Sikora Małgorzata, Bohdal Tadeusz, Formela Karolina
Department of Energy, Koszalin University of Technology, ul. Racławicka 15-17, 75-620 Koszalin, Poland.
Materials (Basel). 2021 Nov 15;14(22):6886. doi: 10.3390/ma14226886.
This article presents the results obtained from our own experimental investigations on heat exchange and pressure drop during the condensation flow of the HFE 7000 refrigerant in pipe minichannels with an internal diameter of d = 1.2-2.5 mm. The influence of vapor quality x and the mass flux density G on the two-phase flow pressure drops and heat transfer is presented. The tests were performed for the mass flux density range of G = 110-4700 kg/ms, saturation inlet temperature of T = 36-43 °C and heat flux density of q = 1 ÷ 20 kW/m. The pressure drop characteristics and heat transfer coefficient as a function of the internal diameter of minichannels are illustrated. The results of experimental research on the heat transfer coefficient and two-phase pressure drop are compared with correlations developed by other authors. The best accuracy has a comparison of experimental study with correlation of Rahman-Kariya-Miyara et al. and Mikielewicz et al.
本文介绍了我们自己对内径d = 1.2 - 2.5 mm的微型管道中HFE 7000制冷剂冷凝流动过程中的热交换和压降进行实验研究所得的结果。文中给出了蒸汽干度x和质量通量密度G对两相流压降及传热的影响。测试是在质量通量密度G = 110 - 4700 kg/ms、饱和入口温度T = 36 - 43 °C以及热通量密度q = 1÷20 kW/m的范围内进行的。阐述了压降特性和传热系数随微型管道内径的变化情况。将传热系数和两相压降的实验研究结果与其他作者提出的关联式进行了比较。与拉赫曼 - 卡里亚 - 宫良等人以及米基莱维茨等人的关联式相比,实验研究与之比较时具有最佳的准确性。