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Laminar flow heat transfer in concentric equilateral triangular annular channels

机译:同心等边三角形环形通道中的层流传热

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The problem of laminar flow heat transfer in channels of annular cross section formed by concentric equilateral triangles is studied.Numerical solutions for friction factor,and magnitude of minimum limiting Nusselt numbers for both constant heat input per unit length and constant wall temperature are obtained.The results obtained by the numerical method are compared with the available solutions for the limiting geometries of equilateral triangle and parallel plates.Experimental data for isothermal pressure drop and constant wall temperature boundary condition at the outer wall are presented.Test sections with length to equivalent diameter ratios of 13.85,15.12 and 20.8 are employed in the present investigation.The Prandtl numbers are varied from 4 to 65 applying Glycerol-water mixture as coolant.Empirical correlations for isothermal friction factor and Nusselt number for constant wall temperature boundary conditions are presented.
机译:研究了同心等边三角形形成的环形截面通道内的层流传热问题。获得了摩擦因数的数值解,以及单位长度恒定热量输入和恒定壁温的最小极限努塞尔数的大小。将数值方法获得的结果与等边三角形和平行板的极限几何的可用解决方案进行了比较。给出了等温压降和外壁恒定壁温边界条件的实验数据。在本研究中采用了13.85、15.12和20.8的数值。以甘油-水混合物为冷却剂时的Prandtl值在4到65之间变化。给出了恒定壁温边界条件下等温摩擦系数和Nusselt值的经验相关性。

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