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Cold model investigation of mixing-separation time distribution in a multi-element process coupled cyclone reactor for ionic liquid-catalyzed isobutane/butene alkylation

机译:冷模型调查多元素过程中混合分离时间分布的旋风反应器离子液催化异丁烷/丁烯烷基化

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The residence time distributions of a dispersed phase in a multi-element process coupled cyclone reactor for ionic liquid-catalyzed isobutane/butene alkylation were numerically studied with a CFD method. The Eulerian-Eulerian multiphase flow model and Reynolds stress model were applied to simulate the flow field distribution in the cyclone reactor. The time in which the dispersed phase flows from the inlet slot to the overflow outlet tube is defined as the mean mixing-separation time between two phases in the cyclone reactor. The effects of the structural parameter of the slot on the mean mixing-separation time were investigated in this work. The results show that the residence time distributions are unimodal except for the condition that the number of slots is 1. Besides, it is concluded that the velocity of dispersed phase flow into the reaction chamber and the relative velocity between two phases in the cyclone reactor are the main influence factors. Based on the results, a prediction model to explain the relationship between the mean mixing-separation time and the velocity of two phases was established.
机译:用CFD方法对分散相偶联的离子液体催化异丁烷/丁烯烷基化的分散相的分散相分布在数值上进行数值研究。应用欧拉欧拉多相流动模型和雷诺应力模型来模拟旋风反应器中的流场分布。分散相从入口槽流到溢流出口管的时间被定义为旋风反应器中的两个阶段之间的平均混合分离时间。在这项工作中研究了槽结构参数对平均混合分离时间的影响。结果表明,除了槽数为1的条件之外,停留时间分布是单峰的。此外,结论是分散相流入反应室的分散相流程的速度和旋风反应器中的两个相之间的相对速度主要影响因素。基于结果,建立了一种预测模型来解释平均混合分离时间与两个阶段的速度之间的关系。

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    《RSC Advances》 |2019年第49期|共10页
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  • 正文语种 eng
  • 中图分类 化学;
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