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Assessing the Effect of Thermodynamic, Hydrodynamic and Geometric of an Air Cooled Condenser on COP of Vapor Compression Cycle
Authors: Hosein Shokohmand, Mahmood Hosein Zare, Abdorreza Qolibeik
Abstract:
In this paper, the effects of thermodynamic, hydrodynamic and geometric of an air cooled condenser on COP of vapor compression cycle are investigated for a fixed condenser facing surface area. The system is utilized with a scroll compressor, modeled based on thermodynamic and heat transfer equations employing Matlab software. The working refrigerant is R134a whose thermodynamic properties are called from Engineering Equation Software. This simulation shows that vapor compression cycle can be designed by different configurations and COPs, economical and optimum working condition can be obtained via considering these parameters.Keywords: Vapor compression cycle, air cooled condenser, COP, heat exchanger, thermal modeling.
Digital Object Identifier (DOI): doi.org/10.5281/zenodo.1334143
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[1] Cherem-Pereira, N. Mendes, Empirical modeling of room air conditioners for building energy analysis, Energy and Buildings 47 (2012) 19-26
[2] Yu Chen, Nils P. Halm, Eckhard A. Groll, James E. Braun, Mathematical modeling of scroll compressors, part one : compression process modeling, International Journal of Refrigeration 25 (2002) 731- 750
[3] Jose M. Corberfin ,Monica Garcia Melon, Modeling of plate finned tube evaporators and condensers working with R134A, international journal of refrigeration, 21,(1998) 273-284
[4] R. Cabello , J. Navarro , E. Torrella, Simplified steady state modeling of a single stage vapor compression plant. Model development and validation, Applied Thermal Engineering 25 (2005) 1740-1752
[5] http://en.wikipedia.org/wiki/Vapor-compression-refrigeration
[6] Klein, S. A. and Reindl, D. T., 1997. "The Relationship of Optimum Heat Exchanger Allocation and Minimum Entropy Generation for Refrigeration Cycles," Proceedings of the ASME Advanced Energy Systems Division, vol. 37, pp. 87-94.
[7] Frank P. Incorpera & Dewitt, fundamentals of heat and mass transfer, third edition, John Wiley & Sons, New York, 1990.
[8] Schmidt, T. E., 1945. "La Production Calorifique des Surfaces Munies d-ailettes," Annexe Du bulletin De L-Institut International Du Froid, Annexe G-5.
[9] Kays, W. M. and London, A. L., 1984. Compact Heat Exchangers, 3rd Edition, McGraw-Hill, New York.
[10] J.R. Thome, Engineering Data Book 3,Wolverine Tube, Inc.,2007.
[11] Churchill, S.W., "Friction factor equations spans all fluid-flow ranges.", Chemical Eng., 91,1977
[12] Chisholm, D., 1983. Two-Phase flow in Pipelines and Heat Exchangers, Longman Inc., New York.
[13] McQuiston, F. C. and Parker, J. P., 1994. Heating Ventilating and Air- Conditioning-Analysis and Design, John Wiley & Sons, New York.
[14] Zukauskas, A. and Ulinskas, R., 1998. "Banks of Plain and Finned Tubes," Heat Exchanger Design Handbook, G. F. Hewitt Edition, Begell House, Inc., New York, pp. 2.24-1 - 2.24-17.
[15] ARI, 1989. Air-conditioning and Refrigeration Standard 210/240-89, p. 3, section 5.1.