Heat transfer analysis of nanofluid flow with entropy generation in a corrugated heat exchanger channel partially filled with porous medium

IF 2.8 Q2 THERMODYNAMICS Heat Transfer Pub Date : 2024-08-19 DOI:10.1002/htj.23149
A. Mezaache, F. Mebarek-Oudina, H. Vaidya, Y. Fouad
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Abstract

Heat exchanger research is mainly exploited to develop and optimize new engineering systems with high thermal efficiency. Passive methods based on nanofluids, fins, wavy walls, and the porous medium are the most attractive ways to achieve this goal. This investigation focuses on heat transfer and entropy production in a nanofluid laminar flow inside a plate corrugated channel (PCC). The channel geometry comprises three sections, partially filled with a porous layer located at the intermediate corrugate channel section. The physical modeling is based on the laminar, two-dimensional Darcy–Brinkman–Forchheimer formulation for nanofluid flow and the local thermal equilibrium model for the heat equation, including the viscous dissipation term. Numerical solutions were obtained using ANSYS Fluent software based on the finite volume technique and the appropriate meshed geometries. The numerical results are validated with theoretical, numerical, and experimental studies. The simulations are performed for CuO–water nanofluid and AISI 304 porous medium. The coupled effects of porous layer thickness (δ), Reynolds number (Re), and nanoparticle fraction (φ) on velocity, streamlines, isotherm contours, Nusselt number (Nu), and entropy generation (S) are analyzed and illustrated. The simulation results demonstrate that heat transfer enhancement in clear PCC can be achieved using a porous layer insert. For the porous thickness range of [0.1–0.6], the corresponding range of average Nusselt number increase is [35.7%–176.9%], and the average entropy generation is [105.4%–771.9%]. The effect of the Reynolds number is more important in a porous duct than in a clear one. For δ = 0.4 and φ = 5%, the increase of Re in the range of [200–500] induces an increase in average Nusselt number in the range of [80.9%–108.4%] and average entropy in [222.9%–309.1%] comparatively to clear PCC. The effect of φ is practically the same for porous and clear channels. For φ = 5%, the increase on average Nu is about 9%, and entropy generation is 5%. Accordingly, important improvements in heat transfer in PCC can be achieved through the combined effect of flow Reynolds number and porous layer thickness.

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部分填充多孔介质的波纹状热交换器通道中产生熵的纳米流体流动的传热分析
热交换器研究主要用于开发和优化具有高热效率的新型工程系统。基于纳米流体、翅片、波浪壁和多孔介质的被动方法是实现这一目标的最有吸引力的途径。本研究的重点是板状波纹通道(PCC)内纳米流体层流中的热传递和熵产生。通道的几何形状由三个部分组成,中间的波纹通道部分填充了多孔层。物理建模基于纳米流体流动的层流二维达西-布林克曼-福克海默公式和热方程的局部热平衡模型,包括粘性耗散项。利用 ANSYS Fluent 软件,基于有限体积技术和适当的网格几何结构,获得了数值解决方案。数值结果与理论、数值和实验研究进行了验证。模拟针对的是 CuO-水纳米流体和 AISI 304 多孔介质。分析并说明了多孔层厚度 (δ)、雷诺数 (Re) 和纳米粒子分数 (φ) 对速度、流线、等温线、努塞尔特数 (Nu) 和熵生成 (S) 的耦合效应。模拟结果表明,使用多孔层插入物可以增强透明 PCC 的传热效果。多孔层厚度范围为[0.1-0.6]时,相应的平均努塞尔特数增加范围为[35.7%-176.9%],平均熵生成量为[105.4%-771.9%]。雷诺数的影响在多孔管道中比在透明管道中更为重要。在 δ = 0.4 和 φ = 5%的情况下,Re 在[200-500]范围内的增加导致平均努塞尔特数在[80.9%-108.4%]范围内增加,平均熵在[222.9%-309.1%]范围内增加。φ对多孔和透明通道的影响基本相同。当 φ = 5%时,平均 Nu 增加约 9%,熵增加 5%。因此,通过流动雷诺数和多孔层厚度的共同作用,可以显著改善 PCC 的传热效果。
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来源期刊
Heat Transfer
Heat Transfer THERMODYNAMICS-
CiteScore
6.30
自引率
19.40%
发文量
342
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