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CFD study on particle-to-fluid heat transfer in fixed bed reactors: Convective heat transfer at low and high pressure

机译:固定床反应器中颗粒到流体传热的CFD研究:低压和高压对流传热

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摘要

Computational fluid dynamics (CID) has proven to be a reliable tool for fixed bed reactor design, through the resolution of 3D transport equations for mass, momentum and energy balances. Solution of these equations allow to obtain velocity and temperature profiles within the reactor. The numerical results obtained allow estimating useful parameters applicable to equipment design. Particle-to-fluid heat transfer coefficient is of primal importance when analyzing the performance of a fixed bed reactor. To gain insight in this subject, numerical results using a modified commercial CFD solver are presented and particle-to-fluid heat transfer in fixed beds is analyzed. Two different configurations are studied: forced convection at low pressure (with air as circulating fluid) and mixed (i.e., free + forced) convection at high pressure (with supercritical CO2 as circulating fluid). In order to impose supercritical fluid properties to the model, modifications into the CFD code were introduced by means of user defined functions (UDF) and user defined equations (UDE). The obtained numerical data is compared to previously published data and a novel CFD-based correlation (for free, forced and mixed convection at high pressure) is presented. (c) 2006 Elsevier Ltd. All rights reserved.
机译:通过解析质量,动量和能量平衡的3D传输方程,计算流体动力学(CID)已被证明是固定床反应器设计的可靠工具。这些方程式的求解允许获得反应器内的速度和温度曲线。获得的数值结果允许估算适用于设备设计的有用参数。当分析固定床反应器的性能时,颗粒到流体的传热系数至关重要。为了深入了解该主题,提出了使用改进的商用CFD求解器的数值结果,并分析了固定床中的颗粒-流体传热。研究了两种不同的配置:低压下的强制对流(以空气作为循环流体)和高压下的混合(即自由+强制)对流(以超临界CO2为循环流体)。为了对模型施加超临界流体特性,通过用户定义函数(UDF)和用户定义方程(UDE)对CFD代码进行了修改。将获得的数值数据与先前发布的数据进行比较,并提出了基于CFD的新型相关性(用于高压下的自由,强制和混合对流)。 (c)2006 Elsevier Ltd.保留所有权利。

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