COMPRESSOR

Abstract
High power of a compressor that compresses a mixed refrigerant containing at least 1,2-difluoroethylene is achieved. A compressor (100) employs an induction motor (70) as a motor that drives a compression unit (60) that compresses a mixed refrigerant containing at least 1,2-difluoroethylene, and thus, high power is enabled at comparatively low costs.
Description
TECHNICAL FIELD

The present invention relates to a compressor to be used in a refrigerant cycle apparatus considering environmental protection.


BACKGROUND ART

In recent years, from the point of view of environmental protection, a refrigerant (hereinafter referred to as GWP refrigerant) having low global warming potential (GWP) has been examined as a refrigerant to be used in an air conditioner. As the low GWP refrigerant, a mixed refrigerant containing 1,2-difluoroethylene is firstly presented.


SUMMARY OF THE INVENTION
Technical Problem

However, the number of prior arts considering from an aspect of high efficiency of an air conditioner that uses the aforementioned refrigerant is small. For example, when the aforementioned refrigerant is to be applied to an air conditioner such as that disclosed in PTL 1 (Japanese Unexamined Patent Application Publication No. 2013-124848), there is a problem that how high power of a compressor is achieved.


Solution to Problem

A compressor according to a first aspect includes a compression unit that compresses a mixed refrigerant containing at least 1,2-difluoroethylene and an induction motor that drives the compression unit.


Employing an induction motor, as described above, in a compressor that compresses a mixed refrigerant containing at least 1,2-difluoroethylene enables high power at comparatively low costs.


A compressor according to a second aspect is the compressor according to the first aspect, in which a rotor of the induction motor has a plurality of conducting bars that are bar-shaped conductors and that are disposed in an annular form, and an end ring that short-circuits the plurality of conducting bars at an end portion in an axial direction. At least the conducting bars are formed of a metal whose electric resistance is lower than electric resistance of aluminum.


In this compressor, heat generation due to current that flows through the conducting bars of the induction motor is suppressed, and thus, high power is enabled.


A compressor according to a third aspect is the compressor according to the first aspect, in which a rotor of the induction motor has a heat-radiation structure.


In this compressor, a temperature increase of the rotor of the induction motor is suppressed, and thus, high power is enabled.


A compressor according to a fourth aspect is the compressor according to the third aspect, in which the rotor of the induction motor has a plurality of conducting bars that are bar-shaped conductors and that are disposed in an annular form, and an end ring that short-circuits the plurality of conducting bars at an end portion in an axial direction. The heat-radiation structure is formed on the end ring.


In this compressor, heat radiation properties are improved because the heat-radiation structure rotates itself, and moreover, the rotation causes forced convection and suppresses an increase in the peripheral temperature, which enables high power.


A compressor according to a fifth aspect is the compressor according to the third aspect or the fourth aspect, in which the heat-radiation structure is a heat sink.


In this compressor, it is possible to integrally mold the heat sink when molding the end ring of the induction motor, and thus, high power is enabled at comparatively low costs.


A compressor according to a sixth aspect is the compressor according to the first aspect, in which a cooling structure that cools a stator of the induction motor by a refrigerant is further provided.


This compressor enables high power because the induction motor is cooled.


A compressor according to a seventh aspect is the compressor according to the sixth aspect, in which the cooling structure cools the stator by the cool heat of a refrigerant that flows in a refrigerant circuit to which the compressor is connected.


A compressor according to a eighth aspect is the compressor according to any of the first through seventh aspects, wherein, the refrigerant comprises trans-1,2-difluoroethylene (HFO-1132(E)), trifluoroethylene (HFO-1123), and 2,3,3,3-tetrafluoro-1-propene (R1234yf).


In this compressor, an induction motor is employed, and thus high power at comparatively low costs can also be achieved when a refrigerant having a sufficiently low GWP, a refrigeration capacity (may also be referred to as a cooling capacity or a capacity) and a coefficient of performance (COP) equal to those of R410A is used.


A compressor according to a ninth aspect is the compressor according to the eighth aspect, wherein, when the mass % of HFO-1132(E), HFO-1123, and R1234yf based on their sum in the refrigerant is respectively represented by x, y, and z, coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R1234yf is 100 mass % are within the range of a figure surrounded by line segments AA′, A′B, BD, DC′, C′C, CO, and OA that connect the following 7 points:


point A (68.6, 0.0, 31.4),


point A′ (30.6, 30.0, 39.4),


point B (0.0, 58.7, 41.3),


point D (0.0, 80.4, 19.6),


point C′ (19.5, 70.5, 10.0),


point C (32.9, 67.1, 0.0), and


point O (100.0, 0.0, 0.0),


or on the above line segments (excluding the points on the line segments BD, CO, and OA);


the line segment AA′ is represented by coordinates (x, 0.0016x2−0.9473x+57.497, −0.0016x2−0.0527x+42.503),


the line segment A′B is represented by coordinates (x, 0.0029x2−1.0268x+58.7, −0.0029x2+0.0268x+41.3),


the line segment DC′ is represented by coordinates (x, 0.0082x2−0.6671x+80.4, −0.0082x2−0.3329x+19.6),


the line segment C′C is represented by coordinates (x, 0.0067x2−0.6034x+79.729, −0.0067x2−0.3966x+20.271), and


the line segments BD, CO, and OA are straight lines.


A compressor according to a tenth aspect is the compressor according to the eighth aspect, wherein, when the mass % of HFO-1132(E), HFO-1123, and R1234yf based on their sum in the refrigerant is respectively represented by x, y, and z, coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R1234yf is 100 mass % are within the range of a figure surrounded by line segments GI, IA, AA′, A′B, BD, DC′, C′C, and CG that connect the following 8 points:


point G (72.0, 28.0, 0.0),


point I (72.0, 0.0, 28.0),


point A (68.6, 0.0, 31.4),


point A′ (30.6, 30.0, 39.4),


point B (0.0, 58.7, 41.3),


point D (0.0, 80.4, 19.6),


point C′ (19.5, 70.5, 10.0), and


point C (32.9, 67.1, 0.0),


or on the above line segments (excluding the points on the line segments IA, BD, and CG);


the line segment AA′ is represented by coordinates (x, 0.0016x2−0.9473x+57.497, −0.0016x2−0.0527x+42.503),


the line segment A′B is represented by coordinates (x, 0.0029x2−1.0268x+58.7, −0.0029x2+0.0268x+41.3),


the line segment DC′ is represented by coordinates (x, 0.0082x2−0.6671x+80.4, −0.0082x2−0.3329x+19.6),


the line segment C′C is represented by coordinates (x, 0.0067x2−0.6034x+79.729, −0.0067x2−0.3966x+20.271), and


the line segments GI, IA, BD, and CG are straight lines.


A compressor according to a eleventh aspect is the compressor according to the eighth aspect, wherein, when the mass % of HFO-1132(E), HFO-1123, and R1234yf based on their sum in the refrigerant is respectively represented by x, y, and z, coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R1234yf is 100 mass % are within the range of a figure surrounded by line segments JP, PN, NK, KA′, A′B, BD, DC′, C′C, and CJ that connect the following 9 points:


point J (47.1, 52.9, 0.0),


point P (55.8, 42.0, 2.2),


point N (68.6, 16.3, 15.1),


point K (61.3, 5.4, 33.3),


point A′ (30.6, 30.0, 39.4),


point B (0.0, 58.7, 41.3),


point D (0.0, 80.4, 19.6),


point C′ (19.5, 70.5, 10.0), and


point C (32.9, 67.1, 0.0),


or on the above line segments (excluding the points on the line segments BD and CJ);


the line segment PN is represented by coordinates (x, −0.1135x2+12.112x−280.43, 0.1135x2−13.112x+380.43),


the line segment NK is represented by coordinates (x, 0.2421x2−29.955x+931.91, −0.2421x2+28.955x−831.91),


the line segment KA′ is represented by coordinates (x, 0.0016x2−0.9473x+57.497, −0.0016x2−0.0527x+42.503),


the line segment A′B is represented by coordinates (x, 0.0029x2−1.0268x+58.7, −0.0029x2+0.0268x+41.3),


the line segment DC′ is represented by coordinates (x, 0.0082x2−0.6671x+80.4, −0.0082x2−0.3329x+19.6),


the line segment C′C is represented by coordinates (x, 0.0067x2−0.6034x+79.729, −0.0067x2−0.3966x+20.271), and


the line segments JP, BD, and CG are straight lines.


A compressor according to a twelveth aspect is the compressor according to the eighth aspect, wherein, when the mass % of HFO-1132(E), HFO-1123, and R1234yf based on their sum in the refrigerant is respectively represented by x, y, and z, coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R1234yf is 100 mass % are within the range of a figure surrounded by line segments JP, PL, LM, MA′, A′B, BD, DC′, C′C, and CJ that connect the following 9 points:


point J (47.1, 52.9, 0.0),


point P (55.8, 42.0, 2.2),


point L (63.1, 31.9, 5.0),


point M (60.3, 6.2, 33.5),


point A′ (30.6, 30.0, 39.4),


point B (0.0, 58.7, 41.3),


point D (0.0, 80.4, 19.6),


point C′ (19.5, 70.5, 10.0), and


point C (32.9, 67.1, 0.0),


or on the above line segments (excluding the points on the line segments BD and CJ);


the line segment PL is represented by coordinates (x, −0.1135x2+12.112x−280.43, 0.1135x2−13.112x+380.43)


the line segment MA′ is represented by coordinates (x, 0.0016x2−0.9473x+57.497, −0.0016x2−0.0527x+42.503),


the line segment A′B is represented by coordinates (x, 0.0029x2−1.0268x+58.7, −0.0029x2+0.0268x+41.3),


the line segment DC′ is represented by coordinates (x, 0.0082x2−0.6671x+80.4, −0.0082x2−0.3329x+19.6),


the line segment C′C is represented by coordinates (x, 0.0067x2−0.6034x+79.729, −0.0067x2−0.3966x+20.271), and


the line segments JP, LM, BD, and CG are straight lines.


A compressor according to a thirteenth aspect is the compressor according to the eighth aspect, wherein, when the mass % of HFO-1132(E), HFO-1123, and R1234yf based on their sum in the refrigerant is respectively represented by x, y, and z, coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R1234yf is 100 mass % are within the range of a figure surrounded by line segments PL, LM, MA′, A′B, BF, FT, and TP that connect the following 7 points:


point P (55.8, 42.0, 2.2),


point L (63.1, 31.9, 5.0),


point M (60.3, 6.2, 33.5),


point A′ (30.6, 30.0, 39.4),


point B (0.0, 58.7, 41.3),


point F (0.0, 61.8, 38.2), and


point T (35.8, 44.9, 19.3),


or on the above line segments (excluding the points on the line segment BF);


the line segment PL is represented by coordinates (x, −0.1135x2+12.112x−280.43, 0.1135x2−13.112x+380.43),


the line segment MA′ is represented by coordinates (x, 0.0016x2−0.9473x+57.497, −0.0016x2−0.0527x+42.503),


the line segment A′B is represented by coordinates (x, 0.0029x2−1.0268x+58.7, −0.0029x2+0.0268x+41.3),


the line segment FT is represented by coordinates (x, 0.0078x2−0.7501x+61.8, −0.0078x2−0.2499x+38.2),


the line segment TP is represented by coordinates (x, 0.00672x2−0.7607x+63.525, −0.00672x2−0.2393x+36.475), and


the line segments LM and BF are straight lines.


A compressor according to a fourteenth aspect is the compressor according to the eighth aspect, wherein, when the mass % of HFO-1132(E), HFO-1123, and R1234yf based on their sum in the refrigerant is respectively represented by x, y, and z, coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R1234yf is 100 mass % are within the range of a figure surrounded by line segments PL, LQ, QR, and RP that connect the following 4 points:


point P (55.8, 42.0, 2.2),


point L (63.1, 31.9, 5.0),


point Q (62.8, 29.6, 7.6), and


point R (49.8, 42.3, 7.9),


or on the above line segments;


the line segment PL is represented by coordinates (x, −0.1135x2+12.112x−280.43, 0.1135x2−13.112x+380.43),


the line segment RP is represented by coordinates (x, 0.00672x2−0.7607x+63.525, −0.00672x2−0.2393x+36.475), and


the line segments LQ and QR are straight lines.


A compressor according to a fifth aspect is the compressor according to the eighth aspect, wherein, when the mass % of HFO-1132(E), HFO-1123, and R1234yf based on their sum in the refrigerant is respectively represented by x, y, and z, coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R1234yf is 100 mass % are within the range of a figure surrounded by line segments SM, MA′, A′B, BF, FT, and TS that connect the following 6 points:


point S (62.6, 28.3, 9.1),


point M (60.3, 6.2, 33.5),


point A′ (30.6, 30.0, 39.4),


point B (0.0, 58.7, 41.3),


point F (0.0, 61.8, 38.2), and


point T (35.8, 44.9, 19.3),


or on the above line segments,


the line segment MA′ is represented by coordinates (x, 0.0016x2−0.9473x+57.497, −0.0016x2−0.0527x+42.503),


the line segment A′B is represented by coordinates (x, 0.0029x2−1.0268x+58.7, −0.0029x2+0.0268x+41.3),


the line segment FT is represented by coordinates (x, 0.0078x2−0.7501x+61.8, −0.0078x2−0.2499x+38.2),


the line segment TS is represented by coordinates (x, −0.0017x2−0.7869x+70.888, −0.0017x2−0.2131x+29.112), and


the line segments SM and BF are straight lines.


A compressor according to a sixth aspect is the compressor according to any of the first through seventh aspects, wherein, the refrigerant comprises trans-1,2-difluoroethylene (HFO-1132(E)) and trifluoroethylene (HFO-1123) in a total amount of 99.5 mass % or more based on the entire refrigerant, and


the refrigerant comprises 62.0 mass % to 72.0 mass % of HFO-1132(E) based on the entire refrigerant.


In this compressor, an induction motor is employed, and thus high power at comparatively low costs can also be achieved when a refrigerant having a sufficiently low GWP, a refrigeration capacity (may also be referred to as a cooling capacity or a capacity) and a coefficient of performance (COP) equal to those of R410A and classified with lower flammability (Class 2L) in the standard of The American Society of Heating, Refrigerating and Air-Conditioning Engineers (ASHRAE) is used.


A compressor according to a seventeenth aspect is the compressor according to any of the first through seventh aspects, wherein, the refrigerant comprises HFO-1132(E) and HFO-1123 in a total amount of 99.5 mass % or more based on the entire refrigerant, and


the refrigerant comprises 45.1 mass % to 47.1 mass % of HFO-1132(E) based on the entire refrigerant.


In this compressor, an induction motor is employed, and thus high power at comparatively low costs can also be achieved when a refrigerant having a sufficiently low GWP, a refrigeration capacity (may also be referred to as a cooling capacity or a capacity) and a coefficient of performance (COP) equal to those of R410A and classified with lower flammability (Class 2L) in the standard of The American Society of Heating, Refrigerating and Air-Conditioning Engineers (ASHRAE) is used.


A compressor according to a eighteenth aspect is the compressor according to any of the first through seventh aspects, wherein, the refrigerant comprises trans-1,2-difluoroethylene (HFO-1132(E)), trifluoroethylene (HFO-1123), 2,3,3,3-tetrafluoro-1-propene (R1234yf), and difluoromethane (R32), wherein


when the mass % of HFO-1132(E), HFO-1123, R1234yf, and R32 based on their sum in the refrigerant is respectively represented by x, y, z, and a,


if 0<a≤11.1, coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R1234yf is (100−a) mass % are within the range of a figure surrounded by straight lines GI, IA, AB, BD′, D′C, and CG that connect the following 6 points:


point G (0.026a2−1.7478a+72.0, −0.026a2+0.7478a+28.0, 0.0),


point I (0.026a2−1.7478a+72.0, 0.0, −0.026a2+0.7478a+28.0),


point A (0.0134a2−1.9681a+68.6, 0.0, −0.0134a2+0.9681a+31.4),


point B (0.0, 0.0144a2−1.6377a+58.7, −0.0144a2+0.6377a+41.3),


point D′ (0.0, 0.0224a2+0.968a+75.4, −0.0224a2−1.968a+24.6), and


point C (−0.2304a2−0.4062a+32.9, 0.2304a2−0.5938a+67.1, 0.0),


or on the straight lines GI, AB, and D′C (excluding point G, point I, point A, point B,


point D′, and point C);


if 11.1<a≤18.2, coordinates (x,y,z) in the ternary composition diagram are within the range of a figure surrounded by straight lines GI, IA, AB, BW, and WG that connect the following 5 points:


point G (0.02a2−1.6013a+71.105, −0.02a2+0.6013a+28.895, 0.0),


point I (0.02a2−1.6013a+71.105, 0.0, −0.02a2+0.6013a+28.895),


point A (0.0112a2−1.9337a+68.484, 0.0, −0.0112a2+0.9337a+31.516),


point B (0.0, 0.0075a2−1.5156a+58.199, −0.0075a2+0.5156a+41.801), and


point W (0.0, 100.0−a, 0.0),


or on the straight lines GI and AB (excluding point G, point I, point A, point B, and point W);


if 18.2<a≤26.7, coordinates (x,y,z) in the ternary composition diagram are within the range of a figure surrounded by straight lines GI, IA, AB, BW, and WG that connect the following 5 points:


point G (0.0135a2−1.4068a+69.727, −0.0135a2+0.4068a+30.273, 0.0),


point I (0.0135a2−1.4068a+69.727, 0.0, −0.0135a2+0.4068a+30.273),


point A (0.0107a2−1.9142a+68.305, 0.0, −0.0107a2+0.9142a+31.695),


point B (0.0, 0.009a2−1.6045a+59.318, −0.009a2+0.6045a+40.682), and


point W (0.0, 100.0−a, 0.0),


or on the straight lines GI and AB (excluding point G, point I, point A, point B, and point W);


if 26.7<a≤36.7, coordinates (x,y,z) in the ternary composition diagram are within the range of a figure surrounded by straight lines GI, IA, AB, BW, and WG that connect the following 5 points:


point G (0.0111a2−1.3152a+68.986, −0.0111a2+0.3152a+31.014, 0.0),


point I (0.0111a2−1.3152a+68.986, 0.0, −0.0111a2+0.3152a+31.014),


point A (0.0103a2−1.9225a+68.793, 0.0, −0.0103a2+0.9225a+31.207),


point B (0.0, 0.0046a2−1.41a+57.286, −0.0046a2+0.41a+42.714), and


point W (0.0, 100.0−a, 0.0),


or on the straight lines GI and AB (excluding point G, point I, point A, point B, and point W); and


if 36.7<a≤46.7, coordinates (x,y,z) in the ternary composition diagram are within the range of a figure surrounded by straight lines GI, IA, AB, BW, and WG that connect the following 5 points:


point G (0.0061a2−0.9918a+63.902, −0.0061a2−0.0082a+36.098, 0.0),


point I (0.0061a2−0.9918a+63.902, 0.0, −0.0061a2−0.0082a+36.098),


point A (0.0085a2−1.8102a+67.1, 0.0, −0.0085a2+0.8102a+32.9),


point B (0.0, 0.0012a2−1.1659a+52.95, −0.0012a2+0.1659a+47.05), and


point W (0.0, 100.0−a, 0.0),


or on the straight lines GI and AB (excluding point G, point I, point A, point B, and point W).


In this compressor, an induction motor is employed, and thus high power at comparatively low costs can also be achieved when a refrigerant having a sufficiently low GWP, a refrigeration capacity (may also be referred to as a cooling capacity or a capacity) and a coefficient of performance (COP) equal to those of R410A is used.


