Affiliation:
1. University of Shanghai for Science and Technology School of Energy and Power Engineering, , Shanghai 200093 , China
2. University of Shanghai for Science and Technology School of Energy and Power Engineering; Shanghai Key Laboratory of Multiphase Flow and Heat Transfer in Power and Engineering, , Shanghai 200093 , China
Abstract
Abstract
It is widely acknowledged that the pressure drop increases with enhanced heat transfer in heat exchanger tubes, and entropy generation analysis serves as an effective method to comprehensively evaluate heat transfer and pressure drops. This paper conducts experimental research on in-tube condensation heat transfer using refrigerants R513A and R134a in six test tubes, comprising both smooth and microfin tubes with outer diameters of 9.52 mm and 12.7 mm, respectively. The microfin tubes are available in two types, with 60 and 65 fins, respectively, and a helix angle of 18 deg. The experimental conditions included mass fluxes of 50–250 kg/m2 s and condensation temperatures of 35 °C, 38 °C, and 40 °C. The findings indicate that replacing R134a with R513A is feasible. The 9.52 mm tube exhibits superior overall heat transfer performance compared to the 12.7 mm tube, and the 60-fin microfin tube outperforms the 65-fin tube in terms of heat transfer efficiency. This suggests that microfin tubes with smaller diameters and an optimal number of fins are more effective in enhancing condensation heat transfer performance.