Flow condensation of R-410A in multiport tubes having smooth or micro-finned internal channels

References

• C. Y. Yang and R. L. Webb, “Condensation of R-12 in small hydraulic diameter extruded aluminum tubes with and without micro-fins,” Int. J. Heat Mass Trans., vol. 39, no. 4, pp.791–800, 1996. DOI: https://doi.org/10.1016/0017-9310(95)00150-6.
   Web of Science ®Google Scholar
• R. L. Webb and C. Y. Yang, “A Comparison of R-12 and R-134a Condensation Inside Small Extruded Aluminum Plain and Microfin Tubes,” IMechE, vol. C4961053195, pp. 77–86, 1995.
   Google Scholar
• C. Y. Yang and R. L. Webb, “A predictive model for condensation in small hydraulic diameter tubes having axial microfins,” J. Heat Trans., vol. 119, no. 4, pp.776–782, 1997. DOI: https://doi.org/10.1115/1.2824182.
   Web of Science ®Google Scholar
• M. Zhang and R. L. Webb, “Correlation of two-phase friction for refrigerants in small-diameter tubes,” Exp. Thermal Fluid. Sci., vol. 25, no. 3–4, pp.131–139, 2001. DOI: https://doi.org/10.1016/S0894-1777(01)00066-8.
   Web of Science ®Google Scholar
• -W.-W.-W. Wang, T. D. Radcliff, and R. N. Christensen, “A condensation heat transfer correlation for millimeter-scale tubing with flow regime transition,” Exp. Thermal Fluid Sci., vol. 26, no. 5, pp.473–485, 2002. DOI: https://doi.org/10.1016/S0894-1777(02)00162-0.
   Web of Science ®Google Scholar
• C. Y. Yang and R. L. Webb, “Frictional pressure drop of R-12 in small hydraulic diameter extruded aluminum tubes with and without microfins,” Int. J. Heat Mass Trans., vol. 39, no. 4, pp.801–809, 1996. DOI: https://doi.org/10.1016/0017-9310(95)00151-4.
   Web of Science ®Google Scholar
• N. H. Kim, J. P. Cho, and B. Youn, “Condensation of R-22 and R-410A in flat aluminum extruded tubes,” Int. J. Refrig., vol. 26, pp. 830–839, 2003. DOI: https://doi.org/10.1016/S0140-7007(03)00049-5.
   Web of Science ®Google Scholar
• R. L. Webb and K. Ermis, “Effect of hydraulic diameter on condensation of R-134A in flat, extruded aluminum tubes,” J. Enhanc. Heat Trans., vol. 8, no. 2, pp.77–90, 2001. DOI: https://doi.org/10.1615/JEnhHeatTransf.v8.i2.20.
   Web of Science ®Google Scholar
• S. Koyama, K. Kuwahara, K. Nakashita, and K. Yamamoto, “An experimental study on condensation of refrigerant R134a in a multi-port extruded tube,” Int. J. Refrig., vol. 26, no. 4, pp.425–432, 2003. DOI: https://doi.org/10.1016/S0140-7007(02)00155-X.
   Web of Science ®Google Scholar
• A. Cavallini, et al., “Condensation heat transfer and pressure gradient inside multiport minichannels,” Heat Transf. Eng., vol. 26, no. 3, pp.45–55, 2005. DOI: https://doi.org/10.1080/01457630590907194.
   Web of Science ®Google Scholar
• T. M. Bandhauer, A. Agarwal, and S. Garimella, “Measurement and modeling of condensation heat transfer coefficients in circular microchannels,” J. Heat Trans., vol. 128, no. 10, pp.1050–1059, 2006. DOI: https://doi.org/10.1115/1.2345427.
   Web of Science ®Google Scholar
• A. Agarwal, T. M. Bandhauer, and S. Garimella, “Measurement and modeling of condensation heat transfer in non-circular microchannels,” Int. J. Refrig., vol. 33, no. 6, pp.1169–1179, 2010. DOI: https://doi.org/10.1016/j.ijrefrig.2009.12.033.
   Web of Science ®Google Scholar
• J. E. Park, F. Vakili-Farahani, L. Consilini, and J. R. Thome, “Experimental study on condensation heat transfer in vertical minichannels for new refrigerant R1234ze(E) versus R134a and R236fa,” Exp. Thermal. Fluid Sci., vol. 35, no. 3, pp.442–454, 2011. DOI: https://doi.org/10.1016/j.expthermflusci.2010.11.006.
   Web of Science ®Google Scholar
• F. Illan-Gomez, A. Lopez-Belchi, J. R. Garcia-Cascales, and F. Vera-Garcia, “Experimental two-phase heat transfer coefficient and friction pressure drop inside minichannels during condensation with R1234yf and R134a,” Int. J. Refrig., vol. 51, pp. 12–23, 2015. DOI: https://doi.org/10.1016/j.ijrefrig.2014.11.014.
