Composition containing compound useful as refrigerant, detergent, propellant, or the like, and refrigerating machine, large-sized air conditioner, or industrial process cooler each including said composition
A technology of composition and compound, applied in the direction of detergent composition, non-surface active detergent composition, refrigerator, etc., can solve the problems of insufficient freezing capacity of HFO refrigerant, corrosion of piping, difficulty in applying to large-scale air-conditioning equipment, etc. , to achieve the effect of excellent freezing ability, low flammability and high effectiveness
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Embodiment 1 and comparative example 1
[0136] Pentafluorobutyne (PFB) was prepared as the refrigerant of Example 1, and HCFO-1233zd(E) was prepared as the refrigerant of Comparative Example 1.
[0137] Using the above refrigerants, evaluate COPc and refrigeration capacity (kJ / m 3 ), density (inhalation) (kg / m 3 ), suction pressure (MPa), discharge pressure (MPa), discharge temperature (°C).
[0138] Regarding the operating conditions (circulation conditions) of large-scale air-conditioning equipment, the evaporation temperature of the refrigerant in the evaporator is set to 0°C, the condensation temperature of the refrigerant in the condenser is set to 40°C, the degree of superheat is set to 5°C, and the degree of subcooling is set to 0°C.
[0139] Table 1 shows the results of each evaluation.
[0140] [Table 1]
[0141] The refrigerant PFB 1233 E COPc 3.80 4.10 freezing capacity [kJ / m3] 1113 442 Density (inhalation) [kg / m3] 10.59 2.78 suction pressure [Mpa] 0.16...
Embodiment 2 and comparative example 2
[0144] Pentafluorobutyne (PFB) was prepared as the refrigerant of Example 2, and HCFO-1233zd(E) was prepared as the refrigerant of Comparative Example 2.
[0145] Using the above refrigerants, evaluate COPc and refrigeration capacity (kJ / m 3 ), density (inhalation) (kg / m 3 ), suction pressure (MPa), discharge pressure (MPa), discharge temperature (°C).
[0146] Regarding the operating conditions (circulation conditions) of the turbo refrigerator, the evaporation temperature of the refrigerant in the evaporator was set to 5°C, the condensation temperature of the refrigerant in the condenser was set to 35°C, the degree of superheat was set to 0°C, and the degree of subcooling was set to 5°C.
[0147] Table 2 shows the results of each evaluation.
[0148] [Table 2]
[0149] The refrigerant PFB 1233 E COPc 5.77 6.01 freezing capacity [kJ / m3] 1501 594 Density (inhalation) [kg / m3] 12.81 3.47 suction pressure [Mpa] O.193 0.060 ...
Embodiment 3 and comparative example 3
[0152] Pentafluorobutyne (PFB) was prepared as the refrigerant of Example 3, and HCFO-1233zd(E) was prepared as the refrigerant of Comparative Example 3.
[0153] Using the above refrigerants, evaluate COPc, refrigeration capacity (kJ / m 3 ), density (inhalation) (kg / m 3 ), suction pressure (MPa), discharge pressure (MPa), discharge temperature (°C).
[0154] Regarding the operating conditions (circulation conditions) of the two-stage cycle turbo refrigerator, the evaporation temperature of the refrigerant in the evaporator is set to 5°C, the condensation temperature of the refrigerant in the condenser is set to 35°C, the degree of superheat is set to 0°C, and the supercooling The temperature is set to 5°C.
[0155] Table 3 shows the results of each evaluation.
[0156] [table 3]
[0157] The refrigerant PFB 1233 E COPc 6.36 6.47 freezing capacity [kJ / m3] 2554 640 Density (inhalation) [kg / m3] 18.01 3.47 suction pressure [Mpa...
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