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Investigation of bubble breakup and coalescence in a packed-bed reactor - Part 1: A comparative study of bubble breakup and coalescence models

机译:填充床反应器中气泡破裂和聚结的研究第1部分:气泡破裂和聚结模型的比较研究

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摘要

In a packed-bed reactor a comparative study of bubble breakup and coalescence models has been investigated to study bubble size distributions as a function of the axial location. The bubble size distributions are obtained by solving population balance equations that describe gas-liquid interactions. Each combination of bubble breakup and coalescence models is examined under two inlet flow conditions: (1) predominant bubble breakup flow and (2) predominant bubble coalescence flow. The resulting bubble size distributions, breakup and coalescence rates estimated by individual models, are qualitatively compared to each other. The change of bubble size distributions along the axial direction is also described with medians. The medians resulting from CFD analyses are compared against the experimental data. Since the predictions estimated by CFD analyses with the existing bubble breakup and coalescence models do not agree with the experimental data, a new bubble breakup and coalescence model that takes account of the geometry effects is required to describe gas-liquid interactions in a packed-bed reactor.
机译:在填充床反应器中,对气泡破裂和合并模型的比较研究进行了研究,以研究气泡尺寸分布随轴向位置的变化。气泡尺寸分布是通过求解描述气液相互作用的总体平衡方程获得的。在两个入口流量条件下检查了气泡破裂和合并模型的每种组合:(1)主要的气泡破裂流动和(2)主要的气泡合并流动。定性比较各个模型得出的气泡大小分布,破裂和聚结率。气泡尺寸分布沿轴向的变化也用中值描述。将CFD分析得出的中位数与实验数据进行比较。由于使用现有的气泡破裂和合并模型通过CFD分析估算的预测与实验数据不一致,因此需要一种考虑几何效应的新的气泡破裂和合并模型来描述填充床中的气液相互作用反应堆。

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