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Numerical Simulation of Heat Transfer Enhancement in Laminar Flow of Viscoelastic Fluids through a Rectangular Channel

机译:矩形通道中粘弹性流体层流动热传递增强的数值模拟

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A finite-volume method is applied to the three-dimensional simulation of heat transfer of a viscoelastic fluid in laminar flow through a rectangular channel with an aspect ratio of 2 and constant heat flux at the channel walls. The objectives of the present work are twofold: (a) to compare the numerical results with the heat transfer experimental data of Hartnett and Kostic [l]; (b) to analyze the influence of the secondary flow on the heat transfer enhancement on account of the non-zero second normal-stress difference. The rheology of the viscoelastic fluid is represented by the Phan-Thien-Tanner constitutive equation with non-zero second normal-stress difference. The simulations show the strong effect of secondary flows on the correct prediction of experimental results. The predictions confirm the enhancement of local and mean Nusselt numbers, as found experimentally by Hartnett and Kostic [1], and show that free convection has a major influence in the experimental heat transfer results for Newtonian fluid, but less so as fluid elasticity is increased.
机译:的有限体积法是通过为2的纵横比和恒定的热通量在所述通道壁的矩形通道适用于层流的粘弹性液体的热传递的三维模拟。本工作的目的是双重的:(a)中以比较和哈特尼特科斯蒂奇[1]的热传递实验数据的数值计算结果; (b)分析在帐户中的非零第二正常应力差对传热促进二次流动的影响。粘弹性流体的流变性是由具有非零第二法向应力差的藩噻吩唐纳构方程表示。仿真结果表明二次流对实验结果的正确预测的强烈的影响。预测确认本地和平均努塞尔数的提高,如通过哈特尼特和科斯蒂奇[1]实验发现,并表明,自由对流具有对于牛顿流体实验传热结果有重大影响,但更小,流体弹性增加。

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