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Enhancement of Heat Transfer by an Electric Field for a Drop Translating at Intermediate Reynolds Number

机译:电场增强中雷诺数的液滴平移传热

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The enhancement of heat transfer by an electric field to a spherical droplet translating at intermediate Reynolds number is numerically investigated using a finite volume method. Two heat transfer limits are considered. The first limit is the external problem where the bulk of the resistance is assumed to be in the continuous phase. Results show that the external Nusselt number significantly increases with electric field strength at all Reynolds numbers. Also, the drag coefficient increases with electric field strength. The enhancement in heat transfer is higher with lower ratio of viscosity of the dispersed phase to the viscosity of the continuous phase. The second heat transfer limit is the internal problem where the bulk of the resistance is assumed to be in the dispersed phase. Results show that the steady state Nusselt number for a combined electrically induced and translational flow is substantially greater than that for purely translational flow. Furthermore, for a drop moving at intermediate Reynolds number, the maximum steady state Nusselt number for a combined electrically induced and translational flow is slightly greater than that for a purely electric field driven motion in a suspended drop.
机译:使用有限体积法对通过电场增强传热到中间雷诺数的球形液滴的传热进行了研究。考虑两个传热极限。第一个极限是外部问题,其中大部分电阻被假定为处于连续相。结果表明,在所有雷诺数下,外部努塞尔数均随电场强度而显着增加。而且,阻力系数随着电场强度而增加。分散相的粘度与连续相的粘度之比越低,传热的提高越高。第二热传递极限是内部问题,其中假定大部分电阻处于分散相。结果表明,电感应和平动相结合的稳态Nusselt数明显大于纯平动相。此外,对于以中间雷诺数运动的液滴,组合的电感应和平移流的最大稳态Nusselt数比悬浮液滴中纯电场驱动的运动的最大稳态努塞尔数略大。

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