Notwithstanding the widespread use of wind tunnel to investigate the performance of radiators and heat exchangers, has never been considered a numerical analysis of radiator inside the wind tunnel with complete three-dimensional geometry of tunnel. In the present study, three-dimensional numerical simulation of thermal performance of a car radiator inside a wind tunnel is performed to predict and improve the air fow behavior in a wind tunnel. The efect of the Reynolds number of air and the mass fow rate of hot water supply into the heat exchanger to preheat the air is investigated on heat transfer and fuid fow. Radiator, heat exchanger, honeycomb and fow straighteners in the difusers are defned as porous media due to their complex geometry. To solve this problem, the k − 휀 turbulence model with a high-resolution discretization was used along with the (RMS) convergence criterion. Moreover, the results of the present numerical analysis are compared with the performance results of a car radiator in a thermal wind tunnel and demonstrated that the results are in good agreement. It can be seen in the results that in formation of vortex and reverse fows, there are the test section and the corner of difusers. But the maximum variety of pressure, velocity and temperature is observed in the test section. The agitation is enhanced by increasing the Reynolds number and the diference between the size of radiator and test chamber. That can lead to undesired errors during the measurement process in experimental tests. In addition, the air non-dimensional temperature decreases by 30.1% and the air total pressure drop increases by 230 times by increasing the Reynolds number of air from 1e5 to 1.5e6 at a constant water mass fow rate of 8 kg s−1. Also, at Reynolds number of 1.5e6, air non-dimensional temperature decreases by 54.03% as the water mass fow rate changes from 18 to 4 kg s−1.
Three-dimensional numerical simulation of external fluid flow and heat transfer of a heat exchanger in a wind tunnel using porous media model / Moradi, Iman; Karimipour, Arash; Afrand, Masoud; Li, Z.; Bach, Quang-Vu. - In: JOURNAL OF THERMAL ANALYSIS AND CALORIMETRY. - ISSN 1388-6150. - 141:5(2020), pp. 1647-1667. [10.1007/s10973-020-10184-1]
Three-dimensional numerical simulation of external fluid flow and heat transfer of a heat exchanger in a wind tunnel using porous media model
Moradi, ImanPrimo
;Karimipour, Arash;Li, Z.;
2020
Abstract
Notwithstanding the widespread use of wind tunnel to investigate the performance of radiators and heat exchangers, has never been considered a numerical analysis of radiator inside the wind tunnel with complete three-dimensional geometry of tunnel. In the present study, three-dimensional numerical simulation of thermal performance of a car radiator inside a wind tunnel is performed to predict and improve the air fow behavior in a wind tunnel. The efect of the Reynolds number of air and the mass fow rate of hot water supply into the heat exchanger to preheat the air is investigated on heat transfer and fuid fow. Radiator, heat exchanger, honeycomb and fow straighteners in the difusers are defned as porous media due to their complex geometry. To solve this problem, the k − 휀 turbulence model with a high-resolution discretization was used along with the (RMS) convergence criterion. Moreover, the results of the present numerical analysis are compared with the performance results of a car radiator in a thermal wind tunnel and demonstrated that the results are in good agreement. It can be seen in the results that in formation of vortex and reverse fows, there are the test section and the corner of difusers. But the maximum variety of pressure, velocity and temperature is observed in the test section. The agitation is enhanced by increasing the Reynolds number and the diference between the size of radiator and test chamber. That can lead to undesired errors during the measurement process in experimental tests. In addition, the air non-dimensional temperature decreases by 30.1% and the air total pressure drop increases by 230 times by increasing the Reynolds number of air from 1e5 to 1.5e6 at a constant water mass fow rate of 8 kg s−1. Also, at Reynolds number of 1.5e6, air non-dimensional temperature decreases by 54.03% as the water mass fow rate changes from 18 to 4 kg s−1.File | Dimensione | Formato | |
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