PERFORMANCE OF NATURAL REFRIGERANTS IN TWO PHASE FLOW
DOI:
https://doi.org/10.11113/jt.v78.9658Keywords:
Two-phase flow, natural refrigerant, optimized conditions, nucleate boiling, forced convectiveAbstract
The search for alternative environmentally friendly refrigerants have never been so crucial with the increasing demand for effective cooling of increasing miniaturization of our heat exchanging devices in the ever expanding air-conditioning and refrigeration industry. Although propane (R290) and ammonia (R717), natural refrigerants, have been around for decades, their two-phase thermal performance in small channels has yet to be fully investigated. Predictions of the heat transfer using correlations developed based on past experimental data have shown poor agreements, with more correlations being developed to date. This research was done to investigate the optimized conditions for the two-phase boiling heat transfer coefficient of R290 and R717 where the contributions from nucleate boiling and forced convective are represented explicitly. Multi-objective Genetic Algorithm (MOGA) is utilized for the simultaneous maximization of nucleate boiling and forced convective, two conflicting phenomena – the former generally significant in the low vapor quality region while the latter in the high quality region. A superposition correlation is used as it sums up both contributions. Two phased-out refrigerants, R134a and R22 are also being research here for comparison purposes. The range of MOGA design parameters set for mass flux, G, is between 100 - 300 kg/m2.s, heat flux q between 5 - 30 kW/m2 and vapor quality, x for 0.0009 - 0.9. The optimization is done for 3 mm channel diameter with saturation temperature at 10˚C. The optimized results showed a strong contribution of each nucleate boiling and forced convective for R717 with increasing vapor quality, compared to the other three refrigerants. The optimized value of the total heat transfer coefficient for R717 could reach up to 90 kW/m2.K and for R290 up to 12 kW/m2.K compared to R134a and R22 at 6 kW/m2.K and 5 kW/m2.K respectively. At lower vapor quality, the nucleate boiling contributes more to the total heat transfer coefficient, and suppressed due to forced convective as the vapor quality reaches middle range. The theoretical results indicate the potential of R717 and R290 as replacement refrigerants for R22 and R134a with further verifications to be done with correlations not using the superposition method.
References
Oh, H. K. and Son, C. H. 2011. Flow Boiling Heat Transfer and Pressure Drop Characteristics of CO2 in Horizontal Tube of 4.57-mm Inner Diameter. Applied Thermal Engineering. 31(2-3): 163-172.
Hassan, M. A. M. and Shedid, M. H. 2015. Experimental Investigation of Two Phases Evaporative Heat Transfer Coefficient of Carbon Dioxide as a Pure Refrigerant and Oil Contaminated Under Forced Flow Conditions in Small And Large Tube. International Journal of Refrigeration. 56: 28-36.
Wu, J., Koettig, T., Franke, C., Helmer, D., Eisel, T., Haug, F. and Bremer, J. 2011. Investigation Of Heat Transfer and Pressure Drop of CO2 Two-Phase Flow in A Horizontal Minichannel. International Journal of Heat and Mass Transfer. 54 (9-10): 2154-2162.
Sathyabhama, A. and Babu, T. P. A. 2011. Experimental Investigation in Pool Boiling Heat Transfer of Ammonia/Water Mixture and Heat Transfer Correlations. International Journal of Heat and Fluid Flow. 32(3): 719-729.
Del Col, D., Bortolato, M. and Bortolin, S. 2014. Comprehensive Experimental Investigation of Two-Phase Heat Transfer and Pressure Drop with Propane in A Minichannel. International Journal of Refrigeration. 47: 66-84.
Fang, X., Zhou, Z. and Wang, H. 2015. Heat Transfer Correlation for Saturated Flow Boiling of Water. Applied Thermal Engineering. 76: 147-156.
Pamitran, A. S., Choi, K. I., Oh, J. T. and Nasruddin. 2011. Evaporation Heat Transfer Coefficient in Single Circular Small Tubes for Flow Natural Refrigerants of C3H8, NH3, and CO2. International Journal of Multiphase Flow. 37(7): 794-801.
