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Numerical study on heat transfer enhancement in capsule-type plate heat exchangers

机译:胶囊式板式换热器传热强化的数值研究

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The capsule-type plate heat exchanger is proposed to address high viscosity fluid which has concave and convex ellipsoidal embossing similar to half capsules. In this paper, single-phase flow and heat transfer in a capsule-type plate channel are investigated numerically. Owing to the periodicity of the structure of the capsule-type plate channel, the heat transfers between the hot and cold fluid in a unit cell with periodic boundary conditions are modeled. Shear Stress Transport k-omega model is employed for turbulent flow. Streamlines, velocity and local convective heat transfer coefficient are presented for discussions. The heat transfer enhancement is found to be primarily attributed to the vortices, one of which has the unique butterfly-shaped head. The correlations of friction factor and Nusselt number in turbulent flow regime with Reynolds number from 500 to 12,470 are obtained based on the simulation results. Compared with other plate heat exchangers (e.g., chevron-type), the capsule-type plate heat exchanger has big Nusselt number, small friction factor f and a good performance with respect to Nuff(1/3). (C) 2016 Elsevier Ltd. All rights reserved.
机译:提出了胶囊型板式热交换器以解决具有类似于半胶囊的具有凹凸凸起的椭圆形压花的高粘度流体。本文对胶囊型平板通道中的单相流动和传热进行了数值研究。由于胶囊型板式通道结构的周期性,对具有周期性边界条件的晶胞中冷热流体之间的热传递进行了建模。剪切应力传递k-ω模型用于湍流。提出了流线,速度和局部对流传热系数进行讨论。发现传热的增强主要归因于涡旋,其中之一具有独特的蝴蝶形头部。根据仿真结果,获得了湍流状态下摩擦系数和努塞尔数与雷诺数在500至12470之间的相关性。与其他板式换热器(例如人字形)相比,胶囊式板式换热器的努塞尔数大,摩擦系数f小,相对于Nuff(1/3)性能良好。 (C)2016 Elsevier Ltd.保留所有权利。

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