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Numerical analysis of an air condenser working with the refrigerant fluid R407C
Affiliation:1. Key Laboratory of Efficient Utilization of Low and Medium Grade Energy, MOE, Tianjin University, No.92 Weijin Road, Tianjin 300072, China;2. China Aviation Planning and Construction Development Co,. LTD, Beijing 100120, China;1. Laboratory of Heat Transfer, Department of Thermal Engineering, School of Mechanical Engineering, National Technical University of Athens, 9 Iroon Polytechniou St., 15780, Zografou, Greece;2. Laboratory of Internal Combustion Engines, Department of Thermal Engineering, School of Mechanical Engineering, National Technical University of Athens, 9 Iroon Polytechniou St., 15780, Zografou, Greece
Abstract:As CFC (clorofluorocarbon) and HCFC (hydrochlorofluorocarbon) refrigerants which have been used as refrigerants in a vapour compression refrigeration system were know to provide a principal cause to ozone depletion and global warming, production and use of these refrigerants have been restricted. Therefore, new alternative refrigerants should be searched for, which fit to the requirements in an air conditioner or a heat pump, and refrigerant mixtures which are composed of HFC (hydrofluorocarbon) refrigerants having zero ODP (ozone depletion potential) are now being suggested as drop-in or mid-term replacement. However also these refrigerants, as the CFC and HCFC refrigerants, present a greenhouse effect.The zeotropic mixture designated as R407C (R32/R125/R134a 23/25/52% in mass) represents a substitute of the HCFC22 for high evaporation temperature applications as the air-conditioning.Aim of the paper is a numerical–experimental analysis for an air condenser working with the non azeotropic mixture R407C in steady-state conditions. A homogeneous model for the condensing refrigerant is considered to forecast the performances of the condenser; this model is capable of predicting the distributions of the refrigerant temperature, the velocity, the void fraction, the tube wall temperature and the air temperature along the test condenser. Obviously in the refrigerant de-superheating phase the numerical analysis becomes very simple. A comparison with the measurements on an air condenser mounted in an air channel linked to a vapour compression plant is discussed. The results show that the simplified model provides a reasonable estimation of the steady-state response and that this model is useful to design purposes.
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