首页> 外文会议>ASME microanoscale heat and mass transfer international conference;MNHMT2009 >A SCALE ANALYSIS BASED THEORETICAL FORCE BALANCE MODEL FOR CRITICAL HEAT FLUX (CHF) DURING SATURATED FLOW BOILING IN MICROCHANNELS AND MINICHANNELS
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A SCALE ANALYSIS BASED THEORETICAL FORCE BALANCE MODEL FOR CRITICAL HEAT FLUX (CHF) DURING SATURATED FLOW BOILING IN MICROCHANNELS AND MINICHANNELS

机译:基于尺度分析的微通道和微通道饱和流沸腾过程中临界热通量(CHF)的理论力平衡模型

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Accurate prediction of critical heat flux (CHF) in microchannels and small diameter tubes is of great interest in estimating the safe operational limits of cooling systems employing flow boiling. Scale analysis is applied to identify the relevant forces leading to the CHF condition. Using these forces, a local parameter model is developed to predict the flow boiling CHF. The theoretical model is an extension of an earlier pool boiling CHF model incorporating a force balance among the evaporation momentum, surface tension, inertia, and viscous forces. Weber number, capillary number, and a new non-dimensional group K_2, representing the ratio of evaporation momentum to surface tension forces, emerged as main groups in quantifying the narrow channel effects on CHF. The constants in the model were calculated from the available experimental data. The mean error with ten data sets is 19.7 percent, with 76 percent data falling within ±30% error band, and 93 percent within ±50% error band. Evaluating individualized set of constants for each data set resulted in mean errors of less than 10 percent for all data sets. The success of the model indicates that flow boiling CHF can be modeled as a local phenomenon and the scale analysis is able to reveal important information regarding fundamental mechanisms leading to the CHF condition. The final equations resulting from this model are given by Eqs. (18-22) along with the transition criteria given by Eq. (28).
机译:准确预测微通道和小直径管中的临界热通量(CHF),对于估算采用流动沸腾的冷却系统的安全运行极限具有重大意义。应用量表分析来识别导致CHF病状的相关力。利用这些力,开发了局部参数模型来预测沸腾CHF的流量。该理论模型是对早期池沸腾CHF模型的扩展,该模型结合了蒸发动量,表面张力,惯性和粘性力之间的力平衡。韦伯数,毛细管数和代表蒸发动量与表面张力的比例的新无量纲K_2成为量化CHF的窄通道效应的主要基团。从可用的实验数据中计算出模型中的常数。十个数据集的平均误差为19.7%,其中76%的数据在±30%误差带内,而93%的数据在±50%误差带内。对每个数据集评估单独的常量集会导致所有数据集的平均误差小于10%。该模型的成功表明,沸腾CHF可以建模为局部现象,并且规模分析能够揭示有关导致CHF状况的基本机制的重要信息。由该模型得出的最终方程由方程式给出。 (18-22)以及等式给出的转换标准。 (28)。

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