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Non-newtonian flow and heat transfer in ducts with arbitrary cross-sectional geometry

机译:具有任意横截面几何形状的管道中的非牛顿流和热传递

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Constant property laminar flow of purely viscous Non-Newtonian fluids in ducts of non-circular cross-sectional geometry is considered. Fully developed friction factors are compared with our own experimental data. For engineering purposes the method, developed by Kozicki, Chou and Tiu (1966) reproduces the data with sufficient accuracy. For slender duct cross-sections with large width to height ratio, analytical approximations for prediction of fully developed friction factors, entrance region pressure drops and Nusselt numbers for a constant heat flux boundary condition are reported.
机译:考虑具有非圆形横截面几何形状的管道中的纯粘性非牛顿流体的恒定特性层流。将充分开发的摩擦系数与我们自己的实验数据进行比较。出于工程目的,由Kozicki,Chou和Tiu(1966)开发的方法以足够的精度重现了数据。对于宽高比大的细长风管横截面,报告了在恒定热通量边界条件下预测充分发展的摩擦系数,入口区域压降和Nusselt数的解析近似值。

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