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Developing and Fully Developed Non-Newtonian Fluid Flow and Heat Transfer Through Concentric Annuli

机译:通过同心圆环开发和充分开发非牛顿流体流动和传热

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摘要

Developing and fully developed laminar flows of power law fluid with forced convection heat transfer through a concentric annular duct are numerically analyzed. The results are presented for the following ranges: 0.2≤n≤1.8 (power law index), 10≤Re≤1000 (Reynolds number), and r =0.2, 0.5, 0.8 (aspect ratio). In addition, the influences of different thermal boundary conditions on the thermal performance are delineated. The effects of rheological parameter on the developing length, friction factor, temperature distribution, velocity profile, and Nusselt number along the channel length are investigated. The results are compared with earlier research and excellent agreement was observed.
机译:对通过同心环形管道进行强制对流换热的幂律流体的层流进行了开发和充分开发。结果在以下范围内显示:0.2≤n≤1.8(幂律指数),10≤Re≤1000(雷诺数)和r = 0.2、0.5、0.8(纵横比)。此外,还描述了不同热边界条件对热性能的影响。研究了流变参数对沿通道长度的显影长度,摩擦系数,温度分布,速度分布和Nusselt数的影响。将结果与早期研究进行比较,观察到了极好的一致性。

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