Flow condensation heat transfer of propane refrigerant inside a horizontal micro-fin tube

Quang Vu Pham1, Jong-Taek Oh2
1Faculty of Energy Technology Electric Power University, Hanoi, Vietnam
2Department of Refrigeration and Air-Conditioning Engineering, Chonnam National University, Yeosu, Republic of Korea

Tóm tắt

Due to the phase-out of CFCs and HCFC refrigerants, propane is a nature refrigerant occurring substance produced by natural gas production and oil refining. As a result, propane has a higher latent heat and lower density than conventional refrigerants while maintaining a comparable saturation pressure and thermal conductivity. So, propane refrigerant is already widely used in domestic fridges and freezers for many years. However, propane’s operating pressures and temperatures are well suited for air conditioning equipment, including chillers. This study investigates the contributions of different heat transfer mechanisms in two-phase flow condensation heat transfer coefficients for propane inside a 6.3-mm ID micro-fin copper tube. Data were collected through an experiment with a two-phase flow condensation. Measurements were taken at different refrigerant mass fluxes from 100 to 300 kg/m2s and heat fluxes from 3 to 9 kW/m2. In addition, the experiments investigated effect of vapor quality, mass flux, and heat flux on the heat transfer coefficients. Finally, a new heat transfer coefficient correlation was developed based on the experimental data with good agreement.

Tài liệu tham khảo

Kim, N.-H. (2016). Condensation of R-134a on horizontal enhanced tubes having three-dimensional roughness. International Journal of Air-Conditioning and Refrigeration, 24, 1650013. Islam, M. A., & Miyara, A. (2007). Liquid film and droplet flow behaviour and heat transfer characteristics of herringbone microfin tubes. International Journal of Refrigeration, 30, 1408–1416. Wijaya, H. (1994). Two-phase flow condensation heat transfer and pressure drop characteristics of HCFC-22 and AZ-20. In International refrigeration and air conditioning conference at Purdue (pp. 305–310). Hossain, M. A., Onaka, Y., & Miyara, A. (2012). Experimental study on condensation heat transfer and pressure drop in horizontal smooth tube for R1234ze(E), R32 and R410A. International Journal of Refrigeration, 35, 927–938. López-Belchí, A. (2019). Assessment of a mini-channel condenser at high ambient temperatures based on experimental measurements working with R134a, R513A and R1234yf. Applied Thermal Engineering, 155, 341–353. Guo, Z., & Anand, N. K. (2000). An analytical model to predict condensation of R-410A in a horizontal rectangular channel. Journal of Heat Transfer, 122, 613. Zhang, J., Zhou, N., Li, W., Luo, Y., & Li, S. (2018). An experimental study of R410A condensation heat transfer and pressure drops characteristics in microfin and smooth tubes with 5 mm OD. International Journal of Heat and Mass Transfer, 125, 1284–1295. Wen, M.-Y., Ho, C.-Y., & Hsieh, J.-M. (2006). Condensation heat transfer and pressure drop characteristics of R-290 (propane), R-600 (butane), and a mixture of R-290/R-600 in the serpentine small-tube bank. Applied Thermal Engineering, 26, 2045–2053. Del Col, D., Torresin, D., & Cavallini, A. (2010). Heat transfer and pressure drop during condensation of the low GWP refrigerant R1234yf. International Journal of Refrigeration, 33, 1307–1318. Cavallini, A., et al. (2006). Condensation in horizontal smooth tubes: a new heat transfer model for heat exchanger design. Heat Transfer Engineering, 27, 31–38. Kedzierski, M. A., & Kim, M. S. (1998). Convective boiling and condensation heat transfer with a twisted-tape insert for R12, R22, R152a, R134a, R290, R32/R134a, R32/R152a, R290/R134a, R134a/R600a. Thermal Science and Engineering, 06, 113–122. Taitel, Y., & Dukler, A. E. (1976). A model for predicting flow regime transitions in horizontal and near horizontal gas-liquid flow. AIChE Journal, 22, 47–55. El Hajal, J., Thome, J. R., & Cavallini, A. (2003). Condensation in horizontal tubes, part 1: two-phase flow pattern map. International Journal of Heat and Mass Transfer, 46, 3349–3363. Jung, D., Song, K. H., Cho, Y., & Kim, S. J. (2003). Flow condensation heat transfer coefficients of pure refrigerants. International Journal of Refrigeration, 26, 4–11. Byun, H.-W., Lee, E.-J., Sim, Y.-S., Lee, J.-K., & Kim, N.-H. (2013). Condensation heat transfer and pressure drop of R-410a in a 5.0 Mm O.D. Smooth and Microfin Tube. International Journal of Air-Conditioning and Refrigeration, 21, 1350018. Bivens, D. B., & Yokozeki, A. (1994). Heat transfer coefficients and transport properties for alternative refrigerants. Proceeding International Refrigeration and Air Conditioning Conference, 299–304 Kedzierski, M. A., & Goncalves, J. M. (1999). Horizontal convective condensation of alternative refrigerants within a micro-fin tube. Journal of Enhanced Heat Transfer, 6, 161–178. Shah, R. K., & London, A. L. (1972). Flow forced convection heat transfer and flow friction in straight and curved ducts - a summary of analytical solutions (Vol. 1, p. 311).