首页> 外文会议>American Society of Mechanical Engineers(ASME) Summer Heat Transfer Conference(HT2005) vol.2; 20050717-22; San Francisco,CA(UA) >SIMULTANEOUS HEAT AND MASS TRANSFER DURING EVAPORATION/CONDENSATION ON THE SURFACE OF A STAGNANT DROPLET IN THE PRESENCE OF INERT ADMIXTURES CONTAINING NON-CONDENSABLE SOLVABLE GAS
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SIMULTANEOUS HEAT AND MASS TRANSFER DURING EVAPORATION/CONDENSATION ON THE SURFACE OF A STAGNANT DROPLET IN THE PRESENCE OF INERT ADMIXTURES CONTAINING NON-CONDENSABLE SOLVABLE GAS

机译:含有不可冷凝可燃气体的惰性添加剂存在时,在滞留液滴表面蒸发/冷凝时同时进行传热和传质

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In this study we investigated numerically simultaneous heat and mass transfer during evaporation/condensation on the surface of a stagnant droplet in the presence of inert admixtures containing non-condensable solvable gas. The performed analysis is pertinent to slow droplet evaporation/condensation when Mach number is small (M 1). The system of transient conjugate nonlinear energy and mass conservation equations was solved using anelastic approximation. Transport coefficients of the gaseous phase were calculated as functions of temperature and concentrations of gaseous species. Thermophysical properties of the liquid phase are assumed to be constant. Using the material balance at the droplet surface we obtained equations for Stefan velocity and the rate of change of the droplet radius taking into account the effect of solvable gas absorption at the gas-liquid interface. We derived also boundary conditions at gas-liquid interface taking into account the effect of gas absorption. The governing equations were solved using a method of lines. Numerical calculations showed essential change of the rates of heat and mass transfer in water droplet-air-water vapor system under the influence of solvable species in a gaseous phase. Consequently, the use of additives of solvable noncondensable gases to enhance the rate of heat and mass transfer in dispersed systems allows to increase the efficiency and reduce the size of gas-liquid contactors.
机译:在这项研究中,我们在含有不可凝可溶气体的惰性混合物存在下,在滞留液滴表面蒸发/凝结过程中同时进行了传热和传质的数值研究。当马赫数较小(M << 1)时,进行的分析与缓慢的液滴蒸发/凝结有关。使用非弹性近似法求解了瞬态共轭非线性能量和质量守恒方程组。计算气相的输送系数作为温度和气态物质浓度的函数。假定液相的热物理性质是恒定的。使用液滴表面的材料平衡,我们考虑了气液界面处可吸收气体的吸收作用,得出了Stefan速度和液滴半径变化率的方程式。考虑到气体吸收的影响,我们还导出了气液界面的边界条件。使用线的方法来求解控制方程。数值计算表明,在气相中可溶物的影响下,水滴-空气-水蒸气系统中的传热和传质速率发生了本质变化。因此,使用可溶解的非冷凝性气体的添加剂来提高分散系统中的传热和传质速率,可以提高效率并减小气液接触器的尺寸。

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