A compressor according to a nineteenth aspect is the compressor according to any of the first through seventh aspects, wherein, the refrigerant comprises trans-1,2-difluoroethylene (HFO-1132(E)), trifluoroethylene (HFO-1123), 2,3,3,3-tetrafluoro-1-propene (R1234yf), and difluoromethane (R32),


wherein


when the mass % of HFO-1132(E), HFO-1123, R1234yf, and R32 based on their sum in the refrigerant is respectively represented by x, y, z, and a,


if 0<a≤11.1, coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R1234yf is (100−a) mass % are within the range of a figure surrounded by straight lines JK′, K′B, BD′, D′C, and CJ that connect the following 5 points:


point J (0.0049a2−0.9645a+47.1, −0.0049a2−0.0355a+52.9, 0.0),


point K′ (0.0514a2−2.4353a+61.7, −0.0323a2+0.4122a+5.9, −0.0191a2+1.0231a+32.4),


point B (0.0, 0.0144a2−1.6377a+58.7, −0.0144a2+0.6377a+41.3),


point D′ (0.0, 0.0224a2+0.968a+75.4, −0.0224a2−1.968a+24.6), and


point C (−0.2304a2−0.4062a+32.9, 0.2304a2−0.5938a+67.1, 0.0),


or on the straight lines JK′, K′B, and D′C (excluding point J, point B, point D′, and point C);


if 11.1<a≤18.2, coordinates (x,y,z) in the ternary composition diagram are within the range of a figure surrounded by straight lines JK′, K′B, BW, and WJ that connect the following 4 points:


point J (0.0243a2−1.4161a+49.725, −0.0243a2+0.4161a+50.275, 0.0),


point K′ (0.0341a2−2.1977a+61.187, −0.0236a2+0.34a+5.636,−0.0105a2+0.8577a+33.177),


point B (0.0, 0.0075a2−1.5156a+58.199, −0.0075a2+0.5156a+41.801), and


point W (0.0, 100.0−a, 0.0),


or on the straight lines JK′ and K′B (excluding point J, point B, and point W);


if 18.2<a≤26.7, coordinates (x,y,z) in the ternary composition diagram are within the range of a figure surrounded by straight lines JK′, K′B, BW, and WJ that connect the following 4 points:


point J (0.0246a2−1.4476a+50.184, −0.0246a2+0.4476a+49.816, 0.0),


point K′ (0.0196a2−1.7863a+58.515, −0.0079a2−0.1136a+8.702, −0.0117a2+0.8999a+32.783),


point B (0.0, 0.009a2−1.6045a+59.318, −0.009a2+0.6045a+40.682), and


point W (0.0, 100.0−a, 0.0),


or on the straight lines JK′ and K′B (excluding point J, point B, and point W);


if 26.7<a≤36.7, coordinates (x,y,z) in the ternary composition diagram are within the range of a figure surrounded by straight lines JK′, K′A, AB, BW, and WJ that connect the following 5 points:


point J (0.0183a2−1.1399a+46.493, −0.0183a2+0.1399a+53.507, 0.0),


point K′ (−0.0051a2+0.0929a+25.95, 0.0, 0.0051a2−1.0929a+74.05),


point A (0.0103a2−1.9225a+68.793, 0.0, −0.0103a2+0.9225a+31.207),


point B (0.0, 0.0046a2−1.41a+57.286, −0.0046a2+0.41a+42.714), and


point W (0.0, 100.0−a, 0.0),


or on the straight lines JK′, K′A, and AB (excluding point J, point B, and point W); and


if 36.7<a≤46.7, coordinates (x,y,z) in the ternary composition diagram are within the range of a figure surrounded by straight lines JK′, K′A, AB, BW, and WJ that connect the following 5 points:


point J (−0.0134a2+1.0956a+7.13, 0.0134a2−2.0956a+92.87, 0.0),


point K′ (−1.892a+29.443, 0.0, 0.892a+70.557),


point A (0.0085a2−1.8102a+67.1, 0.0, −0.0085a2+0.8102a+32.9),


point B (0.0, 0.0012a2−1.1659a+52.95, −0.0012a2+0.1659a+47.05), and


point W (0.0, 100.0−a, 0.0),


or on the straight lines JK′, K′A, and AB (excluding point J, point B, and point W).


In this compressor, an induction motor is employed, and thus high power at comparatively low costs can also be achieved when a refrigerant having a sufficiently low GWP, a refrigeration capacity (may also be referred to as a cooling capacity or a capacity) and a coefficient of performance (COP) equal to those of R410A is used.


A compressor according to a twentieth aspect is the compressor according to any of the first through seventh aspects, wherein the refrigerant comprises trans-1,2-difluoroethylene (HFO-1132(E)), difluoromethane(R32), and 2,3,3,3-tetrafluoro-1-propene (R1234yf),


wherein


when the mass % of HFO-1132(E), R32, and R1234yf based on their sum in the refrigerant is respectively represented by x, y, and z, coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), R32, and R1234yf is 100 mass % are within the range of a figure surrounded by line segments IJ, JN, NE, and EI that connect the following 4 points:


point I (72.0, 0.0, 28.0),


point J (48.5, 18.3, 33.2),


point N (27.7, 18.2, 54.1), and


point E (58.3, 0.0, 41.7),


or on these line segments (excluding the points on the line segment EI;


the line segment IJ is represented by coordinates (0.0236y2−1.7616y+72.0, y, −0.0236y2+0.7616y+28.0);


the line segment NE is represented by coordinates (0.012y2−1.9003y+58.3, y, −0.012y2+0.9003y+41.7); and


the line segments JN and EI are straight lines.


In this compressor, an induction motor is employed, and thus high power at comparatively low costs can also be achieved when a refrigerant having a sufficiently low GWP, a refrigeration capacity (may also be referred to as a cooling capacity or a capacity) equal to those of R410A and classified with lower flammability (Class 2L) in the standard of The American Society of Heating, Refrigerating and Air-Conditioning Engineers (ASHRAE) is used.


A compressor according to a twenty-first aspect is the compressor according to any of the first through seventh aspects, wherein the refrigerant comprises HFO-1132(E), R32, and R1234yf,


wherein


when the mass % of HFO-1132(E), R32, and R1234yf based on their sum in the refrigerant is respectively represented by x, y, and z, coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), R32, and R1234yf is 100 mass % are within the range of a figure surrounded by line segments MM′, M′N, NV, VG, and GM that connect the following 5 points:


point M (52.6, 0.0, 47.4),


point M′ (39.2, 5.0, 55.8),


point N (27.7, 18.2, 54.1),


point V (11.0, 18.1, 70.9), and


point G (39.6, 0.0, 60.4),


or on these line segments (excluding the points on the line segment GM);


the line segment MM′ is represented by coordinates (0.132y2−3.34y+52.6, y, −0.132y2+2.34y+47.4);


the line segment M′N is represented by coordinates (0.0596y2−2.2541y+48.98, y, −0.0596y2+1.2541y+51.02);


the line segment VG is represented by coordinates (0.0123y2−1.8033y+39.6, y, −0.0123y2+0.8033y+60.4); and


the line segments NV and GM are straight lines.


In this compressor, an induction motor is employed, and thus high power at comparatively low costs can also be achieved when a refrigerant having a sufficiently low GWP, a refrigeration capacity (may also be referred to as a cooling capacity or a capacity) equal to those of R410A and classified with lower flammability (Class 2L) in the standard of The American Society of Heating, Refrigerating and Air-Conditioning Engineers (ASHRAE) is used.


A compressor according to a twenty-second aspect is the compressor according to any of the first through seventh aspects, wherein the refrigerant comprises HFO-1132(E), R32, and R1234yf,


wherein


when the mass % of HFO-1132(E), R32, and R1234yf based on their sum in the refrigerant is respectively represented by x, y and z, coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), R32, and R1234yf is 100 mass % are within the range of a figure surrounded by line segments ON, NU, and UO that connect the following 3 points:


point O (22.6, 36.8, 40.6),


point N (27.7, 18.2, 54.1), and


point U (3.9, 36.7, 59.4),


or on these line segments;


the line segment ON is represented by coordinates (0.0072y2−0.6701y+37.512, y, −0.0072y2−0.3299y+62.488);


the line segment NU is represented by coordinates (0.0083y2−1.7403y+56.635, y, −0.0083y2+0.7403y+43.365); and


the line segment UO is a straight line.


In this compressor, an induction motor is employed, and thus high power at comparatively low costs can also be achieved when a refrigerant having a sufficiently low GWP, a refrigeration capacity (may also be referred to as a cooling capacity or a capacity) equal to those of R410A and classified with lower flammability (Class 2L) in the standard of The American Society of Heating, Refrigerating and Air-Conditioning Engineers (ASHRAE) is used.


A compressor according to a twenty-third aspect is the compressor according to any of the first through seventh aspects, wherein the refrigerant comprises HFO-1132(E), R32, and R1234yf,


wherein


when the mass % of HFO-1132(E), R32, and R1234yf based on their sum in the refrigerant is respectively represented by x, y, and z, coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), R32, and R1234yf is 100 mass % are within the range of a figure surrounded by line segments QR, RT, TL, LK, and KQ that connect the following 5 points:


point Q (44.6, 23.0, 32.4),


point R (25.5, 36.8, 37.7),


point T (8.6, 51.6, 39.8),


point L (28.9, 51.7, 19.4), and


point K (35.6, 36.8, 27.6),


or on these line segments;


the line segment QR is represented by coordinates (0.0099y2−1.975y+84.765, y, −0.0099y2+0.975y+15.235);


the line segment RT is represented by coordinates (0.0082y2−1.8683y+83.126, y, −0.0082y2+0.8683y+16.874);


the line segment LK is represented by coordinates (0.0049y2−0.8842y+61.488, y, −0.0049y2−0.1158y+38.512);


the line segment KQ is represented by coordinates (0.0095y2−1.2222y+67.676, y, −0.0095y2+0.2222y+32.324); and


the line segment TL is a straight line.


In this compressor, an induction motor is employed, and thus high power at comparatively low costs can also be achieved when a refrigerant having a sufficiently low GWP, a refrigeration capacity (may also be referred to as a cooling capacity or a capacity) equal to those of R410A and classified with lower flammability (Class 2L) in the standard of The American Society of Heating, Refrigerating and Air-Conditioning Engineers (ASHRAE) is used.


A compressor according to a twenty-fourth aspect is the compressor according to any of the first through seventh aspects, wherein the refrigerant comprises HFO-1132(E), R32, and R1234yf,


wherein


when the mass % of HFO-1132(E), R32, and R1234yf based on their sum in the refrigerant is respectively represented by x, y, and z, coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), R32, and R1234yf is 100 mass % are within the range of a figure surrounded by line segments PS, ST, and TP that connect the following 3 points:


point P (20.5, 51.7, 27.8),


point S (21.9, 39.7, 38.4), and


point T (8.6, 51.6, 39.8),


or on these line segments;


the line segment PS is represented by coordinates (0.0064y2−0.7103y+40.1, y, −0.0064y2−0.2897y+59.9);


the line segment ST is represented by coordinates (0.0082y2−1.8683y+83.126, y, −0.0082y2+0.8683y+16.874); and


the line segment TP is a straight line.


In this compressor, an induction motor is employed, and thus high power at comparatively low costs can also be achieved when a refrigerant having a sufficiently low GWP, a refrigeration capacity (may also be referred to as a cooling capacity or a capacity) equal to those of R410A and classified with lower flammability (Class 2L) in the standard of The American Society of Heating, Refrigerating and Air-Conditioning Engineers (ASHRAE) is used.


A compressor according to a twenty-fifth aspect is the compressor according to any of the first through seventh aspects, wherein the refrigerant comprises trans-1,2-difluoroethylene (HFO-1132(E)), trifluoroethylene (HFO-1123), and difluoromethane (R32),


wherein


when the mass % of HFO-1132(E), HFO-1123, and R32 based on their sum in the refrigerant is respectively represented by x, y, and z, coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R32 is 100 mass % are within the range of a figure surrounded by line segments IK, KB′, B′H, HR, RG, and GI that connect the following 6 points:


point I (72.0, 28.0, 0.0),


point K (48.4, 33.2, 18.4),


point B′ (0.0, 81.6, 18.4),


point H (0.0, 84.2, 15.8),


point R (23.1, 67.4, 9.5), and


point G (38.5, 61.5, 0.0),


or on these line segments (excluding the points on the line segments B′H and GI);


the line segment IK is represented by coordinates (0.025z2−1.7429z+72.00, −0.025z2+0.7429z+28.0, z),


the line segment HR is represented by coordinates (−0.3123z2+4.234z+11.06, 0.3123z2−5.234z+88.94, z),


the line segment RG is represented by coordinates (−0.0491z2−1.1544z+38.5, 0.0491z2+0.1544z+61.5, z), and


the line segments KB′ and GI are straight lines.


In this compressor, an induction motor is employed, and thus high power at comparatively low costs can also be achieved when a refrigerant having a sufficiently low GWP, and a coefficient of performance (COP) equal to that of R410A is used.


A compressor according to a twenty-sixth aspect is the compressor according to any of the first through seventh aspects, wherein the refrigerant comprises HFO-1132(E), HFO-1123, and R32,


wherein


when the mass % of HFO-1132(E), HFO-1123, and R32 based on their sum in the refrigerant is respectively represented by x, y, and z, coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R32 is 100 mass % are within the range of a figure surrounded by line segments IJ, JR, RG, and GI that connect the following 4 points:


point I (72.0, 28.0, 0.0),


point J (57.7, 32.8, 9.5),


point R (23.1, 67.4, 9.5), and


point G (38.5, 61.5, 0.0),


or on these line segments (excluding the points on the line segment GI);


the line segment IJ is represented by coordinates (0.025z2−1.7429z+72.0, −0.025z2+0.7429z+28.0, z),


the line segment RG is represented by coordinates (−0.0491z2−1.1544z+38.5, 0.0491z2+0.1544z+61.5, z), and


the line segments JR and GI are straight lines.


In this compressor, an induction motor is employed, and thus high power at comparatively low costs can also be achieved when a refrigerant having a sufficiently low GWP, and a coefficient of performance (COP) equal to that of R410A is used.


A compressor according to a twenty-seventh aspect is the compressor according to any of the first through seventh aspects, wherein the refrigerant comprises HFO-1132(E), HFO-1123, and R32,


wherein


when the mass % of HFO-1132(E), HFO-1123, and R32 based on their sum in the refrigerant is respectively represented by x, y, and z, coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R32 is 100 mass % are within the range of a figure surrounded by line segments MP, PB′, B′H, HR, RG, and GM that connect the following 6 points:


point M (47.1, 52.9, 0.0),


point P (31.8, 49.8, 18.4),


point B′ (0.0, 81.6, 18.4),


point H (0.0, 84.2, 15.8),


point R (23.1, 67.4, 9.5), and


point G (38.5, 61.5, 0.0),


or on these line segments (excluding the points on the line segments B′H and GM);


the line segment MP is represented by coordinates (0.0083z2−0.984z+47.1, −0.0083z2−0.016z+52.9, z),


the line segment HR is represented by coordinates (−0.3123z2+4.234z+11.06, 0.3123z2−5.234z+88.94, z),


the line segment RG is represented by coordinates (−0.0491z2−1.1544z+38.5, 0.0491z2+0.1544z+61.5, z), and


the line segments PB′ and GM are straight lines.


In this compressor, an induction motor is employed, and thus high power at comparatively low costs can also be achieved when a refrigerant having a sufficiently low GWP, and a coefficient of performance (COP) equal to that of R410A is used.


A compressor according to a twenty-eighth aspect is the compressor according to any of the first through seventh aspects, wherein the refrigerant comprises HFO-1132(E), HFO-1123, and R32,


wherein


when the mass % of HFO-1132(E), HFO-1123, and R32 based on their sum in the refrigerant is respectively represented by x, y, and z, coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R32 is 100 mass % are within the range of a figure surrounded by line segments MN, NR, RG, and GM that connect the following 4 points:


point M (47.1, 52.9, 0.0),


point N (38.5, 52.1, 9.5),


point R (23.1, 67.4, 9.5), and


point G (38.5, 61.5, 0.0),


or on these line segments (excluding the points on the line segment GM);


the line segment MN is represented by coordinates (0.0083z2−0.984z+47.1, −0.0083z2−0.016z+52.9, z),


the line segment RG is represented by coordinates (−0.0491z2−1.1544z+38.5, 0.0491z2+0.1544z+61.5, z), and


the line segments JR and GI are straight lines.


In this compressor, an induction motor is employed, and thus high power at comparatively low costs can also be achieved when a refrigerant having a sufficiently low GWP, and a coefficient of performance (COP) equal to that of R410A is used.


A compressor according to a twenty-ninth aspect is the compressor according to any of the first through seventh aspects, wherein the refrigerant comprises HFO-1132(E), HFO-1123, and R32,


wherein


when the mass % of HFO-1132(E), HFO-1123, and R32 based on their sum in the refrigerant is respectively represented by x, y, and z, coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R32 is 100 mass % are within the range of a figure surrounded by line segments PS, ST, and TP that connect the following 3 points:


point P (31.8, 49.8, 18.4),


point S (25.4, 56.2, 18.4), and


point T (34.8, 51.0, 14.2),


or on these line segments;


the line segment ST is represented by coordinates (−0.0982z2+0.9622z+40.931, 0.0982z2−1.9622z+59.069, z),


the line segment TP is represented by coordinates (0.0083z2−0.984z+47.1, −0.0083z2−0.016z+52.9, z), and


the line segment PS is a straight line.


In this compressor, an induction motor is employed, and thus high power at comparatively low costs can also be achieved when a refrigerant having a sufficiently low GWP, and a coefficient of performance (COP) equal to that of R410A is used.


A compressor according to a thirtieth aspect is the compressor according to any of the first through seventh aspects, wherein the refrigerant comprises HFO-1132(E), HFO-1123, and R32,


wherein


when the mass % of HFO-1132(E), HFO-1123, and R32 based on their sum in the refrigerant is respectively represented by x, y, and z, coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R32 is 100 mass % are within the range of a figure surrounded by line segments QB″, B″D, DU, and UQ that connect the following 4 points:


point Q (28.6, 34.4, 37.0),


point B″ (0.0, 63.0, 37.0),


point D (0.0, 67.0, 33.0), and


point U (28.7, 41.2, 30.1),


or on these line segments (excluding the points on the line segment B″D);


the line segment DU is represented by coordinates (−3.4962z2+210.71z−3146.1, 3.4962z2−211.71z+3246.1, z),


the line segment UQ is represented by coordinates (0.0135z2−0.9181z+44.133, −0.0135z2−0.0819z+55.867, z), and


the line segments QB″ and B″D are straight lines.


In this compressor, an induction motor is employed, and thus high power at comparatively low costs can also be achieved when a refrigerant having a sufficiently low GWP, and a coefficient of performance (COP) equal to that of R410A is used.


A refrigeration cycle apparatus according to a thirty-first aspect is a refrigeration cycle apparatus including any one of the compressors according to the first aspect to the thirtieth aspect.





BRIEF DESCRIPTION OF THE DRAWINGS


FIG. 1 is a schematic view of an instrument used for a flammability test.



FIG. 2 is a diagram showing points A to T and line segments that connect these points in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R1234yf is 100 mass %.



FIG. 3 is a diagram showing points A to C, D′, G, I, J, and K′, and line segments that connect these points to each other in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R1234yf is (100−a) mass %.



FIG. 4 is a diagram showing points A to C, D′, G, I, J, and K′, and line segments that connect these points to each other in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R1234yf is 92.9 mass % (the content of R32 is 7.1 mass %).



FIG. 5 is a diagram showing points A to C, D′, G, I, J, K′, and W, and line segments that connect these points to each other in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R1234yf is 88.9 mass % (the content of R32 is 11.1 mass %).



