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首页> 外文期刊>International communications in heat and mass transfer >Numerical study on bubble-liquid two-phase turbulent hydrodynamics in extremely narrow shape bioreactor
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Numerical study on bubble-liquid two-phase turbulent hydrodynamics in extremely narrow shape bioreactor

机译:极窄形状生物反应器中气液两相湍流动力学的数值研究

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The main objective of this work was to determine the influence of the bubble-liquid two-phase turbulent hydrodynamics on cell culture in extremely narrow shape bioreactor. An improved second-order moment bubble-liquid turbulent model and built in-house calculation source code were developed to numerically simulate the hydrodynamics that related to cell damage. Two higher gas entrance velocities of 78.3 m/s and 104.4 m/s were employed and their effects on hydrodynamic parameters, such as bubble rising and liquid flow velocities, bubble normal and shear stresses, correlation of bubble-liquid normal stresses, turbulent kinetic energy and turbulent energy dissipation rate of bubble and liquid were investigated details. All increased with gas entrance velocities increase but failed to explain an experimental observation that higher cell death at jetting region. A new correlation definition, bubbleliquid two-phase turbulent energy production term was proposed to successfully elaborate it, as well as the effects of high gas entrance velocities. Simulation results showed turbulent energy production terms are the largest at near gas jetting regions in comparison to those of developed flow regions, which are in good agreements with experimental result. Furthermore, extremely narrow shape deteriorated the cell living environment.
机译:这项工作的主要目的是确定气泡-液体两相湍流流体动力学对极其狭窄形状的生物反应器中细胞培养的影响。开发了改进的二阶矩气泡-液体湍流模型和内置的内部计算源代码,以数值模拟与细胞损伤有关的流体动力学。使用了两个较高的气体入口速度,分别为78.3 m / s和104.4 m / s,它们对流体力学参数的影响,例如气泡上升和液体流速,气泡正向和剪切应力,气泡-液体正向应力的相关性,湍动能详细研究了气泡和液体的湍流能量耗散率。所有这些都随着气体入口速度的增加而增加,但是未能解释实验观察到喷射区域较高的细胞死亡。提出了一个新的相关定义,即气泡液体两相湍流能量产生项,并成功地阐述了它,以及高气体入口速度的影响。仿真结果表明,与发达的流动区域相比,湍流能量产生项在近气体喷射区域最大,与实验结果吻合良好。此外,极窄的形状恶化了细胞的生存环境。

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