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首页> 外文期刊>Chemical Engineering Science >Liquid holdup and pressure drop in the gas-liquid cocurrent downflow packed-bed reactor under elevated pressures
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Liquid holdup and pressure drop in the gas-liquid cocurrent downflow packed-bed reactor under elevated pressures

机译:高压下气液并流下流填充床反应器中的持液量和压降

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摘要

An experimental investigation of the residence time distribution, liquid holdup, and pressure drop in a gas-liquid downflow packed bed reactor with porous particles operated under elevated pressures is presented. The effects of the two-phase flow rates and reactor pressures on the external liquid holdup and pressure drop are discussed. A mechanistic model, which accounts for the interaction between the gas and liquid phases by incorporating the shear and velocity slip factors between phases, is employed to predict the external liquid holdup and pressure drop for the experimentally covered flow regime. The involved parameters, such as shear and velocity slip factors and Ergun single-phase flow bed constants, are calculated from the correlations developed via neural network regression. The model's predictions and the experimental observations at elevated pressure are compared. (C) 2004 Elsevier Ltd. All rights reserved.
机译:提出了在带有在升高的压力下操作的多孔颗粒的气液下行填充床反应器中的停留时间分布,液体滞留率和压降的实验研究。讨论了两相流速和反应器压力对外部持液量和压降的影响。通过结合两相之间的剪切和速度滑移因子来解决气相和液相之间相互作用的机械模型,用于预测实验覆盖的流态下的外部持液量和压降。所涉及的参数,例如剪切和速度滑移因子以及Ergun单相流化床常数,是根据通过神经网络回归建立的相关性来计算的。比较了模型在高压下的预测结果和实验观察结果。 (C)2004 Elsevier Ltd.保留所有权利。

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