FIG. 6 is a diagram showing points A, B, G, I, J, K′, and W, and line segments that connect these points to each other in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R1234yf is 85.5 mass % (the content of R32 is 14.5 mass %).



FIG. 7 is a diagram showing points A, B, G, I, J, K′, and W, and line segments that connect these points to each other in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R1234yf is 81.8 mass % (the content of R32 is 18.2 mass %).



FIG. 8 is a diagram showing points A, B, G, I, J, K′, and W, and line segments that connect these points to each other in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R1234yf is 78.1 mass % (the content of R32 is 21.9 mass %).



FIG. 9 is a diagram showing points A, B, G, I, J, K′, and W, and line segments that connect these points to each other in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R1234yf is 73.3 mass % (the content of R32 is 26.7 mass %).



FIG. 10 is a diagram showing points A, B, G, I, J, K′, and W, and line segments that connect these points to each other in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R1234yf is 70.7 mass % (the content of R32 is 29.3 mass %).



FIG. 11 is a diagram showing points A, B, G, I, J, K′, and W, and line segments that connect these points to each other in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R1234yf is 63.3 mass % (the content of R32 is 36.7 mass %).



FIG. 12 is a diagram showing points A, B, G, I, J, K′, and W, and line segments that connect these points to each other in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R1234yf is 55.9 mass % (the content of R32 is 44.1 mass %).



FIG. 13 is a diagram showing points A, B, G, I, J, K′, and W, and line segments that connect these points to each other in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R1234yf is 52.2 mass % (the content of R32 is 47.8 mass %).



FIG. 14 is a view showing points A to C, E, G, and I to W; and line segments that connect points A to C, E, G, and I to W in a ternary composition diagram in which the sum of HFO-1132(E), R32, and R1234yf is 100 mass %.



FIG. 15 is a view showing points A to U; and line segments that connect the points in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R32 is 100 mass %.



FIG. 16 is a refrigeration circuit diagram of an air conditioner in which a compressor according to an embodiment of the present disclosure is utilized.



FIG. 17 is a longitudinal sectional view of the compressor according to an embodiment of the present disclosure.



FIG. 18 is a sectional view of a motor sectioned along a plane perpendicular to an axis.



FIG. 19 is a sectional view of a rotor sectioned along a plane perpendicular to an axis.



FIG. 20 is a perspective view of the rotor.



FIG. 21 is a perspective view of a rotor 71 used in an induction motor of a compressor according to a second modification.



FIG. 22 is a refrigerant circuit diagram of an air conditioner in which a compressor according to a third modification is utilized.



FIG. 23 is a longitudinal sectional view of a compressor according to a second embodiment of the present disclosure.





DESCRIPTION OF EMBODIMENTS
(1) Definition of Terms

In the present specification, the term “refrigerant” includes at least compounds that are specified in ISO 817 (International Organization for Standardization), and that are given a refrigerant number (ASHRAE number) representing the type of refrigerant with “R” at the beginning; and further includes refrigerants that have properties equivalent to those of such refrigerants, even though a refrigerant number is not yet given. Refrigerants are broadly divided into fluorocarbon compounds and non-fluorocarbon compounds in terms of the structure of the compounds. Fluorocarbon compounds include chlorofluorocarbons (CFC), hydrochlorofluorocarbons (HCFC), and hydrofluorocarbons (HFC). Non-fluorocarbon compounds include propane (R290), propylene (R1270), butane (R600), isobutane (R600a), carbon dioxide (R744), ammonia (R717), and the like.


In the present specification, the phrase “composition comprising a refrigerant” at least includes (1) a refrigerant itself (including a mixture of refrigerants), (2) a composition that further comprises other components and that can be mixed with at least a refrigeration oil to obtain a working fluid for a refrigerating machine, and (3) a working fluid for a refrigerating machine containing a refrigeration oil. In the present specification, of these three embodiments, the composition (2) is referred to as a “refrigerant composition” so as to distinguish it from a refrigerant itself (including a mixture of refrigerants). Further, the working fluid for a refrigerating machine (3) is referred to as a “refrigeration oil-containing working fluid” so as to distinguish it from the “refrigerant composition.”


In the present specification, when the term “alternative” is used in a context in which the first refrigerant is replaced with the second refrigerant, the first type of “alternative” means that equipment designed for operation using the first refrigerant can be operated using the second refrigerant under optimum conditions, optionally with changes of only a few parts (at least one of the following: refrigeration oil, gasket, packing, expansion valve, dryer, and other parts) and equipment adjustment. In other words, this type of alternative means that the same equipment is operated with an alternative refrigerant. Embodiments of this type of “alternative” include “drop-in alternative,” “nearly drop-in alternative,” and “retrofit,” in the order in which the extent of changes and adjustment necessary for replacing the first refrigerant with the second refrigerant is smaller.


The term “alternative” also includes a second type of “alternative,” which means that equipment designed for operation using the second refrigerant is operated for the same use as the existing use with the first refrigerant by using the second refrigerant. This type of alternative means that the same use is achieved with an alternative refrigerant.


In the present specification, the term “refrigerating machine” refers to machines in general that draw heat from an object or space to make its temperature lower than the temperature of ambient air, and maintain a low temperature. In other words, refrigerating machines refer to conversion machines that gain energy from the outside to do work, and that perform energy conversion, in order to transfer heat from where the temperature is lower to where the temperature is higher.


In the present specification, a refrigerant having a “WCF lower flammability” means that the most flammable composition (worst case of formulation for flammability: WCF) has a burning velocity of 10 cm/s or less according to the US ANSI/ASHRAE Standard 34-2013. Further, in the present specification, a refrigerant having “ASHRAE lower flammability” means that the burning velocity of WCF is 10 cm/s or less, that the most flammable fraction composition (worst case of fractionation for flammability: WCFF), which is specified by performing a leakage test during storage, shipping, or use based on ANSI/ASHRAE 34-2013 using WCF, has a burning velocity of 10 cm/s or less, and that flammability classification according to the US ANSI/ASHRAE Standard 34-2013 is determined to classified as be “Class 2L.”


In the present specification, a refrigerant having an “RCL of x % or more” means that the refrigerant has a refrigerant concentration limit (RCL), calculated in accordance with the US ANSI/ASHRAE Standard 34-2013, of x % or more. RCL refers to a concentration limit in the air in consideration of safety factors. RCL is an index for reducing the risk of acute toxicity, suffocation, and flammability in a closed space where humans are present. RCL is determined in accordance with the ASHRAE Standard. More specifically, RCL is the lowest concentration among the acute toxicity exposure limit (ATEL), the oxygen deprivation limit (ODL), and the flammable concentration limit (FCL), which are respectively calculated in accordance with sections 7.1.1, 7.1.2, and 7.1.3 of the ASHRAE Standard.


In the present specification, temperature glide refers to an absolute value of the difference between the initial temperature and the end temperature in the phase change process of a composition containing the refrigerant of the present disclosure in the heat exchanger of a refrigerant system.


(2) Refrigerant
(2-1) Refrigerant Component

Any one of various refrigerants such as refrigerant A, refrigerant B, refrigerant C, refrigerant D, and refrigerant E, details of these refrigerant are to be mentioned later, can be used as the refrigerant.


(2-2) Use of Refrigerant

The refrigerant according to the present disclosure can be preferably used as a working fluid in a refrigerating machine.


The composition according to the present disclosure is suitable for use as an alternative refrigerant for HFC refrigerant such as R410A, R407C and R404 etc, or HCFC refrigerant such as R22 etc.


(3) Refrigerant Composition

The refrigerant composition according to the present disclosure comprises at least the refrigerant according to the present disclosure, and can be used for the same use as the refrigerant according to the present disclosure. Moreover, the refrigerant composition according to the present disclosure can be further mixed with at least a refrigeration oil to thereby obtain a working fluid for a refrigerating machine.


The refrigerant composition according to the present disclosure further comprises at least one other component in addition to the refrigerant according to the present disclosure. The refrigerant composition according to the present disclosure may comprise at least one of the following other components, if necessary. As described above, when the refrigerant composition according to the present disclosure is used as a working fluid in a refrigerating machine, it is generally used as a mixture with at least a refrigeration oil. Therefore, it is preferable that the refrigerant composition according to the present disclosure does not substantially comprise a refrigeration oil. Specifically, in the refrigerant composition according to the present disclosure, the content of the refrigeration oil based on the entire refrigerant composition is preferably 0 to 1 mass %, and more preferably 0 to 0.1 mass %.


(3-1) Water

The refrigerant composition according to the present disclosure may contain a small amount of water. The water content of the refrigerant composition is preferably 0.1 mass % or less based on the entire refrigerant. A small amount of water contained in the refrigerant composition stabilizes double bonds in the molecules of unsaturated fluorocarbon compounds that can be present in the refrigerant, and makes it less likely that the unsaturated fluorocarbon compounds will be oxidized, thus increasing the stability of the refrigerant composition.


(3-2) Tracer

A tracer is added to the refrigerant composition according to the present disclosure at a detectable concentration such that when the refrigerant composition has been diluted, contaminated, or undergone other changes, the tracer can trace the changes.


The refrigerant composition according to the present disclosure may comprise a single tracer, or two or more tracers.


The tracer is not limited, and can be suitably selected from commonly used tracers. Preferably, a compound that cannot be an impurity inevitably mixed in the refrigerant of the present disclosure is selected as the tracer.


Examples of tracers include hydrofluorocarbons, hydrochlorofluorocarbons, chlorofluorocarbons, hydrochlorocarbons, fluorocarbons, deuterated hydrocarbons, deuterated hydrofluorocarbons, perfluorocarbons, fluoroethers, brominated compounds, iodinated compounds, alcohols, aldehydes, ketones, and nitrous oxide (N2O). The tracer is particularly preferably a hydrofluorocarbon, a hydrochlorofluorocarbon, a chlorofluorocarbon, a fluorocarbon, a hydrochlorocarbon, a fluorocarbon, or a fluoroether.


The following compounds are preferable as the tracer.


FC-14 (tetrafluoromethane, CF4)


HCC-40 (chloromethane, CH3Cl)


HFC-23 (trifluoromethane, CHF3)


HFC-41 (fluoromethane, CH3Cl)


HFC-125 (pentafluoroethane, CF3CHF2)


HFC-134a (1,1,1,2-tetrafluoroethane, CF3CH2F)


HFC-134 (1,1,2,2-tetrafluoroethane, CHF2CHF2)


HFC-143a (1,1,1-trifluoroethane, CF3CH3)


HFC-143 (1,1,2-trifluoroethane, CHF2CH2F)


HFC-152a (1,1-difluoroethane, CHF2CH3)


HFC-152 (1,2-difluoroethane, CH2FCH2F)


HFC-161 (fluoroethane, CH3CH2F)


HFC-245fa (1,1,1,3,3-pentafluoropropane, CF3CH2CHF2)


HFC-236fa (1,1,1,3,3,3-hexafluoropropane, CF3CH2CF3)


HFC-236ea (1,1,1,2,3,3-hexafluoropropane, CF3CHFCHF2)


HFC-227ea (1,1,1,2,3,3,3-heptafluoropropane, CF3CHFCF3)


HCFC-22 (chlorodifluoromethane, CHClF2)


HCFC-31 (chlorofluoromethane, CH2ClF)


CFC-1113 (chlorotrifluoroethylene, CF2═CClF)


HFE-125 (trifluoromethyl-difluoromethyl ether, CF3OCHF2)


HFE-134a (trifluoromethyl-fluoromethyl ether, CF3OCH2F)


HFE-143a (trifluoromethyl-methyl ether, CF3OCH3)


HFE-227ea (trifluoromethyl-tetrafluoroethyl ether, CF3OCHFCF3)


HFE-236fa (trifluoromethyl-trifluoroethyl ether, CF3OCH2CF3)


The tracer compound may be present in the refrigerant composition at a total concentration of about 10 parts per million (ppm) to about 1000 ppm. Preferably, the tracer compound is present in the refrigerant composition at a total concentration of about 30 ppm to about 500 ppm, and most preferably, the tracer compound is present at a total concentration of about 50 ppm to about 300 ppm.


(3-3) Ultraviolet Fluorescent Dye

The refrigerant composition according to the present disclosure may comprise a single ultraviolet fluorescent dye, or two or more ultraviolet fluorescent dyes.


The ultraviolet fluorescent dye is not limited, and can be suitably selected from commonly used ultraviolet fluorescent dyes.


Examples of ultraviolet fluorescent dyes include naphthalimide, coumarin, anthracene, phenanthrene, xanthene, thioxanthene, naphthoxanthene, fluorescein, and derivatives thereof. The ultraviolet fluorescent dye is particularly preferably either naphthalimide or coumarin, or both.


(3-4) Stabilizer

The refrigerant composition according to the present disclosure may comprise a single stabilizer, or two or more stabilizers.


The stabilizer is not limited, and can be suitably selected from commonly used stabilizers.


Examples of stabilizers include nitro compounds, ethers, and amines.


Examples of nitro compounds include aliphatic nitro compounds, such as nitromethane and nitroethane; and aromatic nitro compounds, such as nitro benzene and nitro styrene.


Examples of ethers include 1,4-dioxane.


Examples of amines include 2,2,3,3,3-pentafluoropropylamine and diphenylamine.


Examples of stabilizers also include butylhydroxyxylene and benzotriazole.


The content of the stabilizer is not limited. Generally, the content of the stabilizer is preferably 0.01 to 5 mass %, and more preferably 0.05 to 2 mass %, based on the entire refrigerant.


(3-5) Polymerization Inhibitor

The refrigerant composition according to the present disclosure may comprise a single polymerization inhibitor, or two or more polymerization inhibitors.


The polymerization inhibitor is not limited, and can be suitably selected from commonly used polymerization inhibitors.


Examples of polymerization inhibitors include 4-methoxy-1-naphthol, hydroquinone, hydroquinone methyl ether, dimethyl-t-butylphenol, 2,6-di-tert-butyl-p-cresol, and benzotriazole.


The content of the polymerization inhibitor is not limited. Generally, the content of the polymerization inhibitor is preferably 0.01 to 5 mass %, and more preferably 0.05 to 2 mass %, based on the entire refrigerant.


(4) Refrigeration Oil-Containing Working Fluid

The refrigeration oil-containing working fluid according to the present disclosure comprises at least the refrigerant or refrigerant composition according to the present disclosure and a refrigeration oil, for use as a working fluid in a refrigerating machine. Specifically, the refrigeration oil-containing working fluid according to the present disclosure is obtained by mixing a refrigeration oil used in a compressor of a refrigerating machine with the refrigerant or the refrigerant composition. The refrigeration oil-containing working fluid generally comprises 10 to 50 mass % of refrigeration oil.


(4-1) Refrigeration Oil

The refrigeration oil is not limited, and can be suitably selected from commonly used refrigeration oils. In this case, refrigeration oils that are superior in the action of increasing the miscibility with the mixture and the stability of the mixture, for example, are suitably selected as necessary.


The base oil of the refrigeration oil is preferably, for example, at least one member selected from the group consisting of polyalkylene glycols (PAG), polyol esters (POE), and polyvinyl ethers (PVE).


The refrigeration oil may further contain additives in addition to the base oil. The additive may be at least one member selected from the group consisting of antioxidants, extreme-pressure agents, acid scavengers, oxygen scavengers, copper deactivators, rust inhibitors, oil agents, and antifoaming agents.


A refrigeration oil with a kinematic viscosity of 5 to 400 cSt at 40° C. is preferable from the standpoint of lubrication.


The refrigeration oil-containing working fluid according to the present disclosure may further optionally contain at least one additive. Examples of additives include compatibilizing agents described below.


(4-2) Compatibilizing Agent

The refrigeration oil-containing working fluid according to the present disclosure may comprise a single compatibilizing agent, or two or more compatibilizing agents.


The compatibilizing agent is not limited, and can be suitably selected from commonly used compatibilizing agents.


Examples of compatibilizing agents include polyoxyalkylene glycol ethers, amides, nitriles, ketones, chlorocarbons, esters, lactones, aryl ethers, fluoroethers, and 1,1,1-trifluoroalkanes. The compatibilizing agent is particularly preferably a polyoxyalkylene glycol ether.


(5) Various Refrigerants

Hereinafter, the refrigerants A to E, which are the refrigerants used in the present embodiment, will be described in detail.


In addition, each description of the following refrigerant A, refrigerant B, refrigerant C, refrigerant D, and refrigerant E is each independent. The alphabet which shows a point or a line segment, the number of an Examples, and the number of a comparative examples are all independent of each other among the refrigerant A, the refrigerant B, the refrigerant C, the refrigerant D, and the refrigerant E. For example, the first embodiment of the refrigerant A and the first embodiment of the refrigerant B are different embodiment from each other.


(5-1) Refrigerant A

The refrigerant A according to the present disclosure is a mixed refrigerant comprising trans-1,2-difluoroethylene (HFO-1132(E)), trifluoroethylene (HFO-1123), and 2,3,3,3-tetrafluoro-1-propene (R1234yf).


The refrigerant A according to the present disclosure has various properties that are desirable as an R410A-alternative refrigerant, i.e., a refrigerating capacity and a coefficient of performance that are equivalent to those of R410A, and a sufficiently low GWP.


The refrigerant A according to the present disclosure is a composition comprising HFO-1132(E) and R1234yf, and optionally further comprising HFO-1123, and may further satisfy the following requirements. This refrigerant also has various properties desirable as an alternative refrigerant for R410A; i.e., it has a refrigerating capacity and a coefficient of performance that are equivalent to those of R410A, and a sufficiently low GWP.


Requirements

Preferable refrigerant A is as follows:


When the mass % of HFO-1132(E), HFO-1123, and R1234yf based on their sum in the refrigerant is respectively represented by x, y, and z, coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R1234yf is 100 mass % are within the range of a figure surrounded by line segments AA′, A′B, BD, DC′, C′C, CO, and OA that connect the following 7 points:


point A (68.6, 0.0, 31.4),


point A′ (30.6, 30.0, 39.4),


point B (0.0, 58.7, 41.3),


point D (0.0, 80.4, 19.6),


point C′ (19.5, 70.5, 10.0),


point C (32.9, 67.1, 0.0), and


point O (100.0, 0.0, 0.0),


or on the above line segments (excluding the points on the line CO);


the line segment AA′ is represented by coordinates (x, 0.0016x2−0.9473x+57.497, −0.0016x2−0.0527x+42.503),


the line segment A′B is represented by coordinates (x, 0.0029x2−1.0268x+58.7, −0.0029x2+0.0268x+41.3,


the line segment DC′ is represented by coordinates (x, 0.0082x2−0.6671x+80.4, −0.0082x2−0.3329x+19.6),


the line segment C′C is represented by coordinates (x, 0.0067x2−0.6034x+79.729, −0.0067x2−0.3966x+20.271), and


the line segments BD, CO, and OA are straight lines.


When the requirements above are satisfied, the refrigerant according to the present disclosure has a refrigerating capacity ratio of 85% or more relative to that of R410A, and a COP of 92.5% or more relative to that of R410A.


