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Local Liquid Side Mass Transfer Model in Gas-Liquid-Solid Three-Phase Flow Airlift Loop Reactor for Newtonian and Non-Newtonian Fluids

机译:牛顿和非牛顿流体的气固三相流气举环流反应器中的局部液体侧传质模型

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摘要

A small scale isotropic mass transfer model was developed for the local liquid side mass transfer coefficients in gas-liquid-solid three-phase flow airlift loop reactor for Newtonian and non-Newtonian fluids. It is based on Higbie's penetration theory and Kolmogoroff's theory of isotropic turbulence with k_1 = 3(2Dε_1~(1/3)/π)~(1/2)(η_1~(-1/3) - λ_f~(-1/3)), where ε_1 is local rate of energy dissipation, λ_f is the local microscale, η_1 is the local Kolmogoroff scale and D is the diffusion coefficient. The capability of the proposed model is discussed in the light of experimental data obtained from 12 L gas-liquid-solid three-phase flow airlift loop reactor using Newtonian and non-Newtonian fluids. Good agreement with the experimental data was obtained over a wide range of conditions suggesting a general applicability of the proposed model.
机译:针对牛顿和非牛顿流体的气液固三相流气举回路反应器中的局部液体侧传质系数,建立了一个小规模的各向同性传质模型。它基于Higbie的渗透理论和Kolmogoroff的各向同性湍流理论,其中k_1 = 3(2Dε_1〜(1/3)/π)〜(1/2)(η_1〜(-1/3)-λ_f〜(-1 / 3)),其中ε_1是局部能量耗散率,λ_f是局部微尺度,η_1是局部Kolmogoroff尺度,D是扩散系数。根据使用牛顿流体和非牛顿流体的12 L气液固三相流气举回路反应器获得的实验数据,讨论了该模型的功能。在广泛的条件下获得了与实验数据的良好一致性,表明了所提出模型的一般适用性。

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