   Web of Science ®Google Scholar
• A. Lopez-Belchi, F. Illan-Gomez, J. R. Garcia-Cascales, and F. Vera-Garcia, “Heat transfer coefficient during condensation inside a minichannel multiport tube with R32 and R410A as working fluids,” Sci. Tech. Built Env., vol. 21, pp. 535–544, 2015. DOI: https://doi.org/10.1080/23744731.2015.1040340.
   Web of Science ®Google Scholar
• D. Jige, N. Inoue, and S. Koyama, “Condensation of refrigerants in a multiport tube with rectangular minichannels,” Int. J. Refrig., vol. 67, pp. 202–213, 2016. DOI: https://doi.org/10.1016/j.ijrefrig.2016.03.020.
   Web of Science ®Google Scholar
• M. M. Rahman, H. Kariya, and A. Miyara, “An experimental study and development of new correlation for condensation heat transfer coefficient of refrigerant inside a multiport minichannel with and without fins,” Int.J. Heat Mass Trans., vol. 116, pp. 50–60, 2018. DOI: https://doi.org/10.1016/j.ijheatmasstransfer.2017.09.010.
   Web of Science ®Google Scholar
• P. Knipper, D. Bertsche, R. Gneiting, and T. Wetzel, “Experimental investigation of heat transfer and pressure drop during condensation of R-134a in multiport flat tubes,” Int. J. Refrig., vol. 98, pp. 211–221, 2019. DOI: https://doi.org/10.1016/j.ijrefrig.2018.10.019.
   Web of Science ®Google Scholar
• C. Y. Park and P. S. Hrnjak, “CO2 flow condensation heat transfer and pressure drop in multiport microchannels at low temperatures,” Int. J. Refrig., vol. 32, pp. 1129–1139, 2009. DOI: https://doi.org/10.1016/j.ijrefrig.2009.01.030.
   Web of Science ®Google Scholar
• J. Heo, H. Park, and R. Yun, “Condensation heat transfer and pressure drop characteristics of CO2 in a microchannel,” Int. J. Refrig., vol. 36, pp. 1657–1668, 2013.
   Web of Science ®Google Scholar
• P. Fernando, B. Palm, T. Ameel, P. Lundquist, and E. Granyd, “A minichannel aluminum tube heat exchanger - Part III: condenser performance with propane,” Int. J. Refrig., vol. 31, pp. 696–708, 2008. DOI: https://doi.org/10.1016/j.ijrefrig.2008.02.013.
   Web of Science ®Google Scholar
• W. W. Akers, H. A. Deans, and O. K. Crosser, “Condensation heat transfer within horizontal tubes,” Chem. Eng. Progress Symp. Series, vol. 55, pp. 171–176, 1959.
   Google Scholar
• H. Haragucchi, S. Koyama, and T. Fujii, “Condensation of refrigerant HCFC22, HFC134a and HCFC123 in a horizontal smooth tube (2nd report, proposal of empirical expressions for the local heat transfer coefficient),” Trans. JSME (B), vol. 60, no. 574, pp. 245–252, 1994. (in Japanese).
   Google Scholar
• Y. P. Chang, R. Tsai, and J. W. Hwang, “Condensing heat transfer characteristics of aluminum flat tube,” Appl. Therm. Eng., vol. 17, no. 11, pp.1055–1065, 1997. DOI: https://doi.org/10.1016/S1359-4311(97)00011-2.
   Web of Science ®Google Scholar
• S. M. Kim and I. Mudawar, “Flow condensation in parallel micro-channels - Part 2: heat transfer results and correlation technique,” Int. J. Heat Mass Trans., vol. 55, no. 4, pp.984–994, 2012. DOI: https://doi.org/10.1016/j.ijheatmasstransfer.2011.10.012.
   Web of Science ®Google Scholar
• Q. V. Pham, K.-I. Choi, J.-T. Oh, and H. Cho, “Flow condensation heat transfer of R410A, R22 and R32 inside a microfin tube,” Exp. Heat Transf., vol. 32, pp. 102–115, 2019. DOI: https://doi.org/10.1080/08916152.2018.1485783.
   Web of Science ®Google Scholar
• A. K. Solanki and R. Kumar, “Condensation heat transfer and pressure drop characteristics of R-134a inside the flattened tubes at high mass flux and different saturation temperature,” Exp. Heat Transf., vol. 32, no. 1, pp.69–84, 2019. DOI: https://doi.org/10.1080/08916152.2018.1485781.
   Web of Science ®Google Scholar
• E. E. Wilson, “A basis for rational design of heat transfer apparatus,” Trans. ASME, vol. 37, pp. 47–70, 1915.
   Google Scholar
• J. G. Collier and J. R. Thome, Convective Boiling and Condensation. 3rd. Oxford University Press, 1994.
