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首页> 外文期刊>Journal of Chemical Engineering of Japan >GAS HOLDUP AND PRESSURE DROP IN THREE-PHASE HORIZONTAL FLOWS OF GAS-LIQUID-FINE SOLID PARTICLES SYSTEM
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GAS HOLDUP AND PRESSURE DROP IN THREE-PHASE HORIZONTAL FLOWS OF GAS-LIQUID-FINE SOLID PARTICLES SYSTEM

机译:气液细固体颗粒系统三相水平流动中的气体滞留和压降

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摘要

References(8) Cited-By(5) Gas holdups and pressure drops of gas-liquid-solid cocurrent three-phase flow containing fine solid particles of 30, 60 and 100μm average size were measured in horizontal tubes and the following results were obtained. (1) Gas holdups at the conditions of homogeneous slurry flow are the same as those of gas-liquid two-phase flow. However, the heterogeneity of slurry flow reduces the gas holdup. Considering these aspects, a gas holdup correlation of gas-liquid-solid three-phase horizontal flow is proposed to correlate the data over a wide range of operating conditions. (2) Pressure drops of gas-liquid-solid three-phase flow in horizontal tubes are more considerably influenced by solid intermixing than those in vertical tubes. A correlation to describe the pressure drop of gas-liquid-solid three-phase horizontal flow is proposed.
机译:参考文献(8)引用(5)在水平管中测量平均尺寸分​​别为30、60和100μm的细小固体颗粒的气-液-固并流三相流的持气量和压降,并获得以下结果。 (1)均匀浆液流动条件下的气体滞留率与气液两相流动相同。但是,泥浆流的非均质性会降低气体滞留率。考虑到这些方面,提出了气-液-固三相水平流的气体滞留率相关性,以在较宽的运行条件范围内使数据相关。 (2)与垂直管相比,水平混合管中气液固三相流的压降受固相混合的影响更大。提出了描述气液固三相水平流压降的相关性。

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