When the mass % of HFO-1132(E), HFO-1123, and R1234yf, based on their sum in the refrigerant A according to the present disclosure is respectively represented by x, y, and z, the refrigerant is preferably a refrigerant wherein coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R1234yf is 100 mass % are within a figure surrounded by line segments GI, IA, AA′, A′B, BD, DC′, C′C, and CG that connect the following 8 points:


point G (72.0, 28.0, 0.0),


point I (72.0, 0.0, 28.0),


point A (68.6, 0.0, 31.4),


point A′ (30.6, 30.0, 39.4),


point B (0.0, 58.7, 41.3),


point D (0.0, 80.4, 19.6),


point C′ (19.5, 70.5, 10.0), and


point C (32.9, 67.1, 0.0),


or on the above line segments (excluding the points on the line segment CG);


the line segment AA′ is represented by coordinates (x, 0.0016x2−0.9473x+57.497, −0.0016x2−0.0527x+42.503),


the line segment A′B is represented by coordinates (x, 0.0029x2−1.0268x+58.7, −0.0029x2+0.0268x+41.3),


the line segment DC′ is represented by coordinates (x, 0.0082x2−0.6671x+80.4, −0.0082x2−0.3329x+19.6),


the line segment C′C is represented by coordinates (x, 0.0067x2−0.6034x+79.729, −0.0067x2−0.3966x+20.271), and


the line segments GI, IA, BD, and CG are straight lines.


When the requirements above are satisfied, the refrigerant A according to the present disclosure has a refrigerating capacity ratio of 85% or more relative to that of R410A, and a COP of 92.5% or more relative to that of R410A; furthermore, the refrigerant A has a WCF lower flammability according to the ASHRAE Standard (the WCF composition has a burning velocity of 10 cm/s or less).


When the mass % of HFO-1132(E), HFO-1123, and R1234yf based on their sum in the refrigerant according to the present disclosure is respectively represented by x, y, and z, the refrigerant is preferably a refrigerant wherein coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R1234yf is 100 mass % are within the range of a figure surrounded by line segments JP, PN, NK, KA′, A′B, BD, DC′, C′C, and CJ that connect the following 9 points:


point J (47.1, 52.9, 0.0),


point P (55.8, 42.0, 2.2),


point N (68.6, 16.3, 15.1),


point K (61.3, 5.4, 33.3),


point A′ (30.6, 30.0, 39.4),


point B (0.0, 58.7, 41.3),


point D (0.0, 80.4, 19.6),


point C′ (19.5, 70.5, 10.0), and


point C (32.9, 67.1, 0.0),


or on the above line segments (excluding the points on the line segment CJ);


the line segment PN is represented by coordinates (x, −0.1135x2+12.112x−280.43, 0.1135x2−13.112x+380.43),


the line segment NK is represented by coordinates (x, 0.2421x2−29.955x+931.91, −0.2421x2+28.955x−831.91),


the line segment KA′ is represented by coordinates (x, 0.0016x2−0.9473x+57.497, −0.0016x2−0.0527x+42.503),


the line segment A′B is represented by coordinates (x, 0.0029x2−1.0268x+58.7, −0.0029x2+0.0268x+41.3),


the line segment DC′ is represented by coordinates (x, 0.0082x2−0.6671x+80.4, −0.0082x2−0.3329x+19.6),


the line segment C′C is represented by coordinates (x, 0.0067x2−0.6034x+79.729, −0.0067x2−0.3966x+20.271), and


the line segments JP, BD, and CG are straight lines.


When the requirements above are satisfied, the refrigerant A according to the present disclosure has a refrigerating capacity ratio of 85% or more relative to that of R410A, and a COP of 92.5% or more relative to that of R410A; furthermore, the refrigerant exhibits a lower flammability (Class 2L) according to the ASHRAE Standard (the WCF composition and the WCFF composition have a burning velocity of 10 cm/s or less).


When the mass % of HFO-1132(E), HFO-1123, and R1234yf based on their sum in the refrigerant according to the present disclosure is respectively represented by x, y, and z, the refrigerant is preferably a refrigerant wherein coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R1234yf is 100 mass % are within the range of a figure surrounded by line segments JP, PL, LM, MA′, A′B, BD, DC′, C′C, and CJ that connect the following 9 points:


point J (47.1, 52.9, 0.0),


point P (55.8, 42.0, 2.2),


point L (63.1, 31.9, 5.0),


point M (60.3, 6.2, 33.5),


point A′ (30.6, 30.0, 39.4),


point B (0.0, 58.7, 41.3),


point D (0.0, 80.4, 19.6),


point C′ (19.5, 70.5, 10.0), and


point (32.9, 67.1, 0.0),


or on the above line segments (excluding the points on the line segment CJ);


the line segment PL is represented by coordinates (x, −0.1135x2+12.112x−280.43, 0.1135x2−13.112x+380.43),


the line segment MA′ is represented by coordinates (x, 0.0016x2−0.9473x+57.497, −0.0016x2−0.0527x+42.503),


the line segment A′B is represented by coordinates (x, 0.0029x2−1.0268x+58.7, −0.0029x2+0.0268x+41.3),


the line segment DC′ is represented by coordinates (x, 0.0082x2−0.6671x+80.4, −0.0082x2−0.3329x+19.6),


the line segment C′C is represented by coordinates (x, 0.0067x2−0.6034x+79.729, −0.0067x2−0.3966x+20.271), and


the line segments JP, LM, BD, and CG are straight lines.


When the requirements above are satisfied, the refrigerant according to the present disclosure has a refrigerating capacity ratio of 85% or more relative to that of R410A, and a COP of 92.5% or more relative to that of R410A; furthermore, the refrigerant has an RCL of 40 g/m3 or more.


When the mass % of HFO-1132(E), HFO-1123, and R1234yf based on their sum in the refrigerant A according to the present disclosure is respectively represented by x, y, and z, the refrigerant is preferably a refrigerant wherein coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R1234yf is 100 mass % are within the range of a figure surrounded by line segments PL, LM, MA′, A′B, BF, FT, and TP that connect the following 7 points:


point P (55.8, 42.0, 2.2),


point L (63.1, 31.9, 5.0),


point M (60.3, 6.2, 33.5),


point A′ (30.6, 30.0, 39.4),


point B (0.0, 58.7, 41.3),


point F (0.0, 61.8, 38.2), and


point T (35.8, 44.9, 19.3),


or on the above line segments (excluding the points on the line segment BF);


the line segment PL is represented by coordinates (x, −0.1135x2+12.112x−280.43, 0.1135x2−13.112x+380.43),


the line segment MA′ is represented by coordinates (x, 0.0016x2−0.9473x+57.497, −0.0016x2−0.0527x+42.503),


the line segment A′B is represented by coordinates (x, 0.0029x2−1.0268x+58.7, −0.0029x2+0.0268x+41.3),


the line segment FT is represented by coordinates (x, 0.0078x2−0.7501x+61.8, −0.0078x2−0.2499x+38.2),


the line segment TP is represented by coordinates (x, 0.00672x2−0.7607x+63.525, −0.00672x2−0.2393x+36.475), and


the line segments LM and BF are straight lines.


When the requirements above are satisfied, the refrigerant according to the present disclosure has a refrigerating capacity ratio of 85% or more relative to that of R410A, and a COP of 95% or more relative to that of R410A; furthermore, the refrigerant has an RCL of 40 g/m3 or more.


The refrigerant A according to the present disclosure is preferably a refrigerant wherein when the mass % of HFO-1132(E), HFO-1123, and R1234yf based on their sum in the refrigerant is respectively represented by x, y, and z, coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R1234yf is 100 mass % are within the range of a figure surrounded by line segments PL, LQ, QR, and RP that connect the following 4 points:


point P (55.8, 42.0, 2.2),


point L (63.1, 31.9, 5.0),


point Q (62.8, 29.6, 7.6), and


point R (49.8, 42.3, 7.9),


or on the above line segments;


the line segment PL is represented by coordinates (x, −0.1135x2+12.112x−280.43, 0.1135x2−13.112x+380.43),


the line segment RP is represented by coordinates (x, 0.00672x2−0.7607x+63.525, −0.00672x2−0.2393x+36.475), and


the line segments LQ and QR are straight lines.


When the requirements above are satisfied, the refrigerant according to the present disclosure has a COP of 95% or more relative to that of R410A, and an RCL of 40 g/m3 or more, furthermore, the refrigerant has a condensation temperature glide of 1° C. or less.


The refrigerant A according to the present disclosure is preferably a refrigerant wherein when the mass % of HFO-1132(E), HFO-1123, and R1234yf based on their sum in the refrigerant is respectively represented by x, y, and z, coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R1234yf is 100 mass % are within the range of a figure surrounded by line segments SM, MA′, A′B, BF, FT, and TS that connect the following 6 points:


point S (62.6, 28.3, 9.1),


point M (60.3, 6.2, 33.5),


point A′(30.6, 30.0, 39.4),


point B (0.0, 58.7, 41.3),


point F (0.0, 61.8, 38.2), and


point T (35.8, 44.9, 19.3),


or on the above line segments,


the line segment MA′ is represented by coordinates (x, 0.0016x2−0.9473x+57.497, −0.0016x2−0.0527x+42.503),


the line segment A′B is represented by coordinates (x, 0.0029x2−1.0268x+58.7, −0.0029x2+0.0268x+41.3),


the line segment FT is represented by coordinates (x, 0.0078x2−0.7501x+61.8, −0.0078x2−0.2499x+38.2),


the line segment TS is represented by coordinates (x, −0.0017x2−0.7869x+70.888, −0.0017x2−0.2131x+29.112), and


the line segments SM and BF are straight lines.


When the requirements above are satisfied, the refrigerant according to the present disclosure has a refrigerating capacity ratio of 85% or more relative to that of R410A, a COP of 95% or more relative to that of R410A, and an RCL of 40 g/m3 or more furthermore, the refrigerant has a discharge pressure of 105% or more relative to that of R410A.


The refrigerant A according to the present disclosure is preferably a refrigerant wherein when the mass % of HFO-1132(E), HFO-1123, and R1234yf based on their sum in the refrigerant is respectively represented by x, y, and z, coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R1234yf is 100 mass % are within the range of a figure surrounded by line segments Od, dg, gh, and hO that connect the following 4 points:


point d (87.6, 0.0, 12.4),


point g (18.2, 55.1, 26.7),


point h (56.7, 43.3, 0.0), and


point o (100.0, 0.0, 0.0),


or on the line segments Od, dg, gh, and hO (excluding the points 0 and h);


the line segment dg is represented by coordinates (0.0047y2−1.5177y+87.598, y, −0.0047y2+0.5177y+12.402),


the line segment gh is represented by coordinates (−0.0134z2−1.0825z+56.692, 0.0134z2+0.0825z+43.308, z), and


the line segments hO and Od are straight lines.


When the requirements above are satisfied, the refrigerant according to the present disclosure has a refrigerating capacity ratio of 92.5% or more relative to that of R410A, and a COP ratio of 92.5% or more relative to that of R410A.


The refrigerant A according to the present disclosure is preferably a refrigerant wherein


when the mass % of HFO-1132(E), HFO-1123, and R1234yf, based on their sum is respectively represented by x, y, and z, coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R1234yf is 100 mass % are within the range of a figure surrounded by line segments lg, gh, hi, and il that connect the following 4 points:


point 1 (72.5, 10.2, 17.3),


point g (18.2, 55.1, 26.7),


point h (56.7, 43.3, 0.0), and


point i (72.5, 27.5, 0.0) or


on the line segments lg, gh, and il (excluding the points h and i);


the line segment lg is represented by coordinates (0.0047y2−1.5177y+87.598, y, −0.0047y2+0.5177y+12.402),


the line gh is represented by coordinates (−0.0134z2−1.0825z+56.692, 0.0134z2+0.0825z+43.308, z), and


the line segments hi and il are straight lines.


When the requirements above are satisfied, the refrigerant according to the present disclosure has a refrigerating capacity ratio of 92.5% or more relative to that of R410A, and a COP ratio of 92.5% or more relative to that of R410A; furthermore, the refrigerant has a lower flammability (Class 2L) according to the ASHRAE Standard.


The refrigerant A according to the present disclosure is preferably a refrigerant wherein


when the mass % of HFO-1132(E), HFO-1123, and R1234yf based on their sum is respectively represented by x, y, and z, coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R1234yf is 100 mass % are within the range of a figure surrounded by line segments Od, de, ef, and fO that connect the following 4 points:


point d (87.6, 0.0, 12.4),


point e (31.1, 42.9, 26.0),


point f (65.5, 34.5, 0.0), and


point O (100.0, 0.0, 0.0),


or on the line segments Od, de, and ef (excluding the points O and f);


the line segment de is represented by coordinates (0.0047y2−1.5177y+87.598, y, −0.0047y2+0.5177y+12.402),


the line segment ef is represented by coordinates (−0.0064z2−1.1565z+65.501, 0.0064z2+0.1565z+34.499, z), and


the line segments fO and Od are straight lines.


When the requirements above are satisfied, the refrigerant according to the present disclosure has a refrigerating capacity ratio of 93.5% or more relative to that of R410A, and a COP ratio of 93.5% or more relative to that of R410A.


The refrigerant A according to the present disclosure is preferably a refrigerant wherein


when the mass % of HFO-1132(E), HFO-1123, and R1234yf based on their sum is respectively represented by x, y, and z,


coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R1234yf is 100 mass % are within the range of a figure surrounded by line segments le, ef, fi, and il that connect the following 4 points:


point l (72.5, 10.2, 17.3),


point e (31.1, 42.9, 26.0),


point f (65.5, 34.5, 0.0), and


point i (72.5, 27.5, 0.0),


or on the line segments le, ef, and il (excluding the points f and i);


the line segment le is represented by coordinates (0.0047y2−1.5177y+87.598, y, −0.0047y2+0.5177y+12.402),


the line segment ef is represented by coordinates (−0.0134z2−1.0825z+56.692, 0.0134z2+0.0825z+43.308, z), and


the line segments fi and il are straight lines.


When the requirements above are satisfied, the refrigerant according to the present disclosure has a refrigerating capacity ratio of 93.5% or more relative to that of R410A, and a COP ratio of 93.5% or more relative to that of R410A; furthermore, the refrigerant has a lower flammability (Class 2L) according to the ASHRAE Standard.


The refrigerant A according to the present disclosure is preferably a refrigerant wherein


when the mass % of HFO-1132(E), HFO-1123, and R1234yf based on their sum is respectively represented by x, y, and z,


coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R1234yf is 100 mass % are within the range of a figure surrounded by line segments Oa, ab, bc, and cO that connect the following 4 points:


point a (93.4, 0.0, 6.6),


point b (55.6, 26.6, 17.8),


point c (77.6, 22.4, 0.0), and


point O (100.0, 0.0, 0.0),


or on the line segments Oa, ab, and bc (excluding the points O and c);


the line segment ab is represented by coordinates (0.0052y2−1.5588y+93.385, y, −0.0052y2+0.5588y+6.615),


the line segment bc is represented by coordinates (−0.0032z2−1.1791z+77.593, 0.0032z2+0.1791z+22.407, z), and


the line segments cO and Oa are straight lines.


When the requirements above are satisfied, the refrigerant according to the present disclosure has a refrigerating capacity ratio of 95% or more relative to that of R410A, and a COP ratio of 95% or more relative to that of R410A.


The refrigerant A according to the present disclosure is preferably a refrigerant wherein


when the mass % of HFO-1132(E), HFO-1123, and R1234yf based on their sum is respectively represented by x, y, and z,


coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R1234yf is 100 mass % are within the range of a figure surrounded by line segments kb, bj, and jk that connect the following 3 points:


point k (72.5, 14.1, 13.4),


point b (55.6, 26.6, 17.8), and


point j (72.5, 23.2, 4.3),


or on the line segments kb, bj, and jk;


the line segment kb is represented by coordinates (0.0052y2−1.5588y+93.385, y, and −0.0052y2+0.5588y+6.615),


the line segment bj is represented by coordinates (−0.0032z2−1.1791z+77.593, 0.0032z2+0.1791z+22.407, z), and


the line segment jk is a straight line.


When the requirements above are satisfied, the refrigerant according to the present disclosure has a refrigerating capacity ratio of 95% or more relative to that of R410A, and a COP ratio of 95% or more relative to that of R410A; furthermore, the refrigerant has a lower flammability (Class 2L) according to the ASHRAE Standard.


The refrigerant according to the present disclosure may further comprise other additional refrigerants in addition to HFO-1132(E), HFO-1123, and R1234yf, as long as the above properties and effects are not impaired. In this respect, the refrigerant according to the present disclosure preferably comprises HFO-1132(E), HFO-1123, and R1234yf in a total amount of 99.5 mass % or more, more preferably 99.75 mass % or more, and still more preferably 99.9 mass % or more, based on the entire refrigerant.


The refrigerant according to the present disclosure may comprise HFO-1132(E), HFO-1123, and R1234yf in a total amount of 99.5 mass % or more, 99.75 mass % or more, or 99.9 mass % or more, based on the entire refrigerant.


Additional refrigerants are not particularly limited and can be widely selected. The mixed refrigerant may contain one additional refrigerant, or two or more additional refrigerants.


(Examples of Refrigerant A)

The present disclosure is described in more detail below with reference to Examples of refrigerant A. However, refrigerant A is not limited to the Examples.


The GWP of R1234yf and a composition consisting of a mixed refrigerant R410A (R32=50%/R125=50%) was evaluated based on the values stated in the Intergovernmental Panel on Climate Change (IPCC), fourth report. The GWP of HFO-1132(E), which was not stated therein, was assumed to be 1 from HFO-1132a (GWP=1 or less) and HFO-1123 (GWP=0.3, described in WO2015/141678). The refrigerating capacity of R410A and compositions each comprising a mixture of HFO-1132(E), HFO-1123, and R1234yf was determined by performing theoretical refrigeration cycle calculations for the mixed refrigerants using the National Institute of Science and Technology (NIST) and Reference Fluid Thermodynamic and Transport Properties Database (Refprop 9.0) under the following conditions.


Further, the RCL of the mixture was calculated with the LFL of HFO-1132(E) being 4.7 vol. %, the LFL of HFO-1123 being 10 vol. %, and the LFL of R1234yf being 6.2 vol. %, in accordance with the ASHRAE Standard 34-2013.


Evaporating temperature: 5° C.


Condensation temperature: 45° C.


Degree of superheating: 5 K


Degree of subcooling: 5 K


Compressor efficiency: 70%


Tables 1 to 34 show these values together with the GWP of each mixed refrigerant.

















TABLE 1








Comp.
Comp.

Example

Comp.




Comp.
Ex. 2
Ex. 3
Example
2
Example
Ex. 4


Item
Unit
Ex. 1
O
A
1
A′
3
B























HFO-1132(E)
mass %
R410A
100.0
68.6
49.0
30.6
14.1
0.0


HFO-1123
mass %

0.0
0.0
14.9
30.0
44.8
58.7


R1234yf
mass %

0.0
31.4
36.1
39.4
41.1
41.3


GWP

2088
1
2
2
2
2
2


COP ratio
% (relative
100
99.7
100.0
98.6
97.3
96.3
95.5



to 410A)









Refrigerating
% (relative
100
98.3
85.0
85.0
85.0
85.0
85.0


capacity ratio
to 410A)









Condensation
° C.
0.1
0.00
1.98
3.36
4.46
5.15
5.35


glide










Discharge
% (relative
100.0
99.3
87.1
88.9
90.6
92.1
93.2


pressure
to 410A)









RCL
g/m3

30.7
37.5
44.0
52.7
64.0
78.6

























TABLE 2







Comp.

Example

Comp.
Comp.
Example
Comp.