Cavallini, A., Del Col, D. and Rossetto, L. 2013. Heat Transfer and Pressure Drop of Natural Refrigerants in Minichannels (Low Charge Equipment). International Journal of Refrigeration. 36(2): 287-300.
Adham, A., Mohd-Ghazali, N. and Ahmad, R. 2016. Optimization of Nanofluid-Cooled Microchannel Heat Sink. Thermal Science. 20 (1): 109-118.
Mohd-Ghazali, N., Jong-Taek, O., Chien, N. B., Kwang-Il, C. and Ahmad, R. 2015. Comparison of the Optimized Thermal Performance of Square and Circular Ammonia-cooled Microchannel Heat Sink with Genetic Algorithm. Energy Conversion Management. 102: 59-65.
Qais, A. Y., Mohd-Ghazali, N., Zolpakar, N. A., Sentot, N., Pamitran, A. S. and Ahmad, R. 2016. Modeling of the Minimized Two-Phase Flow Frictional Pressure Drop in a Small Tube with Different Correlations. Jurnal Teknologi. 78(6-11): 109-115.
Qais, A. Y., Mohd-Ghazali, N., Pamitran, A. S., Sentot, N. and Ahmad, R. 2016. Optimization of the Friction Factor and Frictional Pressure Drop of R22 And R290. Jurnal Teknologi. 7(2): 2087-2100.
Oh, J. T., Pamitran, A. S., Choi, K. I. and Hrnjak, P. 2011. Experimental Investigation on Two-Phase Flow Boiling Heat Transfer of Five Refrigerants in Horizontal Small Tubes of 0.5, 1.5 and 3.0 mm Inner Diameters. International Journal of Heat and Mass Transfer. 54(9-10): 2080-2088.
Cooper, M. G. 1989. Flow Boiling - The ‘Apparently Nucleate’ Regime. International Journal of Heat and Mass Transfer. 32(3): 459-464.
Dittus, F. W. and Boelter, L. M. K. 1985. Heat Transfer in Automobile Radiators of the Tubular Type. International Communications in Heat and Mass Transfer. 12(1): 3-22.
Chisholm, D. 1967. A Theoretical Basis for the Lockhart-Martinelli Correlation for Two-Phase Flow. International Journal of Heat and Mass Transfer. 10(12): 1767-1778.
Linstrom, P. J. and Mallard, W. G. NIST Chemistry WebBook, NIST Standard Reference Database Number 69. National Institute of Standards and Technology. [Online]. Available: http://webbook.nist.gov. [Accessed: 01-Jul-2016].
Kim, S. M. and Mudawar, I. 2013. Universal Approach to Predicting Saturated Flow Boiling Heat Transfer in Mini/Micro-Channels - Part II. Two-Phase Heat Transfer Coefficient. International Journal of Heat and Mass Transfer. 64: 1239-1256.
Gosselin, L., Tye-Gingras, M. and Mathieu-Potvin, F. 2009. Review of Utilization of Genetic Algorithms in Heat Transfer Problems. International Journal of Heat and Mass Transfer. 52 (9-10): 2169-2188.
Matlab and Optimization Toolbox 2014a. The Mathworks Inc., Natick, Massachussets, United States.
Siriwardene, N. R. and Perera, B. J. C. 2006. Selection of Genetic Algorithm Operators for Urban Drainage Model Parameter Optimisation. Mathematical Computing and Modelling. 44: 415-429.
Spindler, K. 2010. Overview and Discussion on Pool Boiling Heat Transfer Data and Correlations of Ammonia. International Journal of Refrigeration. 33(7):1292-1306.
Choi, K., Oh, J., Saito, K. and Soo, J. 2014. Comparison of Heat Transfer Coefficient during Evaporation of Natural Refrigerants and R-1234yf in Horizontal Small Tube. International Journal of Refrigeration. 41: 210-218.
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