Fei Suyu, Jiang Haitao, Hua Dan
Jiangsu Key Laboratory of Micro and Nano Heat Fluid Flow Technology and Energy Application, School of Environmental Science and Engineering, Suzhou University of Science and Technology, Suzhou, 215009, Jiangsu, China.
Sci Rep. 2024 Jan 23;14(1):1979. doi: 10.1038/s41598-024-52568-5.
To investigate the boiling characteristics of flow outside the R410A tube under swaying conditions, this article conducts numerical simulation and experimental research on the flow boiling heat transfer of R410A outside a horizontal tube. The results show that when the swing frequency increased from 0.2 to 2 Hz, the sway amplitude is 0.03 m, the heat flux on the inner wall of the runner remains unchanged, and the mass flow rate increases from 85 to 170 kg/(m·s), which makes the heat transfer coefficient of the working fluid in the annular area increases significantly. Keeping the inlet mass flow rate unchanged, the heat flux on the inner wall of the flow channel increases from 25 to 35 kW/m, the heat transfer coefficient of the working fluid in the annular area has also improved, but under high heat flux conditions, the working fluid is evaporated and dried, its heat transfer coefficient increases less than in low heat flux conditions. When the sway amplitude increases from 0.02 to 0.07 m, the sway frequency is 0.2 Hz and 2 Hz respectively, and the heat transfer coefficient of the working fluid shows a downward trend as a whole. The studies provide a reference for heat exchanger design suitable for offshore swaying conditions.
为研究R410A在摇摆条件下管外流动的沸腾特性,本文对水平管外R410A的流动沸腾传热进行了数值模拟和实验研究。结果表明,当摇摆频率从0.2Hz增加到2Hz,摇摆幅度为0.03m,流道内壁热流密度不变,质量流速从85kg/(m·s)增加到170kg/(m·s)时,环形区域内工质的传热系数显著增加。在入口质量流速不变的情况下,流道内壁热流密度从25kW/m增加到35kW/m,环形区域内工质的传热系数也有所提高,但在高热流密度条件下,工质发生蒸发干涸,其传热系数的增加幅度小于低热流密度条件。当摇摆幅度从0.02m增加到0.07m,摇摆频率分别为0.2Hz和2Hz时,工质的传热系数总体呈下降趋势。这些研究为适用于海上摇摆条件的换热器设计提供了参考。