Ex. 5
Example
5
Example
Ex. 6
Ex. 7
7
Ex. 8


Item
Unit
C
4
C′
6
D
E
E′
F
























HFO-1132(E)
mass %
32.9
26.6
19.5
10.9
0.0
58.0
23.4
0.0


HFO-1123
mass %
67.1
68.4
70.5
74.1
80.4
42.0
48.5
61.8


R1234yf
mass %
0.0
5.0
10.0
15.0
19.6
0.0
28.1
38.2


GWP

1
1
1
1
2
1
2
2


COP ratio
%
92.5
92.5
92.5
92.5
92.5
95.0
95.0
95.0



(relative











to 410A)










Refrigerating
%
107.4
105.2
102.9
100.5
97.9
105.0
92.5
86.9


capacity ratio
(relative











to 410A)










Condensation
° C.
0.16
0.52
0.94
1.42
1.90
0.42
3.16
4.80


glide











Discharge
%
119.5
117.4
115.3
113.0
115.9
112.7
101.0
95.8


pressure
(relative











to 410A)










RCL
g/m3
53.5
57.1
62.0
69.1
81.3
41.9
46.3
79.0























TABLE 3







Comp.
Example
Example
Example
Example
Example




Ex. 9
8
9
10
11
12


Item
Unit
J
P
L
N
N′
K






















HFO-1132(E)
mass %
47.1
55.8
63.1
68.6
65.0
61.3


HFO-1123
mass %
52.9
42.0
31.9
16.3
7.7
5.4


R1234yf
mass %
0.0
2.2
5.0
15.1
27.3
33.3


GWP

1
1
1
1
2
2


COP ratio
% (relative to
93.8
95.0
96.1
97.9
99.1
99.5



410A)








Refrigerating capacity
% (relative to
106.2
104.1
101.6
95.0
88.2
85.0


ratio
410A)








Condensation glide
° C.
0.31
0.57
0.81
1.41
2.11
2.51


Discharge pressure
% (relative to
115.8
111.9
107.8
99.0
91.2
87.7



410A)








RCL
g/m3
46.2
42.6
40.0
38.0
38.7
39.7
























TABLE 4







Example
Example
Example
Example
Example
Example
Example




13
14
15
16
17
18
19


Item
Unit
L
M
Q
R
S
S′
T























HFO-1132(E)
mass %
63.1
60.3
62.8
49.8
62.6
50.0
35.8


HFO-1123
mass %
31.9
6.2
29.6
42.3
28.3
35.8
44.9


R1234yf
mass %
5.0
33.5
7.6
7.9
9.1
14.2
19.3


GWP

1
2
1
1
1
1
2


COP ratio
% (relative
96.1
99.4
96.4
95.0
96.6
95.8
95.0



to 410A)









Refrigerating
% (relative
101.6
85.0
100.2
101.7
99.4
98.1
96.7


capacity ratio
to 410A)









Condensation
° C.
0.81
2.58
1.00
1.00
1.10
1.55
2.07


glide










Discharge
% (relative
107.8
87.9
106.0
109.6
105.0
105.0
105.0


pressure
to 410A)









RCL
g/m3
40.0
40.0
40.0
44.8
40.0
44.4
50.8




















TABLE 5







Comp. Ex.
Example
Example




10
20
21


Item
Unit
G
H
I



















HFO-1132(E)
mass %
72.0
72.0
72.0


HFO-1123
mass %
28.0
14.0
0.0


R1234yf
mass %
0.0
14.0
28.0


GWP

1
1
2


COP ratio
% (relative to
96.6
98.2
99.9



410A)





Refrigerating
% (relative to
103.1
95.1
86.6


capacity ratio
410A)





Condensation glide
° C.
0.46
1.27
1.71


Discharge pressure
% (relative to
108.4
98.7
88.6



410A)





RCL
g/m3
37.4
37.0
36.6

























TABLE 6







Comp.
Comp.
Example
Example
Example
Example
Example
Comp.


Item
Unit
Ex. 11
Ex. 12
22
23
24
25
26
Ex. 13
























HFO-1132(E)
mass %
10.0
20.0
30.0
40.0
50.0
60.0
70.0
80.0


HFO-1123
mass %
85.0
75.0
65.0
55.0
45.0
35.0
25.0
15.0


R1234yf
mass %
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0


GWP

1
1
1
1
1
1
1
1


COP ratio
% (relative
91.4
92.0
92.8
93.7
94.7
95.8
96.9
98.0



to 410A)










Refrigerating
% (relative
105.7
105.5
105.0
104.3
103.3
102.0
100.6
99.1


capacity ratio
to 410A)










Condensation
° C.
0.40
0.46
0.55
0.66
0.75
0.80
0.79
0.67


glide











Discharge
% (relative
120.1
118.7
116.7
114.3
111.6
108.7
105.6
102.5


pressure
to 410A)










RCL
g/m3
71.0
61.9
54.9
49.3
44.8
41.0
37.8
35.1

























TABLE 7







Comp.
Example
Example
Example
Example
Example
Example
Comp.


Item
Unit
Ex. 14
27
28
29
30
31
32
Ex. 15
























HFO-1132(E)
mass %
10.0
20.0
30.0
40.0
50.0
60.0
70.0
80.0


HFO-1123
mass %
80.0
70.0
60.0
50.0
40.0
30.0
20.0
10.0


R1234yf
mass %
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0


GWP

1
1
1
1
1
1
1
1


COP ratio
% (relative
91.9
92.5
93.3
94.3
95.3
96.4
97.5
98.6



to 410A)










Refrigerating
% (relative
103.2
102.9
102.4
101.5
100.5
99.2
97.8
96.2


capacity ratio
to 410A)










Condensation
° C.
0.87
0.94
1.03
1.12
1.18
1.18
1.09
0.88


glide











Discharge
% (relative
116.7
115.2
113.2
110.8
108.1
105.2
102.1
99.0


pressure
to 410A)










RCL
g/m3
70.5
61.6
54.6
49.1
44.6
40.8
37.7
35.0

























TABLE 8







Comp.
Example
Example
Example
Example
Example
Example
Comp.


Item
Unit
Ex. 16
33
34
35
36
37
38
Ex. 17
























HFO-1132(E)
mass %
10.0
20.0
30.0
40.0
50.0
60.0
70.0
80.0


HFO-1123
mass %
75.0
65.0
55.0
45.0
35.0
25.0
15.0
5.0


R1234yf
mass %
15.0
15.0
15.0
15.0
15.0
15.0
15.0
15.0


GWP

1
1
1
1
1
1
1
1


COP ratio
% (relative
92.4
93.1
93.9
94.8
95.9
97.0
98.1
99.2



to 410A)










Refrigerating
% (relative
100.5
100.2
99.6
98.7
97.7
96.4
94.9
93.2


capacity ratio
to 410A)










Condensation
° C.
1.41
1.49
1.56
1.62
1.63
1.55
1.37
1.05


glide











Discharge
% (relative
113.1
111.6
109.6
107.2
104.5
101.6
98.6
95.5


pressure
to 410A)










RCL
g/m3
70.0
61.2
54.4
48.9
44.4
40.7
37.5
34.8
























TABLE 9







Example
Example
Example
Example
Example
Example
Example


Item
Unit
39
40
41
42
43
44
45























HFO-1132(E)
mass %
10.0
20.0
30.0
40.0
50.0
60.0
70.0


HFO-1123
mass %
70.0
60.0
50.0
40.0
30.0
20.0
10.0


R1234yf
mass %
20.0
20.0
20.0
20.0
20.0
20.0
20.0


GWP

2
2
2
2
2
2
2


COP ratio
% (relative
93.0
93.7
94.5
95.5
96.5
97.6
98.7



to 410A)









Refrigerating
% (relative
97.7
97.4
96.8
95.9
94.7
93.4
91.9


capacity ratio
to 410A)









Condensation
° C.
2.03
2.09
2.13
2.14
2.07
1.91
1.61


glide










Discharge
% (relative
109.4
107.9
105.9
103.5
100.8
98.0
95.0


pressure
to 410A)









RCL
g/m3
69.6
60.9
54.1
48.7
44.2
40.5
37.4
























TABLE 10







Example
Example
Example
Example
Example
Example
Example


Item
Unit
46
47
48
49
50
51
52























HFO-1132(E)
mass %
10.0
20.0
30.0
40.0
50.0
60.0
70.0


HFO-1123
mass %
65.0
55.0
45.0
35.0
25.0
15.0
5.0


R1234yf
mass %
25.0
25.0
25.0
25.0
25.0
25.0
25.0


GWP

2
2
2
2
2
2
2


COP ratio
% (relative
93.6
94.3
95.2
96.1
97.2
98.2
99.3



to 410A)









Refrigerating
% (relative
94.8
94.5
93.8
92.9
91.8
90.4
88.8


capacity ratio
to 410A)









Condensation
° C.
2.71
2.74
2.73
2.66
2.50
2.22
1.78


glide










Discharge
% (relative
105.5
104.0
102.1
99.7
97.1
94.3
91.4


pressure
to 410A)









RCL
g/m3
69.1
60.5
53.8
48.4
44.0
40.4
37.3























TABLE 11







Example
Example
Example
Example
Example
Example


Item
Unit
53
54
55
56
57
58






















HFO-1132(E)
mass %
10.0
20.0
30.0
40.0
50.0
60.0


HFO-1123
mass %
60.0
50.0
40.0
30.0
20.0
10.0


R1234yf
mass %
30.0
30.0
30.0
30.0
30.0
30.0


GWP

2
2
2
2
2
2


COP ratio
% (relative
94.3
95.0
95.9
96.8
97.8
98.9



to 410A)








Refrigerating
% (relative
91.9
91.5
90.8
89.9
88.7
87.3


capacity ratio
to 410A)








Condensation
° C.
3.46
3.43
3.35
3.18
2.90
2.47


glide









Discharge
% (relative
101.6
100.1
98.2
95.9
93.3
90.6


pressure
to 410A)








RCL
g/m3
68.7
60.2
53.5
48.2
43.9
40.2























TABLE 12







Example
Example
Example
Example
Example
Comp.


Item
Unit
59
60
61
62
63
Ex. 18






















HFO-1132(E)
mass %
10.0
20.0
30.0
40.0
50.0
60.0


HFO-1123
mass %
55.0
45.0
35.0
25.0
15.0
5.0


R1234yf
mass %
35.0
35.0
35.0
35.0
35.0
35.0


GWP

2
2
2
2
2
2


COP ratio
% (relative
95.0
95.8
96.6
97.5
98.5
99.6



to 410A)








Refrigerating
% (relative
88.9
88.5
87.8
86.8
85.6
84.1


capacity ratio
to 410A)








Condensation
° C.
4.24
4.15
3.96
3.67
3.24
2.64


glide









Discharge
% (relative
97.6
96.1
94.2
92.0
89.5
86.8


pressure
to 410A)








RCL
g/m3
68.2
59.8
53.2
48.0
43.7
40.1






















TABLE 13







Example
Example
Comp.
Comp.
Comp.


Item
Unit
64
65
Ex. 19
Ex. 20
Ex. 21





















HFO-1132(E)
mass %
10.0
20.0
30.0
40.0
50.0


HFO-1123
mass %
50.0
40.0
30.0
20.0
10.0


R1234yf
mass %
40.0
40.0
40.0
40.0
40.0


GWP

2
2
2
2
2


COP ratio
% (relative
95.9
96.6
97.4
98.3
99.2



to 410A)







Refrigerating
% (relative
85.8
85.4
84.7
83.6
82.4


capacity ratio
to 410A)







Condensation
° C.
5.05
4.85
4.55
4.10
3.50


glide








Discharge
% (relative
93.5
92.1
90.3
88.1
85.6


pressure
to 410A)







RCL
g/m3
67.8
59.5
53.0
47.8
43.5

























TABLE 14







Example
Example
Example
Example
Example
Example
Example
Example


Item
Unit
66
67
68
69
70
71
72
73
























HFO-1132(E)
mass %
54.0
56.0
58.0
62.0
52.0
54.0
56.0
58.0


HFO-1123
mass %
41.0
39.0
37.0
33.0
41.0
39.0
37.0
35.0


R1234yf
mass %
5.0
5.0
5.0
5.0
7.0
7.0
7.0
7.0


GWP

1
1
1
1
1
1
1
1


COP ratio
% (relative
95.1
95.3
95.6
96.0
95.1
95.4
95.6
95.8



to 410A)










Refrigerating
% (relative
102.8
102.6
102.3
101.8
101.9
101.7
101.5
101.2


capacity ratio
to 410A)










Condensation
° C.
0.78
0.79
0.80
0.81
0.93
0.94
0.95
0.95


glide











Discharge
% (relative
110.5
109.9
109.3
108.1
109.7
109.1
108.5
107.9


pressure
to 410A)










RCL
g/m3
43.2
42.4
41.7
40.3
43.9
43.1
42.4
41.6

























TABLE 15







Example
Example
Example
Example
Example
Example
Example
Example


Item
Unit
74
75
76
77
78
79
80
81
























HFO-1132(E)
mass %
60.0
62.0
61.0
58.0
60.0
62.0
52.0
54.0


HFO-1123
mass %
33.0
31.0
29.0
30.0
28.0
26.0
34.0
32.0


R1234yf
mass %
7.0
7.0
10.0
12.0
12.0
12.0
14.0
14.0


GWP

1
1
1
1
1
1
1
1


COP ratio
% (relative
96.0
96.2
96.5
96.4
96.6
96.8
96.0
96.2



to 410A)










Refrigerating
% (relative
100.9
100.7
99.1
98.4
98.1
97.8
98.0
97.7


capacity ratio
to 410A)










Condensation
° C.
0.95
0.95
1.18
1.34
1.33
1.32
1.53
1.53


glide











Discharge
% (relative
107.3
106.7
104.9
104.4
103.8
103.2
104.7
104.1


pressure
to 410A)










RCL
g/m3
40.9
40.3
40.5
41.5
40.8
40.1
43.6
42.9

























TABLE 16







Example
Example
Example
Example
Example
Example
Example
Example


Item
Unit
82
83
84
85
86
87
88
89
























HFO-1132(E)
mass %
56.0
58.0
60.0
48.0
50.0
52.0
54.0
56.0


HFO-1123
mass %
30.0
28.0
26.0
36.0
34.0
32.0
30.0
28.0


R1234yf
mass %
14.0
14.0
14.0
16.0
16.0
16.0
16.0
16.0


GWP

1
1
1
1
1
1
1
1


COP ratio
% (relative
96.4
96.6
96.9
95.8
96.0
96.2
96.4
96.7



to 410A)










Refrigerating
% (relative
97.5
97.2
96.9
97.3
97.1
96.8
96.6
96.3


capacity ratio
to 410A)










Condensation
° C.
1.51
1.50
1.48
1.72
1.72
1.71
1.69
1.67


glide











Discharge
% (relative
103.5
102.9
102.3
104.3
103.8
103.2
102.7
102.1


pressure
to 410A)










RCL
g/m3
42.1
41.4
40.7
45.2
44.4
43.6
42.8
42.1

























TABLE 17







Example
Example
Example
Example
Example
Example
Example
Example


Item
Unit
90
91
92
93
94
95
96
97
























HFO-1132(E)
mass %
58.0
60.0
42.0
44.0
46.0
48.0
50.0
52.0


HFO-1123
mass %
26.0
24.0
40.0
38.0
36.0
34.0
32.0
30.0


R1234yf
mass %
16.0
16.0
18.0
18.0
18.0
18.0
18.0
18.0


GWP

1
1
2
2
2
2
2
2


COP ratio
% (relative
96.9
97.1
95.4
95.6
95.8
96.0
96.3
96.5



to 410A)










Refrigerating
% (relative
96.1
95.8
96.8
96.6
96.4
96.2
95.9
95.7


capacity ratio
to 410A)










Condensation
° C.
1.65
1.63
1.93
1.92
1.92
1.91
1.89
1.88


glide











Discharge
% (relative
101.5
100.9
104.5
103.9
103.4
102.9
102.3
101.8


pressure
to 410A)










RCL
g/m3
41.4
40.7
47.8
46.9
46.0
45.1
44.3
43.5

























TABLE 18







Example
Example
Example
Example
Example
Example
Example
Example


Item
Unit
98
99
100
101
102
103
104
105
























HFO-1132(E)
mass %
54.0
56.0
58.0
60.0
36.0
38.0
42.0
44.0


HFO-1123
mass %
28.0
26.0
24.0
22.0
44.0
42.0
38.0
36.0


R1234yf
mass %
18.0
18.0
18.0
18.0
20.0
20.0
20.0
20.0


GWP

2
2
2
2
2
2
2
2


COP ratio
% (relative
96.7
96.9
97.1
97.3
95.1
95.3
95.7
95.9



to 410A)










Refrigerating
% (relative
95.4
95.2
94.9
94.6
96.3
96.1
95.7
95.4


capacity ratio
to 410A)










Condensation
° C.
1.86
1.83
1.80
1.77
2.14
2.14
2.13
2.12


glide











Discharge
% (relative
101.2
100.6
100.0
99.5
104.5
104.0
103.0
102.5


pressure
to 410A)










RCL
g/m3
42.7
42.0
41.3
40.6
50.7
49.7
47.7
46.8

























TABLE 19







Example
Example
Example
Example
Example
Example
Example
Example


Item
Unit
106
107
108
109
110
111
112
113
























HFO-1132(E)
mass %
46.0
48.0
52.0
54.0
56.0
58.0
34.0
36.0


HFO-1123
mass %
34.0
32.0
28.0
26.0
24.0
22.0
44.0
42.0


R1234yf
mass %
20.0
20.0
20.0
20.0
20.0
20.0
22.0
22.0


GWP

2
2
2
2
2
2
2
2


COP ratio
% (relative
96.1
96.3
96.7
96.9
97.2
97.4
95.1
95.3



to 410A)










Refrigerating
% (relative
95.2
95.0
94.5
94.2
94.0
93.7
95.3
95.1


capacity ratio
to 410A)










Condensation
° C.
2.11
2.09
2.05
2.02
1.99
1.95
2.37
2.36


glide











Discharge
% (relative
101.9
101.4
100.3
99.7
99.2
98.6
103.4
103.0


pressure
to 410A)










RCL
g/m3
45.9
45.0
43.4
42.7
41.9
41.2
51.7
50.6

























TABLE 20







Ex-
Ex-
Ex-
Ex-
Ex-
Ex-
Ex-
Ex-




ample
ample
ample
ample
ample
ample
ample
ample


Item
Unit
114
115
116
117
118
119
120
121
























HFO-
mass %
38.0
40.0
42.0
44.0
46.0
48.0
50.0
52.0


1132 (E)











HFO-
mass %
40.0
38.0
36.0
34.0
32.0
30.0
28.0
26.0


1123











R1234yf
mass %
22.0
22.0
22.0
22.0
22.0
22.0
22.0
22.0


GWP

2
2
2
2
2
2
2
2


COP
% (relative
95.5
95.7
95.9
96.1
96.4
96.6
96.8
97.0


ratio
to 410A)










Refrig-
% (relative
94.9
94.7
94.5
94.3
94.0
93.8
93.6
93.3


erating
to 410A)










capacity











ratio











Conden-
° C.
2.36
2.35
2.33
2.32
2.30
2.27
2.25
2.21


sation











glide











Discharge
% (relative
102.5
102.0
101.5
101.0
100.4
99.9
99.4
98.8


pressure
to 410A)










RCL
g/m3
49.6
48.6
47.6
46.7
45.8
45.0
44.1
43.4

























TABLE 21







Ex-
Ex-
Ex-
Ex-
Ex-
Ex-
Ex-
Ex-




ample
ample
ample
ample
ample
ample
ample
ample


Item
Unit
122
123
124
125
126
127
128
129
























HFO-
mass %
54.0
56.0
58.0
60.0
32.0
34.0
36.0
38.0


1132 (E)











HFO-
mass %
24.0
22.0
20.0
18.0
44.0
42.0
40.0
38.0


1123











R1234yf
mass %
22.0
22.0
22.0
22.0
24.0
24.0
24.0
24.0


GWP

2
2
2
2
2
2
2
2


COP
% (relative
97.2
97.4
97.6
97.9
95.2
95.4
95.6
95.8


ratio
to 410A)










