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The mechanism model of gas-liquid mass transfer enhancement by fine catalyst particles

机译:催化剂细颗粒促进气液传质的机理模型

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In order to present the enhancement of gas-liquid mass transfer by heterogeneous chemical reaction near interface,the mechanism model has been proposed to describe the mass transfer rate for a gas-liquid-solid system containing fine catalyst particles.The composite grid technique has been used to solve the model equations.With this model the effect of particle size,first-order reaction rate constant,distance of particle to gas-liquid interface and residence time of particle near gas-liquid interface on the mass transfer enhancement have been discussed.The particle-particle interaction and slurry apparent viscosity can be considered in the model.The experimental data have been used to verify the model,and the agreement has been found to be satisfied.
机译:为了通过界面附近的多相化学反应促进气液传质,提出了一种机理模型来描述含细催化剂颗粒的气液固系统的传质速率。利用该模型讨论了粒径,一阶反应速率常数,粒子到气液界面的距离以及粒子在气液界面附近的停留时间对传质增强的影响。在模型中可以考虑颗粒间的相互作用和浆液的表观粘度。通过实验数据对模型进行了验证,发现符合要求。

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