波浪通道内涡发生器强化传热:CFD研究

Q1 Chemical Engineering
Aimen Tanougast, Krisztián Hriczó
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引用次数: 0

摘要

波纹通道是一种广泛使用的增强传热的方法,已被用于许多热工应用,如热交换器和紧凑的冷却系统。波纹段产生再循环区,这可以影响流动效率。因此,我们引入了涡流发生器。本文对雷诺数(Re)为500-5000的波纹状波纹通道内的对流换热进行了数值研究。在这种配置下,波浪通道配备了两种类型的涡发生器(VGs),呈现了一种新的设置,在现有的研究中没有涉及到:不同直径的全圆涡发生器(fcvg) (D = 2,4和6mm),以及两个半圆涡发生器(thcvg),两半之间的距离可变(S = 1,2和3mm)。在ANSYS Fluent中采用有限体积法进行数值模拟,高雷诺数流动采用SST k -ω湍流模型。VGs通常可以改善传热。使用压降比(PR)和增强百分比(PE)来衡量性能。为了评估热液性能,还计算了性能因子(PF),结果表明,在Re=500时,ffcvg配置(D = 6 mm)在层流中达到了最佳平衡,最大PF为0.94,而较小的ffcvg在湍流状态下的表现优于thcvg。fcvg (D = 6 mm)的PE最大,在Re=1000时增加了46%,而thvg (S =1 mm)在Re=500时增加了38%。然而,由于fcv的PR值比thcv的PR值上升得更快,因此这种增强是以压降为代价的。这样的改进使热交换器设计更加紧凑和高效,支持节能和系统小型化。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Enhanced heat transfer in wavy channels with vortex generators: A CFD investigation
The corrugated channel is a widely used method for enhancing heat transfer and has been employed in many thermal engineering applications, such as heat exchangers and compact cooling systems. The corrugated sections create recirculation zones, which can impact flow efficiency. For that reason, we introduced vortex generators. In this study, numerical investigations were conducted on convective heat transfer in a wavy corrugated channel within a Reynolds number (Re) range of 500–5000. The wavy channel was equipped with two types of vortex generators (VGs) in this configuration, presenting a novel setup not previously addressed in existing studies: full-circle vortex generators (FCVGs) with different diameters (D = 2, 4, and 6 mm), and two-half-circle vortex generators (THCVGs) with variable distances between the halves (S = 1, 2, and 3 mm). The numerical simulations were performed using the finite volume method in ANSYS Fluent, with the SST kω turbulence model employed for high Reynolds number flows. The VGs generally improve heat transfer. Performance is measured using the pressure drop ratio (PR) and the percentage enhancement (PE). To evaluate thermo-hydraulic performance, the Performance Factor (PF) was also calculated, showing that the FCVG configuration (D = 6 mm) achieved the best balance in laminar flow with a maximum PF of 0.94 at Re=500, while smaller FCVGs performed better in the turbulent regime compared to THCVGs. FCVGs (D = 6 mm) had the largest PE, increasing by 46% at Re=1000, whereas THCVGs (S = 1 mm) increased by 38% at Re=500. However, because PR values can rise more for FCVGs than for THCVGs, this enhancement comes at a pressure drop cost. Such improvements enable more compact and efficient heat exchanger designs, supporting energy savings and system miniaturization.
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来源期刊
International Journal of Thermofluids
International Journal of Thermofluids Engineering-Mechanical Engineering
CiteScore
10.10
自引率
0.00%
发文量
111
审稿时长
66 days
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