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Liquid hold-up and backmixing in cocurrent upflow three-phase fixed-bed reactors

机译:并流上流三相固定床反应器中的液体滞留和返混

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摘要

Liquid-phase hydrodynamics is studied in a three-phase fixed bed with cocurrent upflow of gas and liquid. Residence-time distributions are measured to determine liquid hold-up and backmixing using different liquids and glass beads of two sizes. Two types of correlations are tested for liquid saturation. Correlations based on the drift flux concept are found to account for experimental results. Liquid mixing is described in terms of the axial dispersion model. A close relation between the axial dispersion coefficient and the bubbles sizes estimated using the theory of fluid emulsions is found. Hence, a new type of correlation is proposed to estimate axial dispersion coefficients in this type of reactors. This correlation considers the influences an the Peclet number of the liquid Reynolds number end the two-phase flow dissipation power rate, which would determine bubbles sizes. (C) 1998 Elsevier Science Ltd. All rights reserved. [References: 33]
机译:在三相固定床中,随着气体和液体的并流向上流动,研究了液相流体力学。测量停留时间分布,以确定使用不同液体和两种尺寸的玻璃珠的液体滞留率和返混率。测试了两种相关性的液体饱和度。发现基于漂移通量概念的相关性可以解释实验结果。根据轴向分散模型描述了液体混合。发现使用流体乳液理论估算的轴向弥散系数与气泡尺寸之间存在密切关系。因此,提出了一种新型的相关性来估计这种类型的反应堆中的轴向弥散系数。这种相关性考虑了液体雷诺数的佩克雷特数对两相流耗散功率率的影响,这将决定气泡的大小。 (C)1998 Elsevier ScienceLtd。保留所有权利。 [参考:33]

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