   Google Scholar
• S. M. Zivi, “Estimation of steady-state steam void fraction by means of the principle of minimum entropy production,” J. Heat Transf., vol. 86, no. 2, pp.247–252, 1964. DOI: https://doi.org/10.1115/1.3687113.
   Google Scholar
• S. J. Kline and F. A. McClintock, “The description of uncertainties in single sample experiments,” Mech. Eng., vol. 75, pp. 3–9, 1953.
   Google Scholar
• V. Gnielinski, “On heat transfer in tubes,” Int. J. Heat Mass Trans., vol. 63, pp. 134–140, 2013. DOI: https://doi.org/10.1016/j.ijheatmasstransfer.2013.04.015.
   Web of Science ®Google Scholar
• K. Sakamatapan, J. Kaew-On, A. S. Dalkilic, and S. Wongwises, “Condensation heat transfer characteristics of R-134a flowing inside the multiport minichannels,” Int. J. Heat Mass Trans., vol. 64, pp. 976–985, 2013. DOI: https://doi.org/10.1016/j.ijheatmasstransfer.2013.04.020.
   Web of Science ®Google Scholar
• H. M. Soliman, “On the annular-to-wavy flow pattern transition during condensation inside horizontal tubes,” Canadian J. Chem. Eng., vol. 60, no. 4, pp.475–481, 1982. DOI: https://doi.org/10.1002/cjce.5450600405.
   Web of Science ®Google Scholar
• A. Lopez-Belchi, F. Vera-Garcia, and J. R. Garcia-Cascales, “Non-uniform condensation of refrigerant R-134a in multi-channel multi-port tubes: two-phase pressure drop and heat transfer coefficient,” J. Enhanc. Heat Trans., vol. 22, no. 5, pp.391–416, 2015. DOI: https://doi.org/10.1615/JEnhHeatTransf.2016014248.
   Web of Science ®Google Scholar
• M. M. Shah, “A correlation for heat transfer during condensation in mini/micro channels,” Int. J. Refrig., vol. 64, pp. 187–202, 2016. DOI: https://doi.org/10.1016/j.ijrefrig.2015.12.008.
   Web of Science ®Google Scholar
• A. Cavallini, D. Del Col, M. Matkovic, and L. Rossetto, “Frictional pressure drop during vapor-liquid flow in minichannels: modeling and experimental evaluation,” Int. J. Heat Fluid Flow, vol. 30, no. 1, pp.131–191, 2009. DOI: https://doi.org/10.1016/j.ijheatfluidflow.2008.09.003.
   Web of Science ®Google Scholar
• L. Sun and K. Mishima, “Evaluation analysis of prediction methods for two-phase flow pressure drop in minichannels,” Int. J. Multiphase Flow, vol. 35, no. 1, pp.47–54, 2009. DOI: https://doi.org/10.1016/j.ijmultiphaseflow.2008.08.003.
   Web of Science ®Google Scholar
• K.-I. Choi, A. S. Pamitran, C.-Y. Oh, and J.-T. Oh, “Two-phase pressure drop of R-410A in horizontal smooth minichannels,” Int. J. Refrig., vol. 31, no. 1, pp.119–129, 2008. DOI: https://doi.org/10.1016/j.ijrefrig.2007.06.006.
   Web of Science ®Google Scholar
• M. M. Shah, “A general correlation for heat transfer during film condensation inside pipes,” Int. J. Heat Mass Trans., vol. 22, no. 4, pp.547–556, 1979. DOI: https://doi.org/10.1016/0017-9310(79)90058-9.
   Web of Science ®Google Scholar
• N.-H. Kim and R. L. Webb, “Analytic prediction of the friction and heat transfer for turbulent flow in axial internal fin tubes,” J. Heat Trans., vol. 115, no. 3, pp.553–559, 1993. DOI: https://doi.org/10.1115/1.2910723.
   Web of Science ®Google Scholar
• A. Cavallini, D. Del Col, S. Mancin, and L. Lossetto, “Condensation of pure and near-azeotropic refrigerants in microfin tubes: a new computational procedure,” Int. J. Refrig., vol. 32, no. 1, pp.162–174, 2009. DOI: https://doi.org/10.1016/j.ijrefrig.2008.08.004.
   Web of Science ®Google Scholar
• S. Mehendale, “Condensing heat transfer of pure refrigerants and refrigerant mixtures flowing within horizontal microfin tubes: a new model,” Int. J. Refrig., vol. 103, pp. 223–242, 2019. DOI: https://doi.org/10.1016/j.ijrefrig.2019.04.015.
   Web of Science ®Google Scholar
• A. Cavallini, J. S. Brown, D. Del Col, and C. Zilio, “In-tube condensation performance of refrigerants considering penaization terms (exergy loss) for heat transfer and pressure drop,” Int. J. Heat Mass Trans., vol. 53, no. 13–14, pp.2885–2896, 2010. DOI: https://doi.org/10.1016/j.ijheatmasstransfer.2010.02.007.
   Web of Science ®Google Scholar