Refrig-
% (relative
93.0
92.8
92.5
92.2
94.3
94.1
93.9
93.7


erating
to 410A)










capacity











ratio











Conden-
° C.
2.18
2.14
2.09
2.04
2.61
2.60
2.59
2.58


sation











glide











Discharge
% (relative
98.2
97.7
97.1
96.5
102.4
101.9
101.5
101.0


pressure
to 410A)










RCL
g/m3
42.6
41.9
41.2
40.5
52.7
51.6
50.5
49.5

























TABLE 22







Ex-
Ex-
Ex-
Ex-
Ex-
Ex-
Ex-
Ex-




ample
ample
ample
ample
ample
ample
ample
ample


Item
Unit
130
131
132
133
134
135
136
137
























HFO-
mass %
40.0
42.0
44.0
46.0
48.0
50.0
52.0
54.0


1132 (E)











HFO-
mass %
36.0
34.0
32.0
30.0
28.0
26.0
24.0
22.0


1123











R1234yf
mass %
24.0
24.0
24.0
24.0
24.0
24.0
24.0
24.0


GWP

2
2
2
2
2
2
2
2


COP
% (relative
96.0
96.2
96.4
96.6
96.8
97.0
97.2
97.5


ratio
to 410A)










Refrig-
% (relative
93.5
93.3
93.1
92.8
92.6
92.4
92.1
91.8


erating
to 410A)










capacity











ratio











Conden-
° C.
2.56
2.54
2.51
2.49
2.45
2.42
2.38
2.33


sation











glide











Discharge
% (relative
100.5
100.0
99.5
98.9
98.4
97.9
97.3
96.8


pressure
to 410A)










RCL
g/m3
48.5
47.5
46.6
45.7
44.9
44.1
43.3
42.5

























TABLE 23







Ex-
Ex-
Ex-
Ex-
Ex-
Ex-
Ex-
Ex-




ample
ample
ample
ample
ample
ample
ample
ample


Item
Unit
138
139
140
141
142
143
144
145
























HFO-
mass %
56.0
58.0
60.0
30.0
32.0
34.0
36.0
38.0


1132 (E)











HFO-
mass %
20.0
18.0
16.0
44.0
42.0
40.0
38.0
36.0


1123











R1234yf
mass %
24.0
24.0
24.0
26.0
26.0
26.0
26.0
26.0


GWP

2
2
2
2
2
2
2
2


COP
% (relative
97.7
97.9
98.1
95.3
95.5
95.7
95.9
96.1


ratio
to 410A)










Refrig-
% (relative
91.6
91.3
91.0
93.2
93.1
92.9
92.7
92.5


erating
to 410A)










capacity











ratio











Conden-
° C.
2.28
2.22
2.16
2.86
2.85
2.83
2.81
2.79


sation











glide











Discharge
% (relative
96.2
95.6
95.1
101.3
100.8
100.4
99.9
99.4


pressure
to 410A)










RCL
g/m3
41.8
41.1
40.4
53.7
52.6
51.5
50.4
49.4

























TABLE 24







Ex-
Ex-
Ex-
Ex-
Ex-
Ex-
Ex-
Ex-




ample
ample
ample
ample
ample
ample
ample
ample


Item
Unit
146
147
148
149
150
151
152
153
























HFO-
mass %
40.0
42.0
44.0
46.0
48.0
50.0
52.0
54.0


1132 (E)











HFO-
mass %
34.0
32.0
30.0
28.0
26.0
24.0
22.0
20.0


1123











R1234yf
mass %
26.0
26.0
26.0
26.0
26.0
26.0
26.0
26.0


GWP

2
2
2
2
2
2
2
2


COP
% (relative
96.3
96.5
96.7
96.9
97.1
97.3
97.5
97.7


ratio
to 410A)










Refrig-
% (relative
92.3
92.1
91.9
91.6
91.4
91.2
90.9
90.6


erating
to 410A)










capacity











ratio











Conden-
° C.
2.77
2.74
2.71
2.67
2.63
2.59
2.53
2.48


sation











glide











Discharge
% (relative
99.0
98.5
97.9
97.4
96.9
96.4
95.8
95.3


pressure
to 410A)










RCL
g/m3
48.4
47.4
46.5
45.7
44.8
44.0
43.2
42.5

























TABLE 25







Ex-
Ex-
Ex-
Ex-
Ex-
Ex-
Ex-
Ex-




ample
ample
ample
ample
ample
ample
ample
ample


Item
Unit
154
155
156
157
158
159
160
161
























HFO-
mass %
56.0
58.0
60.0
30.0
32.0
34.0
36.0
38.0


1132 (E)











HFO-
mass %
18.0
16.0
14.0
42.0
40.0
38.0
36.0
34.0


1123











R1234yf
mass %
26.0
26.0
26.0
28.0
28.0
28.0
28.0
28.0


GWP

2
2
2
2
2
2
2
2


COP
% (relative
97.9
98.2
98.4
95.6
95.8
96.0
96.2
96.3


ratio
to 410A)










Refrig-
% (relative
90.3
90.1
89.8
92.1
91.9
91.7
91.5
91.3


erating
to 410A)










capacity











ratio











Conden-
° C.
2.42
2.35
2.27
3.10
3.09
3.06
3.04
3.01


sation











glide











Discharge
% (relative
94.7
94.1
93.6
99.7
99.3
98.8
98.4
97.9


pressure
to 410A)










RCL
g/m3
41.7
41.0
40.3
53.6
52.5
51.4
50.3
49.3

























TABLE 26







Ex-
Ex-
Ex-
Ex-
Ex-
Ex-
Ex-
Ex-




ample
ample
ample
ample
ample
ample
ample
ample


Item
Unit
162
163
164
165
166
167
168
169
























HFO-
mass %
40.0
42.0
44.0
46.0
48.0
50.0
52.0
54.0


1132 (E)











HFO-
mass %
32.0
30.0
28.0
26.0
24.0
22.0
20.0
18.0


1123











R1234yf
mass %
28.0
28.0
28.0
28.0
28.0
28.0
28.0
28.0


GWP

2
2
2
2
2
2
2
2


COP
% (relative
96.5
96.7
96.9
97.2
97.4
97.6
97.8
98.0


ratio
to 410A)










Refrig-
% (relative
91.1
90.9
90.7
90.4
90.2
89.9
89.7
89.4


erating
to 410A)










capacity











ratio











Conden-
° C.
2.98
2.94
2.90
2.85
0.80
2.75
2.68
2.62


sation











glide











Discharge
% (relative
97.4
96.9
96.4
95.9
95.4
94.9
94.3
93.8


pressure
to 410A)










RCL
g/m3
48.3
47.4
46.4
45.6
44.7
43.9
43.1
42.4

























TABLE 27







Ex-
Ex-
Ex-
Ex-
Ex-
Ex-
Ex-
Ex-




ample
ample
ample
ample
ample
ample
ample
ample


Item
Unit
170
171
172
173
174
175
176
177
























HFO-
mass %
56.0
58.0
60.0
32.0
34.0
36.0
38.0
42.0


1132 (E)











HFO-
mass %
16.0
14.0
12.0
38.0
36.0
34.0
32.0
28.0


1123











R1234yf
mass %
28.0
28.0
28.0
30.0
30.0
30.0
30.0
30.0


GWP

2
2
2
2
2
2
2
2


COP
% (relative
98.2
98.4
98.6
96.1
96.2
96.4
96.6
97.0


ratio
to 410A)










Refrig-
% (relative
89.1
88.8
88.5
90.7
90.5
90.3
90.1
89.7


erating
to 410A)










capacity











ratio











Conden-
° C.
2.54
2.46
2.38
3.32
3.30
3.26
3.22
3.14


sation











glide











Discharge
% (relative
93.2
92.6
92.1
97.7
97.3
96.8
96.4
95.4


pressure
to 410A)










RCL
g/m3
41.7
41.0
40.3
52.4
51.3
50.2
49.2
47.3

























TABLE 28







Ex-
Ex-
Ex-
Ex-
Ex-
Ex-
Ex-
Ex-




ample
ample
ample
ample
ample
ample
ample
ample


Item
Unit
178
179
180
181
182
183
184
185
























HFO-
mass %
44.0
46.0
48.0
50.0
52.0
54.0
56.0
58.0


1132 (E)











HFO-
mass %
26.0
24.0
22.0
20.0
18.0
16.0
14.0
12.0


1123











R1234yf
mass %
30.0
30.0
30.0
30.0
30.0
30.0
30.0
30.0


GWP

2
2
2
2
2
2
2
2


COP
% (relative
97.2
97.4
97.6
97.8
98.0
98.3
98.5
98.7


ratio
to 410A)










Refrig-
% (relative
89.4
89.2
89.0
88.7
88.4
88.2
87.9
87.6


erating
to 410A)










capacity











ratio











Conden-
° C.
3.08
3.03
2.97
2.90
2.83
2.75
2.66
2.57


sation











glide











Discharge
% (relative
94.9
94.4
93.9
93.3
92.8
92.3
91.7
91.1


pressure
to 410A)










RCL
g/m3
46.4
45.5
44.7
43.9
43.1
42.3
41.6
40.9

























TABLE 29







Ex-
Ex-
Ex-
Ex-
Ex-
Ex-
Ex-
Ex-




ample
ample
ample
ample
ample
ample
ample
ample


Item
Unit
186
187
188
189
190
191
192
193
























HFO-
mass %
30.0
32.0
34.0
36.0
38.0
40.0
42.0
44.0


1132 (E)











HFO-
mass %
38.0
36.0
34.0
32.0
30.0
28.0
26.0
24.0


1123











R1234yf
mass %
32.0
32.0
32.0
32.0
32.0
32.0
32.0
32.0


GWP

2
2
2
2
2
2
2
2


COP
% (relative
96.2
96.3
96.5
96.7
96.9
97.1
97.3
97.5


ratio
to 410A)










Refrig-
% (relative
89.6
89.5
89.3
89.1
88.9
88.7
88.4
88.2


erating
to 410A)










capacity











ratio











Conden-
° C.
3.60
3.56
3.52
3.48
3.43
3.38
3.33
3.26


sation











glide











Discharge
% (relative
96.6
96.2
95.7
95.3
94.8
94.3
93.9
93.4


pressure
to 410A)










RCL
g/m3
53.4
52.3
51.2
50.1
49.1
48.1
47.2
46.3

























TABLE 30







Ex-
Ex-
Ex-
Ex-
Ex-
Ex-
Ex-
Ex-




ample
ample
ample
ample
ample
ample
ample
ample


Item
Unit
194
195
196
197
198
199
200
201
























HFO-
mass %
46.0
48.0
50.0
52.0
54.0
56.0
58.0
60.0


1132 (E)











HFO-
mass %
22.0
20.0
18.0
16.0
14.0
12.0
10.0
8.0


1123











R1234yf
mass %
32.0
32.0
32.0
32.0
32.0
32.0
32.0
32.0


GWP

2
2
2
2
2
2
2
2


COP
% (relative
97.7
97.9
98.1
98.3
98.5
98.7
98.9
99.2


ratio
to 410A)










Refrig-
% (relative
88.0
87.7
87.5
87.2
86.9
86.6
86.3
86.0


erating
to 410A)










capacity











ratio











Conden-
° C.
3.20
3.12
3.04
2.96
2.87
2.77
2.66
2.55


sation











glide











Discharge
% (relative
92.8
92.3
91.8
91.3
90.7
90.2
89.6
89.1


pressure
to 410A)










RCL
g/m3
45.4
44.6
43.8
43.0
42.3
41.5
40.8
40.2

























TABLE 31







Ex-
Ex-
Ex-
Ex-
Ex-
Ex-
Ex-
Ex-




ample
ample
ample
ample
ample
ample
ample
ample


Item
Unit
202
203
204
205
206
207
208
209
























HFO-
mass %
30.0
32.0
34.0
36.0
38.0
40.0
42.0
44.0


1132 (E)











HFO-
mass %
36.0
34.0
32.0
30.0
28.0
26.0
24.0
22.0


1123











R1234yf
mass %
34.0
34.0
34.0
34.0
34.0
34.0
34.0
34.0


GWP

2
2
2
2
2
2
2
2


COP
% (relative
96.5
96.6
96.8
97.0
97.2
97.4
97.6
97.8


ratio
to 410A)










Refrig-
% (relative
88.4
88.2
88.0
87.8
87.6
87.4
87.2
87.0


erating
to 410A)










capacity











ratio











Conden-
° C.
3.84
3.80
3.75
3.70
3.64
6.58
3.51
3.43


sation











glide











Discharge
% (relative
95.0
94.6
94.2
93.7
93.3
92.8
92.3
91.8


pressure
to 410A)










RCL
g/m3
53.3
52.2
51.1
50.0
49.0
48.0
47.1
46.2

























TABLE 32







Ex-
Ex-
Ex-
Ex-
Ex-
Ex-
Ex-
Ex-




ample
ample
ample
ample
ample
ample
ample
ample


Item
Unit
210
211
212
213
214
215
216
217
























HFO-
mass %
46.0
48.0
50.0
52.0
54.0
30.0
32.0
34.0


1132 (E)











HFO-
mass %
20.0
18.0
16.0
14.0
12.0
34.0
32.0
30.0


1123











R1234yf
mass %
34.0
34.0
34.0
34.0
34.0
36.0
36.0
36.0


GWP

2
2
2
2
2
2
2
2


COP
% (relative
98.0
98.2
98.4
98.6
98.8
96.8
96.9
97.1


ratio
to 410A)










Refrig-
% (relative
86.7
86.5
86.2
85.9
85.6
87.2
87.0
86.8


erating
to 410A)










capacity











ratio











Conden-
° C.
3.36
3.27
3.18
3.08
2.97
4.08
4.03
3.97


sation











glide











Discharge
% (relative
91.3
90.8
90.3
89.7
89.2
93.4
93.0
92.6


pressure
to 410A)










RCL
g/m3
45.3
44.5
43.7
42.9
42.2
53.2
52.1
51.0

























TABLE 33







Ex-
Ex-
Ex-
Ex-
Ex-
Ex-
Ex-
Ex-




ample
ample
ample
ample
ample
ample
ample
ample


Item
Unit
218
219
220
221
222
223
224
225
























HFO-
mass %
36.0
38.0
40.0
42.0
44.0
46.0
30.0
32.0


1132 (E)











HFO-
mass %
28.0
26.0
24.0
22.0
20.0
18.0
32.0
30.0


1123











R1234yf
mass %
36.0
36.0
36.0
36.0
36.0
36.0
38.0
38.0


GWP

2
2
2
2
2
2
2
2


COP
% (relative
97.3
97.5
97.7
97.9
98.1
98.3
97.1
97.2


ratio
to 410A)










Refrig-
% (relative
86.6
86.4
86.2
85.9
85.7
85.5
85.9
85.7


erating
to 410A)










capacity











ratio











Conden-
° C.
3.91
3.84
3.76
3.68
3.60
3.50
4.32
4.25


sation











glide











Discharge
% (relative
92.1
91.7
91.2
90.7
90.3
89.8
91.9
91.4


pressure
to 410A)










RCL
g/m3
49.9
48.9
47.9
47.0
46.1
45.3
53.1
52.0



















TABLE 34







Example
Example


Item
Unit
226
227


















HFO-1132(E)
mass %
34.0
36.0


HFO-1123
mass %
28.0
26.0


R1234yf
mass %
38.0
38.0


GWP

2
2


COP ratio
% (relative to
97.4
97.6



410A)




Refrigerating
% (relative to
85.6
85.3


capacity ratio
410A)




Condensation glide
° C.
4.18
4.11


Discharge
% (relative to
91.0
90.6


pressure
410A)




RCL
g/m3
50.9
49.8









These results indicate that under the condition that the mass % of HFO-1132(E), HFO-1123, and R1234yf based on their sum is respectively represented by x, y, and z, when coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R1234yf is 100 mass % are within the range of a figure surrounded by line segments AA′, A′B, BD, DC′, C′C, CO, and OA that connect the following 7 points:


point A (68.6, 0.0, 31.4),


point A′(30.6, 30.0, 39.4),


point B (0.0, 58.7, 41.3),


point D (0.0, 80.4, 19.6),


point C′ (19.5, 70.5, 10.0),


point C (32.9, 67.1, 0.0), and


point O (100.0, 0.0, 0.0),


or on the above line segments (excluding the points on the line segment CO);


the line segment AA′ is represented by coordinates (x, 0.0016x2−0.9473x+57.497, −0.0016x2−0.0527x+42.503),


the line segment A′B is represented by coordinates (x, 0.0029x2−1.0268x+58.7, −0.0029x2+0.0268x+41.3,


the line segment DC′ is represented by coordinates (x, 0.0082x2−0.6671x+80.4, −0.0082x2−0.3329x+19.6),


the line segment C′C is represented by coordinates (x, 0.0067x2−0.6034x+79.729, −0.0067x2−0.3966x+20.271), and


the line segments BD, CO, and OA are straight lines,


the refrigerant has a refrigerating capacity ratio of 85% or more relative to that of R410A, and a COP of 92.5% or more relative to that of R410A.


The point on the line segment AA′ was determined by obtaining an approximate curve connecting point A, Example 1, and point A′ by the least square method.


The point on the line segment A′B was determined by obtaining an approximate curve connecting point A′, Example 3, and point B by the least square method.


The point on the line segment DC′ was determined by obtaining an approximate curve connecting point D, Example 6, and point C′ by the least square method.


The point on the line segment C′C was determined by obtaining an approximate curve connecting point C′, Example 4, and point C by the least square method.


Likewise, the results indicate that when coordinates (x,y,z) are within the range of a figure surrounded by line segments AA′, A′B, BF, FT, TE, EO, and OA that connect the following 7 points:


point A (68.6, 0.0, 31.4),


point A′ (30.6, 30.0, 39.4),


point B (0.0, 58.7, 41.3),


point F (0.0, 61.8, 38.2),


point T (35.8, 44.9, 19.3),


point E (58.0, 42.0, 0.0) and


point O (100.0, 0.0, 0.0),


or on the above line segments (excluding the points on the line EO);


the line segment AA′ is represented by coordinates (x, 0.0016x2−0.9473x+57.497, −0.0016x2−0.0527x+42.503),


the line segment A′B is represented by coordinates (x, 0.0029x2−1.0268x+58.7, −0.0029x2+0.0268x+41.3),


the line segment FT is represented by coordinates (x, 0.0078x2−0.7501x+61.8, −0.0078x2−0.2499x+38.2), and


the line segment TE is represented by coordinates (x, 0.0067x2−0.7607x+63.525, −0.0067x2−0.2393x+36.475), and


the line segments BF, FO, and OA are straight lines,


the refrigerant has a refrigerating capacity ratio of 85% or more relative to that of R410A, and a COP of 95% or more relative to that of R410A.


The point on the line segment FT was determined by obtaining an approximate curve connecting three points, i.e., points T, E′, and F, by the least square method.


The point on the line segment TE was determined by obtaining an approximate curve connecting three points, i.e., points E, R, and T, by the least square method.


The results in Tables 1 to 34 clearly indicate that in a ternary composition diagram of the mixed refrigerant of HFO-1132(E), HFO-1123, and R1234yf in which the sum of these components is 100 mass %, a line segment connecting a point (0.0, 100.0, 0.0) and a point (0.0, 0.0, 100.0) is the base, the point (0.0, 100.0, 0.0) is on the left side, and the point (0.0, 0.0, 100.0) is on the right side, when coordinates (x,y,z) are on or below the line segment LM connecting point L (63.1, 31.9, 5.0) and point M (60.3, 6.2, 33.5), the refrigerant has an RCL of 40 g/m3 or more.


