In this study,a new and effective improved Semi-Analytic and Semi-Empirical formula f(Pr)= (0.749999437Pr^(1/2))/((0.609+1.221Pr^(1/2)+1.238Pr)^(1/4))has been proposed to solve a conjugate problem with free convection...In this study,a new and effective improved Semi-Analytic and Semi-Empirical formula f(Pr)= (0.749999437Pr^(1/2))/((0.609+1.221Pr^(1/2)+1.238Pr)^(1/4))has been proposed to solve a conjugate problem with free convection in the incompressible laminar boundary layer flow and heat conduction in a solid wall for the flow passing a flat plate fin. A combination of flat-plate flow and flat-plate fin heat conduction has been considered in the present study.Finite -difference solutions for the interface temperature profiles and the heat transfer rates have been presented over the entire thermo-fluid-dynamic field for Prandtl numbers from 0.001 to 10000.First,the similar flow field has been solved by the Runge-Kutta method and the shooting methods,then the correlation equation of the local heat transfer coefficient have been obtained.Finally,the empirical formula has been substituted into the fin temperature heat conduction calculation processes to obtain the iterative solutions of the conjugate problems.展开更多
为改进大功率电子设备冷却系统,对竖直五边形肋柱通道进行了氟碳工质过冷沸腾实验,热流密度、进口流速、过冷度分别为50~400 k W·m^(-2)、0.1~0.9 m·s^(-1)、14~29℃。研究发现:随着热流密度的增大,平均传热系数和压降总体上...为改进大功率电子设备冷却系统,对竖直五边形肋柱通道进行了氟碳工质过冷沸腾实验,热流密度、进口流速、过冷度分别为50~400 k W·m^(-2)、0.1~0.9 m·s^(-1)、14~29℃。研究发现:随着热流密度的增大,平均传热系数和压降总体上增大,传热因子在进口流速大于0.5 m·s^(-1)时增大;随着进口流速的增大,平均传热系数在中高热流密度下先减小后增大,传热因子均减小;随着过冷度的增大,加热壁面均温总体上降低,平均传热系数均减小,传热因子在进口流速大于0.5 m·s^(-1)时减小。展开更多
基金National Science Council for the financial support through Grant.NSC 98-2221-E-434-009-
文摘In this study,a new and effective improved Semi-Analytic and Semi-Empirical formula f(Pr)= (0.749999437Pr^(1/2))/((0.609+1.221Pr^(1/2)+1.238Pr)^(1/4))has been proposed to solve a conjugate problem with free convection in the incompressible laminar boundary layer flow and heat conduction in a solid wall for the flow passing a flat plate fin. A combination of flat-plate flow and flat-plate fin heat conduction has been considered in the present study.Finite -difference solutions for the interface temperature profiles and the heat transfer rates have been presented over the entire thermo-fluid-dynamic field for Prandtl numbers from 0.001 to 10000.First,the similar flow field has been solved by the Runge-Kutta method and the shooting methods,then the correlation equation of the local heat transfer coefficient have been obtained.Finally,the empirical formula has been substituted into the fin temperature heat conduction calculation processes to obtain the iterative solutions of the conjugate problems.
