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Numerical analysis of temperature distributions in a gas-phasepolypropylene reactor with a single helical ribbon agitator

机译:单螺旋螺带式搅拌器气相聚丙烯反应器温度分布的数值分析

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A numerical simulation method was developed for estimating the temperature distribution in acommercial-scale gas-phase polypropylene reactor with a single helical ribbon agitator. The localvelocities of particle phase needed for calculation were determined by local averaging of theindividual particle velocities obtained by means of the DEM (Discrete Element Method) simulationcode that was developed by Kaneko et al. (2000, Powder Technology, 108, 55-64). The particletemperature distribution predicted by the present simulation was in good agreement with thatobtained in a commercial-scale reactor under high-pressure condition. A high temperature regionwas found to form near the inner side of the agitator. The effects of some operating conditions onthe temperature distribution were studied using this simulation method. It was found that thetemperature distribution became broader with increased production rate and with decreasedrotational speed of the agitator.
机译:开发了一种数值模拟方法来估算建筑物中的温度分布。 具有单个螺旋螺带式搅拌器的工业规模气相聚丙烯反应器。本地的 计算所需的粒子相速度是通过对粒子的局部平均来确定的。 通过DEM(离散元方法)模拟获得的单个粒子速度 由Kaneko等人开发的代码。 (2000,粉末技术,108,55-64)。粒子 本模拟预测的温度分布与 在工业规模的反应器中在高压条件下获得。高温地区 被发现在搅拌器内侧附近形成。某些运行条件对 用这种模拟方法研究了温度分布。发现, 随着生产率的提高和温度的降低,温度分布变得越来越宽 搅拌器的转速。

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