The results in Tables 1 to 34 clearly indicate that in a ternary composition diagram of the mixed refrigerant of HFO-1132(E), HFO-1123 and R1234yf in which their sum is 100 mass %, a line segment connecting a point (0.0, 100.0, 0.0) and a point (0.0, 0.0, 100.0) is the base, the point (0.0, 100.0, 0.0) is on the left side, and the point (0.0, 0.0, 100.0) is on the right side, when coordinates (x,y,z) are on the line segment QR connecting point Q (62.8, 29.6, 7.6) and point R (49.8, 42.3, 7.9) or on the left side of the line segment, the refrigerant has a temperature glide of 1° C. or less.


The results in Tables 1 to 34 clearly indicate that in a ternary composition diagram of the mixed refrigerant of HFO-1132(E), HFO-1123, and R1234yf in which their sum is 100 mass %, a line segment connecting a point (0.0, 100.0, 0.0) and a point (0.0, 0.0, 100.0) is the base, the point (0.0, 100.0, 0.0) is on the left side, and the point (0.0, 0.0, 100.0) is on the right side, when coordinates (x,y,z) are on the line segment ST connecting point S (62.6, 28.3, 9.1) and point T (35.8, 44.9, 19.3) or on the right side of the line segment, the refrigerant has a discharge pressure of 105% or less relative to that of 410A.


In these compositions, R1234yf contributes to reducing flammability, and suppressing deterioration of polymerization etc. Therefore, the composition preferably contains R1234yf.


Further, the burning velocity of these mixed refrigerants whose mixed formulations were adjusted to WCF concentrations was measured according to the ANSI/ASHRAE Standard 34-2013. Compositions having a burning velocity of 10 cm/s or less were determined to be classified as “Class 2L (lower flammability).”


A burning velocity test was performed using the apparatus shown in FIG. 1 in the following manner. In FIG. 1, reference numeral 901 refers to a sample cell, 902 refers to a high-speed camera, 903 refers to a xenon lamp, 904 refers to a collimating lens, 905 refers to a collimating lens, and 906 refers to a ring filter. First, the mixed refrigerants used had a purity of 99.5% or more, and were degassed by repeating a cycle of freezing, pumping, and thawing until no traces of air were observed on the vacuum gauge. The burning velocity was measured by the closed method. The initial temperature was ambient temperature. Ignition was performed by generating an electric spark between the electrodes in the center of a sample cell. The duration of the discharge was 1.0 to 9.9 ms, and the ignition energy was typically about 0.1 to 1.0 J. The spread of the flame was visualized using schlieren photographs. A cylindrical container (inner diameter: 155 mm, length: 198 mm) equipped with two light transmission acrylic windows was used as the sample cell, and a xenon lamp was used as the light source. Schlieren images of the flame were recorded by a high-speed digital video camera at a frame rate of 600 fps and stored on a PC.


Each WCFF concentration was obtained by using the WCF concentration as the initial concentration and performing a leak simulation using NIST Standard Reference Database REFLEAK Version 4.0.


Tables 35 and 36 show the results.













TABLE 35





Item
Unit
G
H
I




















WCF
HFO-1132(E)
mass %
72.0
72.0
72.0



HFO-1123
mass %
28.0
9.6
0.0



R1234yf
mass %
0.0
18.4
28.0











Burning velocity (WCF)
cm/s
10
10
10























TABLE 36





Item
Unit
J
P
L
N
N′
K























WCF
HFO-
mass
47.1
55.8
63.1
68.6
65.0
61.3



1132
%









(E)










HFO-
mass
52.9
42.0
31.9
16.3
7.7
5.4



1132
%









R1234yf
mass
0.0
2.2
5.0
15.1
27.3
33.3




%



















Leak condition that
Storage/
Storage/
Storage/
Storage/
Storage/
Storage/


results in WCFF
Shipping
Shipping
Shipping
Shipping
Shipping
Shipping


















−40° C.,
−40° C.,
−40° C.,
−40° C.,
−40° C.,
−40° C.,





92%
90%
90%
66%
12%
0%





release,
release,
release,
release,
release,
release,





liquid
liquid
gas
gas
gas
gas





phase
phase
phase
phase
phase
phase





side
side
side
side
side
side


WCFF
HFO-
mass
72.0
72.0
72.0
72.0
72.0
72.0



1132
%









(E)










HFO-
mass
28.0
17.8
17.4
13.6
12.3
9.8



1123
%









R1234yf
mass
0.0
10.2
10.6
14.4
15.7
18.2




%




















Burning
cm/s
8 or
8 or
8 or
9
9
8 or


velocity (WCF)

less
less
less


less


Burning
cm/s
10
10
10
10
10
10


velocity









(WCFF)









The results in Table 35 clearly indicate that when a mixed refrigerant of HFO-1132(E), HFO-1123, and R1234yf contains HFO-1132(E) in a proportion of 72.0 mass % or less based on their sum, the refrigerant can be determined to have a WCF lower flammability.


The results in Tables 36 clearly indicate that in a ternary composition diagram of a mixed refrigerant of HFO-1132(E), HFO-1123, and R1234yf in which their sum is 100 mass %, and a line segment connecting a point (0.0, 100.0, 0.0) and a point (0.0, 0.0, 100.0) is the base,


when coordinates (x,y,z) are on or below the line segments JP, PN, and NK connecting the following 6 points:


point J (47.1, 52.9, 0.0),


point P (55.8, 42.0, 2.2),


point L (63.1,31.9,5.0)


point N (68.6, 16.3, 15.1)


point N′ (65.0, 7.7, 27.3) and


point K (61.3, 5.4, 33.3),


the refrigerant can be determined to have a WCF lower flammability, and a WCFF lower flammability.


In the diagram, the line segment PN is represented by coordinates (x, −0.1135x2+12.112x−280.43, 0.1135x2−13.112x+380.43),


and the line segment NK is represented by coordinates (x, 0.2421x2−29.955x+931.91, −0.2421x2+28.955x−831.91).


The point on the line segment PN was determined by obtaining an approximate curve connecting three points, i.e., points P, L, and N, by the least square method.


The point on the line segment NK was determined by obtaining an approximate curve connecting three points, i.e., points N, N′, and K, by the least square method.


(5-2) Refrigerant B

The refrigerant B according to the present disclosure is


a mixed refrigerant comprising trans-1,2-difluoroethylene (HFO-1132(E)) and trifluoroethylene (HFO-1123) in a total amount of 99.5 mass % or more based on the entire refrigerant, and the refrigerant comprising 62.0 mass % to 72.0 mass % or 45.1 mass % to 47.1 mass % of HFO-1132(E) based on the entire refrigerant, or


a mixed refrigerant comprising HFO-1132(E) and HFO-1123 in a total amount of 99.5 mass % or more based on the entire refrigerant, and the refrigerant comprising 45.1 mass % to 47.1 mass % of HFO-1132(E) based on the entire refrigerant.


The refrigerant B according to the present disclosure has various properties that are desirable as an R410A-alternative refrigerant, i.e., (1) a coefficient of performance equivalent to that of R410A, (2) a refrigerating capacity equivalent to that of R410A, (3) a sufficiently low GWP, and (4) a lower flammability (Class 2L) according to the ASHRAE standard.


When the refrigerant B according to the present disclosure is a mixed refrigerant comprising 72.0 mass % or less of HFO-1132(E), it has WCF lower flammability. When the refrigerant B according to the present disclosure is a composition comprising 47.1% or less of HFO-1132(E), it has WCF lower flammability and WCFF lower flammability, and is determined to be “Class 2L,” which is a lower flammable refrigerant according to the ASHRAE standard, and which is further easier to handle.


When the refrigerant B according to the present disclosure comprises 62.0 mass % or more of HFO-1132(E), it becomes superior with a coefficient of performance of 95% or more relative to that of R410A, the polymerization reaction of HFO-1132(E) and/or HFO-1123 is further suppressed, and the stability is further improved. When the refrigerant B according to the present disclosure comprises 45.1 mass % or more of HFO-1132(E), it becomes superior with a coefficient of performance of 93% or more relative to that of R410A, the polymerization reaction of HFO-1132(E) and/or HFO-1123 is further suppressed, and the stability is further improved.


The refrigerant B according to the present disclosure may further comprise other additional refrigerants in addition to HFO-1132(E) and HFO-1123, as long as the above properties and effects are not impaired. In this respect, the refrigerant according to the present disclosure preferably comprises HFO-1132(E) and HFO-1123 in a total amount of 99.75 mass % or more, and more preferably 99.9 mass % or more, based on the entire refrigerant.


Such additional refrigerants are not limited, and can be selected from a wide range of refrigerants. The mixed refrigerant may comprise a single additional refrigerant, or two or more additional refrigerants.


(Examples of Refrigerant B)

The present disclosure is described in more detail below with reference to Examples of refrigerant B. However, the refrigerant B is not limited to the Examples.


Mixed refrigerants were prepared by mixing HFO-1132(E) and HFO-1123 at mass % based on their sum shown in Tables 37 and 38.


The GWP of compositions each comprising a mixture of R410A (R32=50%/R125=50%) was evaluated based on the values stated in the Intergovernmental Panel on Climate Change (IPCC), fourth report. The GWP of HFO-1132(E), which was not stated therein, was assumed to be 1 from HFO-1132a (GWP=1 or less) and HFO-1123 (GWP=0.3, described in WO2015/141678). The refrigerating capacity of compositions each comprising R410A and a mixture of HFO-1132(E) and HFO-1123 was determined by performing theoretical refrigeration cycle calculations for the mixed refrigerants using the National Institute of Science and Technology (NIST) and Reference Fluid Thermodynamic and Transport Properties Database (Refprop 9.0) under the following conditions.


Evaporating temperature: 5° C.


Condensation temperature: 45° C.


Superheating temperature: 5 K


Subcooling temperature: 5 K


Compressor efficiency: 70%


The composition of each mixture was defined as WCF. A leak simulation was performed using NIST Standard Reference Data Base Refleak Version 4.0 under the conditions of Equipment, Storage, Shipping, Leak, and Recharge according to the ASHRAE Standard 34-2013. The most flammable fraction was defined as WCFF.


Tables 1 and 2 show GWP, COP, and refrigerating capacity, which were calculated based on these results. The COP and refrigerating capacity are ratios relative to R410A.


The coefficient of performance (COP) was determined by the following formula.





COP=(refrigerating capacity or heating capacity)/power consumption


For the flammability, the burning velocity was measured according to the ANSI/ASHRAE Standard 34-2013. Both WCF and WCFF having a burning velocity of 10 cm/s or less were determined to be “Class 2L (lower flammability).”


A burning velocity test was performed using the apparatus shown in FIG. 1 in the following manner. First, the mixed refrigerants used had a purity of 99.5% or more, and were degassed by repeating a cycle of freezing, pumping, and thawing until no traces of air were observed on the vacuum gauge. The burning velocity was measured by the closed method. The initial temperature was ambient temperature. Ignition was performed by generating an electric spark between the electrodes in the center of a sample cell. The duration of the discharge was 1.0 to 9.9 ms, and the ignition energy was typically about 0.1 to 1.0 J. The spread of the flame was visualized using schlieren photographs. A cylindrical container (inner diameter: 155 mm, length: 198 mm) equipped with two light transmission acrylic windows was used as the sample cell, and a xenon lamp was used as the light source. Schlieren images of the flame were recorded by a high-speed digital video camera at a frame rate of 600 fps and stored on a PC.



















TABLE 37







Com-
Com-






Com-




parative
parative
Com-
Ex-
Ex-
Ex-
Ex-
Ex-
parative




Example 1
Example 2
parative
ample
ample
ample
ample
ample
Example


Item
Unit
R410A
HFO-1132E
Example 3
1
2
3
4
5
4

























HFO-
mass %

100
80
72
70
68
65
62
60


1132E












(WCF)












HFO-
mass %

0
20
28
30
32
35
38
40


1123












(WCF)












GWP

2088
1
1
1
1
1
1
1
1


COP
%
100
99.7
97.5
96.6
96.3
96.1
95.8
95.4
95.2


ratio
(relative












to












R410A)











Refrig-
%
100
98.3
101.9
103.1
103.4
103.8
104.1
104.5
104.8


erating
(relative











capacity
to











ratio
R410A)











Discharge
Mpa
2.73
2.71
2.89
2.96
2.98
3.00
3.02
3.04
3.06


pressure












Burning
cm/sec
Non-
20
13
10
9
9
8
8 or less
8 or less


velocity

flammable










(WCF)


























TABLE 38















Com-












parative




Com-
Com-
Ex-
Ex-
Ex-
Com-
Com-
Com-
Example 10




parative
parative
ample
ample
ample
parative
parative
parative
HFO-


Item
Unit
Example 5
Example 6
7
8
9
Example 7
Example 8
Example 9
1123

























HFO-
mass %
50
48
47.1
46.1
45.1
43
40
25
0


1132E












(WCF)












HFO-1123
mass %
50
52
52.9
53.9
54.9
57
60
75
100


(WCF)












GWP

1
1
1
1
1
1
1
1
1


COP ratio
%
94.1
93.9
93.8
93.7
93.6
93.4
93.1
91.9
90.6



(relative












to












R410A)











Refrigerating
%
105.9
106.1
106.2
106.3
106.4
106.6
106.9
107.9
108.0


capacity
(relative











ratio
to












R410A)











Discharge
Mpa
3.14
3.16
3.16
3.17
3.18
3.20
3.21
3.31
3.39


pressure


























Leakage test
Storage/
Storage/
Storage/
Storage/
Storage/
Storage/
Storage/
Storage/



conditions
Shipping
Shipping
Shipping
Shipping
Shipping
Shipping
Shipping
Shipping



(WCFF)
−40° C.,
−40° C.,
−40° C.,
−40° C.,
−40° C.,
−40° C.,
−40° C.,
−40° C.,




92%
92%
92%
92%
92%
92%
92%
90%




release,
release,
release,
release,
release,
release,
release,
release,




liquid
liquid
liquid
liquid
liquid
liquid
liquid
liquid




phase
phase
phase
phase
phase
phase
phase
phase




side
side
side
side
side
side
side
side


















HFO-1132E
mass %
74
73
72
71
70
67
63
38



(WCFF)












HFO-1123
mass %
26
27
28
29
30
33
37
62



(WCFF)












Burning
cm/sec
8 or less
8 or less
8 or
8 or
8 or
8 or less
8 or less
8 or less
5


velocity



less
less
less






(WCF)












Burning
cm/sec
11
10.5
10.0
9.5
9.5
8.5
8 or less
8 or less



velocity












(WCFF)


























ASHRAE flammability
2
2
2 L
2 L
2 L
2 L
2 L
2 L
2 L


classification


















The compositions each comprising 62.0 mass % to 72.0 mass % of HFO-1132(E) based on the entire composition are stable while having a low GWP (GWP=1), and they ensure WCF lower flammability. Further, surprisingly, they can ensure performance equivalent to that of R410A. Moreover, compositions each comprising 45.1 mass % to 47.1 mass % of HFO-1132(E) based on the entire composition are stable while having a low GWP (GWP=1), and they ensure WCFF lower flammability. Further, surprisingly, they can ensure performance equivalent to that of R410A.


(5-3) Refrigerant C

The refrigerant C according to the present disclosure is a composition comprising trans-1,2-difluoroethylene (HFO-1132(E)), trifluoroethylene (HFO-1123), 2,3,3,3-tetrafluoro-1-propene (R1234yf), and difluoromethane (R32), and satisfies the following requirements. The refrigerant C according to the present disclosure has various properties that are desirable as an alternative refrigerant for R410A; i.e. it has a coefficient of performance and a refrigerating capacity that are equivalent to those of R410A, and a sufficiently low GWP.


Requirements

Preferable refrigerant C is as follows:


When the mass % of HFO-1132(E), HFO-1123, R1234yf, and R32 based on their sum is respectively represented by x, y, z, and a,


if 0<a≤11.1, coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R1234yf is (100−a) mass % are within the range of a figure surrounded by straight lines GI, IA, AB, BD′, D′C, and CG that connect the following 6 points:


point G (0.026a2−1.7478a+72.0, −0.026a2+0.7478a+28.0, 0.0),


point I (0.026a2−1.7478a+72.0, 0.0, −0.026a2+0.7478a+28.0),


point A (0.0134a2−1.9681a+68.6, 0.0, −0.0134a2+0.9681a+31.4),


point B (0.0, 0.0144a2−1.6377a+58.7, −0.0144a2+0.6377a+41.3),


point D′ (0.0, 0.0224a2+0.968a+75.4, −0.0224a2−1.968a+24.6), and


point C (−0.2304a2−0.4062a+32.9, 0.2304a2−0.5938a+67.1, 0.0),


or on the straight lines GI, AB, and D′C (excluding point G, point I, point A, point B, point D′, and point C);


if 11.1<a≤18.2, coordinates (x,y,z) in the ternary composition diagram are within the range of a figure surrounded by straight lines GI, IA, AB, BW, and WG that connect the following 5 points:


point G (0.02a2−1.6013a+71.105, −0.02a2+0.6013a+28.895, 0.0),


point I (0.02a2−1.6013a+71.105, 0.0, −0.02a2+0.6013a+28.895),


point A (0.0112a2−1.9337a+68.484, 0.0, −0.0112a2+0.9337a+31.516),


point B (0.0, 0.0075a2−1.5156a+58.199, −0.0075a2+0.5156a+41.801) and


point W (0.0, 100.0−a, 0.0),


or on the straight lines GI and AB (excluding point G, point I, point A, point B, and point W);


if 18.2<a≤26.7, coordinates (x,y,z) in the ternary composition diagram are within the range of a figure surrounded by straight lines GI, IA, AB, BW, and WG that connect the following 5 points:


point G (0.0135a2−1.4068a+69.727, −0.0135a2+0.4068a+30.273, 0.0),


point I (0.0135a2−1.4068a+69.727, 0.0, −0.0135a2+0.4068a+30.273),


point A (0.0107a2−1.9142a+68.305, 0.0, −0.0107a2+0.9142a+31.695),


point B (0.0, 0.009a2−1.6045a+59.318, −0.009a2+0.6045a+40.682) and


point W (0.0, 100.0−a, 0.0),


or on the straight lines GI and AB (excluding point G, point I, point A, point B, and point W);


if 26.7<a≤36.7, coordinates (x,y,z) in the ternary composition diagram are within the range of a figure surrounded by straight lines GI, IA, AB, BW, and WG that connect the following 5 points:


point G (0.0111a2−1.3152a+68.986, −0.0111a2+0.3152a+31.014, 0.0),


point I (0.0111a2−1.3152a+68.986, 0.0, −0.0111a2+0.3152a+31.014),


point A (0.0103a2−1.9225a+68.793, 0.0, −0.0103a2+0.9225a+31.207),


point B (0.0, 0.0046a2−1.41a+57.286, −0.0046a2+0.41a+42.714) and


point W (0.0, 100.0−a, 0.0),


or on the straight lines GI and AB (excluding point G, point I, point A, point B, and point W); and


if 36.7<a≤46.7, coordinates (x,y,z) in the ternary composition diagram are within the range of a figure surrounded by straight lines GI, IA, AB, BW, and WG that connect the following 5 points:


point G (0.0061a2−0.9918a+63.902, −0.0061a2−0.0082a+36.098, 0.0),


point I (0.0061a2−0.9918a+63.902, 0.0, −0.0061a2−0.0082a+36.098),


point A (0.0085a2−1.8102a+67.1, 0.0, −0.0085a2+0.8102a+32.9),


point B (0.0, 0.0012a2−1.1659a+52.95, −0.0012a2+0.1659a+47.05) and


point W (0.0, 100.0−a, 0.0),


or on the straight lines GI and AB (excluding point G, point I, point A, point B, and point W). When the refrigerant according to the present disclosure satisfies the above requirements, it has a refrigerating capacity ratio of 85% or more relative to that of R410A, and a COP ratio of 92.5% or more relative to that of R410A, and further ensures a WCF lower flammability.


