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Effect of Schmidt number on mass transfer across a sheared gas-liquid interface in a wind-driven turbulence

机译:的施密特数对风力驱动湍流穿过剪切气 - 液界面物质转移的影响

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The mass transfer across a sheared gas-liquid interface strongly depends on the Schmidt number. Here we investigate the relationship between mass transfer coefficient on the liquid side, kL, and Schmidt number, Sc, in the wide range of 0.7?≤?Sc?≤?1000. We apply a three-dimensional semi direct numerical simulation (SEMI-DNS), in which the mass transfer is solved based on an approximated deconvolution model (ADM) scheme, to wind-driven turbulence with mass transfer across a sheared wind-driven wavy gas-liquid interface. In order to capture the deforming gas-liquid interface, an arbitrary Lagrangian-Eulerian (ALE) method is employed. Our results show that similar to the case for flat gas-liquid interfaces, kL for the wind-driven wavy gas-liquid interface is generally proportional to Sc(-0.5), and can be roughly estimated by the surface divergence model. This trend is endorsed by the fact that the mass transfer across the gas-liquid interface is controlled mainly by streamwise vortices on the liquid side even for the wind-driven turbulence under the conditions of low wind velocities without wave breaking.
机译:穿过剪切气液界面的传质强烈取决于施米特数。在这里,我们研究了液体侧,KL和施密特数,SC的质量传递系数之间的关系,在0.7Ω·≤β≤c≤≤≤x≤10。我们应用三维半直接数值模拟(半DNS),其中基于近似的解卷积模型(ADM)方案来求解传质,其在剪切风力驱动的波浪气体上具有大规模转移的风力驱动湍流 - 界面。为了捕获变形气液界面,采用任意拉格朗日 - 欧拉(ALE)方法。我们的结果表明,类似于平坦气液界面的情况,风力驱动的波浪气液界面的KL通常与SC(-0.5)成比例,并且可以通过表面发散模型大致估计。这种趋势是通过液体界面的传质转移来概念,即使在液体侧的流动涡流上的流动涡流,甚至对于在没有波浪的低风速条件下的风力驱动的湍流,也可以是液面上的流动涡流。

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