Middle-high temperature heat pump mixing working substance containing trifluoroiodomethane (R13I1) and tetrafluoromethane (HFCl34a)
A technology of trifluoroiodomethane and tetrafluoroethane, which is applied in the field of refrigerants, can solve the problems of easy accidents, inability to provide heat energy, and deterioration of cycle performance, so as to reduce the greenhouse effect, excellent environmental characteristics, and excellent cycle performance. Effect
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Embodiment 1
[0012] take 35 mass % R13I1, 27 mass % HFC134a, 38 mass % HFC245fa, used as a refrigerant after physical mixing at room temperature.
[0013] The design conditions of the heat pump system are taken as follows: the average evaporation temperature is 40°C, the average condensation temperature is 85°C, and the suction superheat is 2°C (for some working fluids, an appropriate exhaust superheat is taken to avoid wet compression), The degree of supercooling is 5°C. Taking non-piston (such as screw, scroll, etc.) compressors as an example, the thermal efficiency of the compressor is 0.9, and the motor efficiency, mechanical efficiency and constant entropy efficiency of the compression process are all 0.85.
Embodiment 2
[0015] Take 38 mass % R13I1, 13 mass % HFC134a, 49 mass % HFC245fa, used as a refrigerant after physical mixing at room temperature.
[0016] The design conditions of the heat pump system are taken as follows: the average evaporation temperature is 50°C, the average condensation temperature is 95°C, and the suction superheat is 2°C (for some working fluids, an appropriate exhaust superheat is taken to avoid wet compression), The degree of subcooling is 0°C. Taking the hermetic piston compressor as an example, the thermal efficiency of the compressor is taken as 0.9, the motor efficiency, mechanical efficiency and constant entropy efficiency of the compression process are all taken as 0.85, and the clearance volume coefficient is taken as 0.03.
Embodiment 3
[0018] Take 36 mass %R13I1,3 mass % HFC134a, 61 mass % HFC245fa, used as a refrigerant after physical mixing at room temperature.
[0019] The design conditions of the heat pump system are taken as follows: the average evaporation temperature is 60°C, the average condensation temperature is 105°C, and the suction superheat is 2°C (for some working fluids, an appropriate exhaust superheat is taken to avoid wet compression), The degree of subcooling is 0°C. Taking the hermetic piston compressor as an example, the thermal efficiency of the compressor is taken as 0.9, the motor efficiency, mechanical efficiency and constant entropy efficiency of the compression process are all taken as 0.85, and the clearance volume coefficient is taken as 0.03.
[0020] According to the cycle calculation, the relevant parameters and cycle performance indexes of the above three embodiments are shown in Table 2.
[0021] Parameters and performance
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