使总系统体积最小化。根据这些基于模型的结果,最终的反应堆设计主要取决于半球形压头(分配器和收集器)的存在。分析了不同的入口CO组成和发电目标。根据入口的CO水平,需要多个催化阶段才能达到设计目标并满足工艺约束。准绝热操作的基于模型的反应器优化允许获得用于减小体积的设计以及允许常规反应器技术的最佳操作条件。然后,使用从基于模型的优化结果中获得的数据,基于考虑颗粒内梯度的严格的一维非均相催化反应器模型进行模拟运行。这些模拟的目的是验证从拟议的一维非均相催化反应器模型获得的最佳设计的可行性,该模型没有颗粒内梯度,旨在近似卵壳催化剂的行为。本工作清楚地反映了应用数学编程技术来优化PrOx反应器的设计和操作条件的优势。

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