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Design of a moving bed reactor for the production of uranium tetrafluoride based on mathematical modeling

机译:基于数学模型的四氟化铀生产移动床反应器设计

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A new model has been developed to analyze the performance of a moving bed reactor producing uranium tetrafluoride. The model includes the solid and gas flow rates, heat transfer by convection, conduction and radiation between gas and solid streams and by the external surrounding. A kinetics model has been also developed for the gas-solid reactions on the basis of the grain model in which, the different resistances are taken into account to determine the overall reaction rates. This study provides an initial and theoretical basis for optimum design of the moving bed on the basis of the kinetics models. The optimum design is carried out from the viewpoint of required length of the reactor and the maximum conversion. According to the primary expectations which are provided by the kinetics models, the feed temperature seems not to have any effective influence on the reactor performance. On the other hand, it is predicted that the inlet gas flow rate contributes an important role. The investigations show that although the kinetics models are rather useful in primary estimations, the strong interdependence between different zones of the reactor may prevent general expressions.
机译:已经开发了一种新模型来分析生产四氟化铀的移动床反应器的性能。该模型包括固体和气体的流速,通过对流的热传递,气体和固体流之间以及外部环境之间的传导和辐射。在颗粒模型的基础上,还开发了用于气固反应的动力学模型,其中考虑了不同的阻力以确定总反应速率。该研究为动力学模型的优化设计提供了初步的理论基础。从反应器的所需长度和最大转化率的角度进行最佳设计。根据动力学模型提供的主要期望,进料温度似乎对反应器性能没有任何有效影响。另一方面,可以预料进气流量将起重要作用。研究表明,尽管动力学模型在初步估算中相当有用,但反应堆不同区域之间的强烈相互依存关系可能会阻止通用表达式。

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