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THEORETICAL MODEL OF ELECTRIC FIELD EFFECTS ON THE ENHANCEMENT OF CRITICAL HEAT FLUX

机译:增强临界热通量的电场效应的理论模型

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Critical heat flux enhancement by the electrohydrodynamic(EHD) effect has been analyzed quantitatively based on the increased frequency of liquid-vapor interface oscillations around the edge of the bubble. The majority of heat transfer occurs when the liquid film thickness becomes less than 50 μm, which only occurs once per period. The main mechanism of heat flux enhancement induced by the EHD effect would be a result of an increase in surface tension due to the effect of electric lines of force. By representing the terms of the forces for a change in curvature and the surface tension resulting from the electric lines of force, the equation of the liquid-vapor instability was obtained and analyzed. Experimentally it has been shown that as the applied voltage increased, the periodic time interval of the thickness change was shortened. This effect reduces the potential for dryout of the liquid film by making the minimum thickness time period shorter. By measuring the pressure oscillation on the boiling surface, the change of the thin liquid film thickness and the dynamic shape of bubbles, the relationship among the pressure, the liquid film thickness and the bubble shape was clarified. Consequently, this model successfully explains the relationship between the applied voltage and the enhancement of the critical heat flux.
机译:基于流体动力学(EHD)效应的临界热通量增强已经基于气泡边缘周围液-气界面振荡频率的增加进行了定量分析。当液膜厚度小于50μm时发生大部分传热,每个周期仅发生一次。 EHD效应引起的热通量增强的主要机理可能是由于电力线的作用导致表面张力增加的结果。通过表示由电力线引起的曲率变化和表面张力变化的力的项,获得并分析了液体-蒸汽不稳定性方程。实验表明,随着施加电压的增加,厚度变化的周期性时间间隔缩短。通过缩短最短厚度时间,该效果降低了液膜变干的可能性。通过测量沸腾表面上的压力振荡,薄液膜厚度的变化和气泡的动态形状,阐明了压力,液膜厚度和气泡形状之间的关系。因此,该模型成功地说明了施加电压与临界热通量增强之间的关系。

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