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Numerical investigation of heat transfer to a non-spherical drop suspended in an electric field: internal problem

机译:传热到悬浮在电场中的非球形液滴的数值研究:内部问题

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Heat transfer to a drop of a dielectric fluid suspended in another dielectric fluid in the presence of an electric field is numerically investigated. The internal heat transfer problem is considered where the bulk of the resistance to the heat transfer is assumed to be in the dispersed phase. We have analyzed the effect of drop deformation on the heat transport to the drop. The deformed drop shape is assumed to be a spheroid and is prescribed in terms of the ratio of drop major and minor diameter. Both prolate and oblate shapes are considered with a range of diameter ratio b/a from 2.0 to 0.5. The electrical field and the induced stresses are obtained analytically. The resulting flow field is determined by numerically solving the Navier-Stokes equations in the continuous and the dispersed phase. An alternating-direction-implicit (ADI) method is used to obtain the transient temperature field for drop Peclet number from 5 to 1500. Heat transfer results for a nearly spherical drop (b/a chemical bounds 0.99 and b/a chemical bounds 1.01) show excellent agreement with the results available in published literature. Results indicate that the drop shape significantly affects the flow field and the heat transport to the drop. At very low and very high Peclet numbers, the steady state Nusselt number is higher for a deformed drop than that for a sphere. However, at intermediate Peclet number, the Nusselt number for a sphere may be higher than that for a deformed drop. For both prolate and oblate drops, the steady state Nusselt number increases with increasing Peclet number, and at high Peclet number, becomes increasingly independent of the Peclet number. The maximum steady state Nusselt numbers for an oblate drop are higher than that for a prolate drop.
机译:对存在电场的情况下,热传递到悬浮在另一种介电液中的一滴介电液进行了数值研究。考虑内部传热问题,其中大部分传热阻力假定为分散相。我们分析了液滴变形对液滴传热的影响。假定变形的液滴形状是球体,并且是根据液滴的直径与直径之比来规定的。扁圆形和扁圆形均被认为具有2.0 / 0.5的直径比b / a。通过分析获得电场和感应应力。通过在连续相和分散相中数值求解Navier-Stokes方程来确定最终的流场。交替方向隐式(ADI)方法用于获得液滴Peclet数从5到1500的瞬态温度场。传热的结果是接近球形的液滴(b / a化学界为0.99,b / a化学界为1.01)与已发表的文献中的结果非常吻合。结果表明,液滴的形状显着影响流场和向液滴的热传递。在非常低的Peclet数和非常高的Peclet数下,变形液滴的稳态Nusselt数高于球体的稳态Nusselt数。但是,在中间Peclet数时,球的Nusselt数可能会高于变形液滴的Nusselt数。对于扁长滴和扁滴滴,稳态努塞尔数均随Peclet数的增加而增加,而在高Peclet数下,其状态逐渐变得独立于Peclet数。扁圆状液滴的最大稳态努塞尔数高于扁圆状液滴的最大稳态努塞尔数。

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