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首页> 外文期刊>Chemical Engineering Science >Solid-liquid mass transfer analysis in a multi-phase tank reactor containing submerged coated inclined-plates: A computational fluid dynamics approach
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Solid-liquid mass transfer analysis in a multi-phase tank reactor containing submerged coated inclined-plates: A computational fluid dynamics approach

机译:包含浸没涂层斜板的多相罐式反应器中的固液传质分析:计算流体动力学方法

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摘要

Although there is a voluminous literature on the estimation of interphase transport parameters in conventional slurry bubble column reactors, these correlations are inadequate in photoreactors equipped with specialized internals to facilitate light harvesting efficiency of the photocatalyst. This is particularly germane to the present externally illuminated bubble column reactor containing titania-coated plates immersed in the liquid column at different angles of inclination. Thus, a computational fluid dynamics (CFD) procedure utilizing the Eulerian-Eulerian approach has been used to solve the governing differential equations for the solid liquid mass transport problem based on the standard k - ε{lunate} model incorporating additional terms that take account of the interfacial turbulent momentum transfer. Mass transfer from the surface of the coated-quartz plates to the liquid phase was modeled using the Launder-Spalding wall functions. The plates were coated with benzoic acid as solid substrate with water and air as the liquid and gas phases, respectively. The increase in mass transfer due to reduction of the boundary layer thickness during air-induced liquid recirculation on either side of the submerged inclined plates was correlated with difference between turbulent and molecular Schmidt numbers via an adjustable parameter, A. CFD simulation using the Launder-Spalding wall function (with A = 1.08) gave better agreement with experimental transient concentration profiles than calculations based on FLUENT's enhanced wall function for the plate orientations (θ = 0~({ring operator}), 22 . 5~({ring operator}), and 45~({ring operator})) studied. The solid-to-liquid mass transfer was higher on the lower-side of the plate than the upper-side. In particular, mass transfer coefficient was higher with the inclined plate than with the vertical or horizontal orientation suggesting an added advantage for the application of the system as a solar photoreactor.
机译:尽管有大量文献对常规淤浆鼓泡塔反应器中的相间传输参数进行了估算,但这些相关性在配备特殊内部构件以促进光催化剂光收集效率的光反应器中是不充分的。这与本发明的外部照明的鼓泡塔反应器特别相关,该反应器包含以不同的倾角浸入液柱的二氧化钛涂覆的板。因此,基于标准k-ε{lunate}模型,结合了考虑了以下因素的附加项,利用欧拉-欧拉方法的计算流体动力学(CFD)程序已解决了固液传质问题的控制微分方程。界面湍动量传递。使用Launder-Spalding壁函数对从涂层石英板表面到液相的质量转移进行建模。将板用苯甲酸作为固体基质涂覆,分别以水和空气作为液相和气相。通过可调整的参数A,通过在浸没的倾斜板的两侧进行的空气诱导的液体再循环过程中边界层厚度的减小,传质的增加与湍流数和分子施密特数之间的差异相关。A.使用Launder-CFD进行CFD模拟与基于FLUENT增强壁函数的板取向(θ= 0〜({ring operator}),22。5〜({ring operator}的计算相比,斯伯丁壁函数(A = 1.08)与实验瞬态浓度曲线具有更好的一致性。 )和45〜({ring operator}))研究。板的下侧的固液传质高于上侧。特别地,倾斜板的传质系数高于垂直或水平取向,这暗示了该系统作为太阳能光反应器的应用具有额外的优势。

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