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Laminar natural convection in power-law liquids from a heated semi-circular cylinder with its flat side oriented downward

机译:加热后的半圆形圆柱体在幂律液体中的层流自然对流,其平面朝下

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In this work, laminar free convection heat transfer from a heated semi-circular cylinder, with its flat base facing downward, submerged in quiescent power-law fluids has been studied. The coupled momentum and energy equations have been solved numerically in the following ranges of dimensionless parameters: Grashof number (lO≤ Cr≤10~5), Prandtl number (0.72≤Pr≤100) and power-law index (0.2is contained in n is contained in 1.8). The detailed flow and temperature fields in the vicinity of the heated object are visualized in terms of the streamline and isotherm contours respectively. The rate of heat transfer is described in terms of the local Nusselt number variation along the surface of the cylinder together with its average value over the above-mentioned ranges of parameters. As expected, the value of the local Nusselt number increases from the front stagnation point up to the sharp corner and then decreases all the way up to the rear stagnation point. Broadly, over the range of conditions spanned here, the flow remains attached to the surface of the cylinder. The average Nusselt number increases with both the Crashof and Prandtl numbers and it decreases with the increasing power-law index. Furthermore, shear-thinning behavior (n < 1) enhances heat transfer whereas shear-thickening behavior (n > 1) impedes it with reference to that in Newtonian fluids otherwise under identical conditions. The numerical results obtained herein are correlated using a composite parameter consistent with the boundary layer analysis and these are contrasted with the results for the other two-dimensional shapes thereby suggesting the general usefulness of the composite parameter.
机译:在这项工作中,已经研究了从加热的半圆形圆柱体(其平底朝下)浸入静态幂律流体中的层流自由对流传热。已在以下无量纲参数范围内对动量和能量耦合方程进行了数值求解:Grashof数(lO≤Cr≤10〜5),Prandtl数(0.72≤Pr≤100)和幂律指数(0.2包含在n中包含在1.8中)。分别根据流线和等温线轮廓显示了加热对象附近的详细流场和温度场。根据沿着圆柱体表面的局部努塞尔数变化及其在上述参数范围内的平均值来描述传热速率。正如预期的那样,局部Nusselt值的值从前停滞点到尖角逐渐增加,然后一直下降到后停滞点。宽泛地讲,在这里所跨越的条件范围内,流量保持附着在气缸表面上。 Nusselt平均数随Crashof和Prandtl数的增加而增加,随幂律指数的增加而减小。此外,相对于牛顿流体,在相同条件下,剪切稀化行为(n <1)会增强传热,而剪切稀化行为(n> 1)会阻碍传热。本文获得的数值结果使用与边界层分析一致的复合参数进行关联,并且将这些结果与其他二维形状的结果进行对比,从而表明了复合参数的一般用途。

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