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Steady State Model for Heat Transfer in a Packed Bed Reactor of Elliptic Cylindrical Shape

机译:椭圆形填充床反应器中传热的稳态模型

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摘要

The fixed-bed reactors of circular cylindrical geometry with heated or coolednwalls are frequently used to carry out heterogeneous reactions of solid-gas typenin engineering applications. The design of a fixed bed reactor requires an extensivenknowledge of heat transfer characteristics within the packed bed. In thisnsense, this work presents a three-dimensional mathematical model to predict thenheat transfer inside a fixed bed elliptical cylinder heat exchanger. The modelnconsiders uniform velocity and temperature profiles of the fluid phase at the entrancenof the reactor, and constant thermo-physical properties. The surface of thenequipment convective boundary condition is assumed to be constant. The energynequation, written in the elliptical cylindrical coordinates, was discretized usingna finite-volume method considering a fully implicit formulation, and WUDS interpolationnscheme. Numerical results of the dimensionless temperature profilesninside the packed bed reactor at a steady state are presented and temperature distributionnis interpreted. To validate the model, numerical results obtained for thencircular cylinder are compared with analytical results from literature and a goodnagreement was obtained.
机译:具有加热的壁或冷却的壁的圆柱形几何形状的固定床反应器通常用于进行固体气体丁二烯工程应用中的异质反应。固定床反应器的设计要求填充床内具有广泛的传热特性。在这种意义上,这项工作提出了一个三维数学模型来预测固定床椭圆形圆柱体热交换器内部的热传递。该模型考虑了反应器入口处液相的均匀速度和温度分布,以及恒定的热物理性质。设设备对流边界条件的表面假定为常数。考虑到完全隐式公式和WUDS插值方法,使用有限体积方法离散化了写在椭圆圆柱坐标上的能量方程。给出了稳态条件下填充床反应器内无因次温度分布的数值结果,并解释了温度分布。为了验证该模型,将圆柱的数值结果与文献的分析结果进行了比较,并取得了良好的共识。

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