首页> 外文期刊>Powder Technology: An International Journal on the Science and Technology of Wet and Dry Particulate Systems >A preliminary CFD study of the gas-solid flow fields in multizone circulating polymerization reactors
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A preliminary CFD study of the gas-solid flow fields in multizone circulating polymerization reactors

机译:多区循环聚合反应器中气固流场的CFD初步研究

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摘要

A Eulerian-Eulerian model incorporating the kinetic theory of granular flow is adopted to describe the gas-solid two-phase flows in a multizone circulating propylene polymerization reactor. Corresponding simulations are carried out in a commercial computational fluid dynamics (CFD) code Fluent. First, the model is validated by comparing simulation results with the experimental data. Entire fields in the reactor composed of a riser and a downer are also obtained numerically. Furthermore, the model is used to distinguish the flow behaviors in the riser and the downer. The effects of riser-outlet configuration and operation gas velocity on the flow behaviors in the reactor are also investigated numerically. The simulated results show that the flow behaviors in the riser of MZCR are different from those in the downer of MZCR. In addition, the simulation results also show that both the exit configuration of the riser and the operation gas velocity can significantly affect the flow behaviors in the MZCR.
机译:采用结合颗粒流动动力学理论的欧拉-欧拉模型来描述多区域循环丙烯聚合反应器中的气固两相流。以商业计算流体动力学(CFD)代码Fluent进行相应的模拟。首先,通过将仿真结果与实验数据进行比较来验证模型。还可以通过数值获得反应堆中由提升管和下降管组成的整个场。此外,该模型用于区分上升管和下降管中的流动行为。还数值研究了立管出口构造和操作气体速度对反应器中流动行为的影响。模拟结果表明,MZCR上升管中的流动特性与MZCR下降管中的不同。此外,仿真结果还表明,立管的出口配置和工作气体速度都可以显着影响MZCR中的流动行为。

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