The refrigerant C according to the present disclosure is preferably a refrigerant wherein


when the mass % of HFO-1132(E), HFO-1123, and R1234yf based on their sum is respectively represented by x, y, and z,


if 0<a≤11.1, coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R1234yf is (100−a) mass % are within the range of a figure surrounded by straight lines JK′, K′B, BD′, D′C, and CJ that connect the following 5 points:


point J (0.0049a2−0.9645a+47.1, −0.0049a2−0.0355a+52.9, 0.0),


point K′ (0.0514a2−2.4353a+61.7, −0.0323a2+0.4122a+5.9, −0.0191a2+1.0231a+32.4),


point B (0.0, 0.0144a2−1.6377a+58.7, −0.0144a2+0.6377a+41.3),


point D′ (0.0, 0.0224a2+0.968a+75.4, −0.0224a2−1.968a+24.6), and


point C (−0.2304a2−0.4062a+32.9, 0.2304a2−0.5938a+67.1, 0.0),


or on the straight lines JK′, K′B, and D′C (excluding point J, point B, point D′, and point C);


if 11.1<a≤18.2, coordinates (x,y,z) in the ternary composition diagram are within the range of a figure surrounded by straight lines JK′, K′B, BW, and WJ that connect the following 4 points:


point J (0.0243a2−1.4161a+49.725, −0.0243a2+0.4161a+50.275, 0.0),


point K′ (0.0341a2−2.1977a+61.187, −0.0236a2+0.34a+5.636,−0.0105a2+0.8577a+33.177),


point B (0.0, 0.0075a2−1.5156a+58.199, −0.0075a2+0.5156a+41.801) and


point W (0.0, 100.0−a, 0.0),


or on the straight lines JK′ and K′B (excluding point J, point B, and point W);


if 18.2<a≤26.7, coordinates (x,y,z) in the ternary composition diagram are within the range of a figure surrounded by straight lines JK′, K′B, BW, and WJ that connect the following 4 points:


point J (0.0246a2−1.4476a+50.184, −0.0246a2+0.4476a+49.816, 0.0),


point K′ (0.0196a2−1.7863a+58.515, −0.0079a2−0.1136a+8.702, −0.0117a2+0.8999a+32.783),


point B (0.0, 0.009a2−1.6045a+59.318, −0.009a2+0.6045a+40.682) and


point W (0.0, 100.0−a, 0.0),


or on the straight lines JK′ and K′B (excluding point J, point B, and point W);


if 26.7<a≤36.7, coordinates (x,y,z) in the ternary composition diagram are within the range of a figure surrounded by straight lines JK′, K′A, AB, BW, and WJ that connect the following 5 points:


point J (0.0183a2−1.1399a+46.493, −0.0183a2+0.1399a+53.507, 0.0),


point K′ (−0.0051a2+0.0929a+25.95, 0.0, 0.0051a2−1.0929a+74.05),


point A (0.0103a2−1.9225a+68.793, 0.0, −0.0103a2+0.9225a+31.207),


point B (0.0, 0.0046a2−1.41a+57.286, −0.0046a2+0.41a+42.714) and


point W (0.0, 100.0−a, 0.0),


or on the straight lines JK′, K′A, and AB (excluding point J, point B, and point W); and


if 36.7<a≤46.7, coordinates (x,y,z) in the ternary composition diagram are within the range of a figure surrounded by straight lines JK′, K′A, AB, BW, and WJ that connect the following 5 points:


point J (−0.0134a2+1.0956a+7.13, 0.0134a2−2.0956a+92.87, 0.0),


point K′ (−1.892a+29.443, 0.0, 0.892a+70.557),


point A (0.0085a2−1.8102a+67.1, 0.0, −0.0085a2+0.8102a+32.9),


point B (0.0, 0.0012a2−1.1659a+52.95, −0.0012a2+0.1659a+47.05) and


point W (0.0, 100.0−a, 0.0),


or on the straight lines JK′, K′A, and AB (excluding point J, point B, and point W). When the refrigerant according to the present disclosure satisfies the above requirements, it has a refrigerating capacity ratio of 85% or more relative to that of R410A, and a COP ratio of 92.5% or more relative to that of R410A. Additionally, the refrigerant has a WCF lower flammability and a WCFF lower flammability, and is classified as “Class 2L,” which is a lower flammable refrigerant according to the ASHRAE standard.


When the refrigerant C according to the present disclosure further contains R32 in addition to HFO-1132 (E), HFO-1123, and R1234yf, the refrigerant may be a refrigerant wherein when the mass % of HFO-1132(E), HFO-1123, R1234yf, and R32 based on their sum is respectively represented by x, y, z, and a,


if 0<a≤10.0, coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R1234yf is (100−a) mass % are within the range of a figure surrounded by straight lines that connect the following 4 points:


point a (0.02a2−2.46a+93.4, 0, −0.02a2+2.46a+6.6),


point b′ (−0.008a2−1.38a+56, 0.018a2−0.53a+26.3, −0.01a2+1.91a+17.7),


point c (−0.016a2+1.02a+77.6, 0.016a2−1.02a+22.4, 0), and


point o (100.0−a, 0.0, 0.0)


or on the straight lines oa, ab′, and b′c (excluding point o and point c);


if 10.0<a≤16.5, coordinates (x,y,z) in the ternary composition diagram are within the range of a figure surrounded by straight lines that connect the following 4 points:


point a (0.0244a2−2.5695a+94.056, 0, −0.0244a2+2.5695a+5.944),


point b′ (0.1161a2−1.9959a+59.749, 0.014a2−0.3399a+24.8, −0.1301a2+2.3358a+15.451),


point c (−0.0161a2+1.02a+77.6, 0.0161a2−1.02a+22.4, 0), and


point o (100.0−a, 0.0, 0.0),


or on the straight lines oa, ab′, and b′c (excluding point o and point c); or


if 16.5<a≤21.8, coordinates (x,y,z) in the ternary composition diagram are within the range of a figure surrounded by straight lines that connect the following 4 points:


point a (0.0161a2−2.3535a+92.742, 0, −0.0161a2+2.3535a+7.258),


point b′ (−0.0435a2−0.0435a+50.406, 0.0304a2+1.8991a−0.0661, 0.0739a2−1.8556a+49.6601),


point c (−0.0161a2+0.9959a+77.851, 0.0161a2−0.9959a+22.149, 0), and


point o (100.0−a, 0.0, 0.0),


or on the straight lines oa, ab′, and b′c (excluding point o and point c). Note that when point b in the ternary composition diagram is defined as a point where a refrigerating capacity ratio of 95% relative to that of R410A and a COP ratio of 95% relative to that of R410A are both achieved, point b′ is the intersection of straight line ab and an approximate line formed by connecting the points where the COP ratio relative to that of R410A is 95%. When the refrigerant according to the present disclosure meets the above requirements, the refrigerant has a refrigerating capacity ratio of 95% or more relative to that of R410A, and a COP ratio of 95% or more relative to that of R410A.


The refrigerant C according to the present disclosure may further comprise other additional refrigerants in addition to HFO-1132(E), HFO-1123, R1234yf, and R32 as long as the above properties and effects are not impaired. In this respect, the refrigerant according to the present disclosure preferably comprises HFO-1132(E), HFO-1123, R1234yf, and R32 in a total amount of 99.5 mass % or more, more preferably 99.75 mass % or more, and still more preferably 99.9 mass % or more, based on the entire refrigerant.


The refrigerant C according to the present disclosure may comprise HFO-1132(E), HFO-1123, R1234yf, and R32 in a total amount of 99.5 mass % or more, 99.75 mass % or more, or 99.9 mass % or more, based on the entire refrigerant.


Additional refrigerants are not particularly limited and can be widely selected. The mixed refrigerant may contain one additional refrigerant, or two or more additional refrigerants.


(Examples of Refrigerant C)

The present disclosure is described in more detail below with reference to Examples of refrigerant C. However, the refrigerant C is not limited to the Examples.


Mixed refrigerants were prepared by mixing HFO-1132(E), HFO-1123, R1234yf, and R32 at mass % based on their sum shown in Tables 39 to 96.


The GWP of compositions each comprising a mixture of R410A (R32=50%/R125=50%) was evaluated based on the values stated in the Intergovernmental Panel on Climate Change (IPCC), fourth report. The GWP of HFO-1132(E), which was not stated therein, was assumed to be 1 from HFO-1132a (GWP=1 or less) and HFO-1123 (GWP=0.3, described in WO2015/141678). The refrigerating capacity of compositions each comprising R410A and a mixture of HFO-1132(E) and HFO-1123 was determined by performing theoretical refrigeration cycle calculations for the mixed refrigerants using the National Institute of Science and Technology (NIST) and Reference Fluid Thermodynamic and Transport Properties Database (Refprop 9.0) under the following conditions.


For each of these mixed refrigerants, the COP ratio and the refrigerating capacity ratio relative to those of R410 were obtained. Calculation was conducted under the following conditions.


Evaporating temperature: 5° C.


Condensation temperature: 45° C.


Superheating temperature: 5 K


Subcooling temperature: 5 K


Compressor efficiency: 70%


Tables 39 to 96 show the resulting values together with the GWP of each mixed refrigerant. The COP and refrigerating capacity are ratios relative to R410A.


The coefficient of performance (COP) was determined by the following formula.





COP=(refrigerating capacity or heating capacity)/power consumption



















TABLE 39








Comp.
Comp.
Comp.
Comp.
Comp.
Comp.
Comp.





Comp.
Ex. 2
Ex. 3
Ex. 4
Ex. 5
Ex. 6
Ex. 7
Ex. 8
Ex. 1


Item
Unit
Ex. 1
A
B
C
D′
G
I
J
K′

























HFO-1132(E)
Mass %
R410A
68.6
0.0
32.9
0.0
72.0
72.0
47.1
61.7


HFO-1123
Mass %

0.0
58.7
67.1
75.4
28.0
0.0
52.9
5.9


R1234yf
Mass %

31.4
41.3
0.0
24.6
0.0
28.0
0.0
32.4


R32
Mass %

0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0


GWP

2088
2
2
1
2
1
2
1
2


COP ratio
% (relative to
100
100.0
95.5
92.5
93.1
96.6
99.9
93.8
99.4



R410A)











Refrigerating
% (relative to
100
85.0
85.0
107.4
95.0
103.1
86.6
106.2
85.5


capacity ratio
R410A)

























TABLE 40







Comp.
Comp.
Comp.


Comp.
Comp.





Ex. 9
Ex. 10
Ex. 11
Comp. Ex. 12
Comp. Ex. 13
Ex. 14
Ex. 15
Ex. 2


Item
Unit
A
B
C
D′
G
I
J
K′
























HFO-1132
Mass %
55.3
0.0
18.4
0.0
60.9
60.9
40.5
47.0


(E)











HFO-1123
Mass %
0.0
47.8
74.5
83.4
32.0
0.0
52.4
7.2


R1234yf
Mass %
37.6
45.1
0.0
9.5
0.0
32.0
0.0
38.7


R32
Mass %
7.1
7.1
7.1
7.1
7.1
7.1
7.1
7.1


GWP

50
50
49
49
49
50
49
50


COP ratio
%
99.8
96.9
92.5
92.5
95.9
99.6
94.0
99.2



(relative











to R410A)










Refrigerating
%
85.0
85.0
110.5
106.0
106.5
87.7
108.9
85.5


capacity ratio
(relative











to R410A)
























TABLE 41







Comp.
Comp.
Comp.
Comp.







Ex. 16
Ex. 17
Ex. 18
Ex. 19
Comp. Ex. 20
Comp. Ex. 21
Ex. 3


Item
Unit
A
B
C = D′
G
I
J
K′























HFO-1132(E)
Mass %
48.4
0.0
0.0
55.8
55.8
37.0
41.0


HFO-1123
Mass %
0.0
42.3
88.9
33.1
0.0
51.9
6.5


R1234yf
Mass %
40.5
46.6
0.0
0.0
33.1
0.0
41.4


R32
Mass %
11.1
11.1
11.1
11.1
11.1
11.1
11.1


GWP

77
77
76
76
77
76
77


COP ratio
%
99.8
97.6
92.5
95.8
99.5
94.2
99.3



(relative










to R410A)









Refrigerating
%
85.0
85.0
112.0
108.0
88.6
110.2
85.4


capacity ratio
(relative










to R410A)























TABLE 42







Comp. Ex.
Comp. Ex.
Comp. Ex.
Comp. Ex.
Comp. Ex.





22
23
24
25
26
Ex. 4


Item
Unit
A
B
G
I
J
K′






















HFO-1132(E)
Mass %
42.8
0.0
52.1
52.1
34.3
36.5


HFO-1123
Mass %
0.0
37.8
33.4
0.0
51.2
5.6


R1234yf
Mass %
42.7
47.7
0.0
33.4
0.0
43.4


R32
Mass %
14.5
14.5
14.5
14.5
14.5
14.5


GWP

100
100
99
100
99
100


COP ratio
% (relative to
99.9
98.1
95.8
99.5
94.4
99.5



R410A)








Refrigerating
% (relative to
85.0
85.0
109.1
89.6
111.1
85.3


capacity ratio
R410A)























TABLE 43







Comp. Ex.
Comp. Ex.
Comp. Ex.
Comp. Ex.
Comp. Ex.





27
28
29
30
31
Ex. 5


Item
Unit
A
B
G
I
J
K′






















HFO-1132(E)
Mass %
37.0
0.0
48.6
48.6
32.0
32.5


HFO-1123
Mass %
0.0
33.1
33.2
0.0
49.8
4.0


R1234yf
Mass %
44.8
48.7
0.0
33.2
0.0
45.3


R32
Mass %
18.2
18.2
18.2
18.2
18.2
18.2


GWP

125
125
124
125
124
125


COP ratio
% (relative to
100.0
98.6
95.9
99.4
94.7
99.8



R410A)








Refrigerating
% (relative to
85.0
85.0
110.1
90.8
111.9
85.2


capacity ratio
R410A)























TABLE 44







Comp. Ex.
Comp. Ex.
Comp. Ex.
Comp. Ex.
Comp. Ex.





32
33
34
35
36
Ex. 6


Item
Unit
A
B
G
I
J
K′






















HFO-1132(E)
Mass %
31.5
0.0
45.4
45.4
30.3
28.8


HFO-1123
Mass %
0.0
28.5
32.7
0.0
47.8
2.4


R1234yf
Mass %
46.6
49.6
0.0
32.7
0.0
46.9


R32
Mass %
21.9
21.9
21.9
21.9
21.9
21.9


GWP

150
150
149
150
149
150


COP ratio
% (relative to
100.2
99.1
96.0
99.4
95.1
100.0



R410A)








Refrigerating
% (relative to
85.0
85.0
111.0
92.1
112.6
85.1


capacity ratio
R410A)























TABLE 45












Comp. Ex.




Comp. Ex. 37
Comp. Ex. 38
Comp. Ex. 39
Comp. Ex. 40
Comp. Ex. 41
42


Item
Unit
A
B
G
I
J
K′






















HFO-1132(E)
Mass %
24.8
0.0
41.8
41.8
29.1
24.8


HFO-1123
Mass %
0.0
22.9
31.5
0.0
44.2
0.0


R1234yf
Mass %
48.5
50.4
0.0
31.5
0.0
48.5


R32
Mass %
26.7
26.7
26.7
26.7
26.7
26.7


GWP

182
182
181
182
181
182


COP ratio
% (relative to
100.4
99.8
96.3
99.4
95.6
100.4



R410A)








Refrigerating
% (relative to
85.0
85.0
111.9
93.8
113.2
85.0


capacity ratio
R410A)























TABLE 46







Comp. Ex.
Comp. Ex.
Comp. Ex.
Comp. Ex.
Comp. Ex.
Comp. Ex.




43
44
45
46
47
48


Item
Unit
A
B
G
I
J
K′






















HFO-1132(E)
Mass %
21.3
0.0
40.0
40.0
28.8
24.3


HFO-1123
Mass %
0.0
19.9
30.7
0.0
41.9
0.0


R1234yf
Mass %
49.4
50.8
0.0
30.7
0.0
46.4


R32
Mass %
29.3
29.3
29.3
29.3
29.3
29.3


GWP

200
200
198
199
198
200


COP ratio
% (relative to
100.6
100.1
96.6
99.5
96.1
100.4



R410A)








Refrigerating
% (relative to
85.0
85.0
112.4
94.8
113.6
86.7


capacity ratio
R410A)























TABLE 47







Comp. Ex.
Comp. Ex.
Comp. Ex.
Comp. Ex.
Comp. Ex.
Comp. Ex.




49
50
51
52
53
54


Item
Unit
A
B
G
I
J
K′






















HFO-1132(E)
Mass %
12.1
0.0
35.7
35.7
29.3
22.5


HFO-1123
Mass %
0.0
11.7
27.6
0.0
34.0
0.0


R1234yf
Mass %
51.2
51.6
0.0
27.6
0.0
40.8


R32
Mass %
36.7
36.7
36.7
36.7
36.7
36.7


GWP

250
250
248
249
248
250


COP ratio
% (relative to
101.2
101.0
96.4
99.6
97.0
100.4



R410A)








Refrigerating
% (relative to
85.0
85.0
113.2
97.6
113.9
90.9


capacity ratio
R410A)























TABLE 48







Comp. Ex.
Comp. Ex.
Comp. Ex.
Comp. Ex.
Comp. Ex.
Comp. Ex.




55
56
57
58
59
60


Item
Unit
A
B
G
I
J
K′






















HFO-1132(E)
Mass %
3.8
0.0
32.0
32.0
29.4
21.1


HFO-1123
Mass %
0.0
3.9
23.9
0.0
26.5
0.0


R1234yf
Mass %
52.1
52.0
0.0
23.9
0.0
34.8


R32
Mass %
44.1
44.1
44.1
44.1
44.1
44.1


GWP

300
300
298
299
298
299


COP ratio
% (relative to
101.8
101.8
97.9
99.8
97.8
100.5



R410A)








Refrigerating
% (relative to
85.0
85.0
113.7
100.4
113.9
94.9


capacity ratio
R410A)






















TABLE 49







Comp. Ex.
Comp. Ex.
Comp. Ex.






61
62
63
Comp. Ex. 64
Comp. Ex. 65


Item
Unit
A = B
G
I
J
K′





















HFO-1132(E)
Mass %
0.0
30.4
30.4
28.9
20.4


HFO-1123
Mass %
0.0
21.8
0.0
23.3
0.0


R1234yf
Mass %
52.2
0.0
21.8
0.0
31.8


R32
Mass %
47.8
47.8
47.8
47.8
47.8


GWP

325
323
324
323
324


COP ratio
% (relative to
102.1
98.2
100.0
98.2
100.6



R410A)







Refrigerating
% (relative to
85.0
113.8
101.8
113.9
96.8


capacity ratio
R410A)

























TABLE 50







Comp. Ex.



Ex.
Ex.
Ex.
Ex.


Item
Unit
66
Ex. 7
Ex. 8
Ex. 9
10
11
12
13
























HFO-1132(E)
Mass %
5.0
10.0
15.0
20.0
25.0
30.0
35.0
40.0


HFO-1123
Mass %
82.9
77.9
72.9
67.9
62.9
57.9
52.9
47.9


R1234yf
Mass %
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0


R32
Mass %
7.1
7.1
7.1
7.1
7.1
7.1
7.1
7.1


GWP

49
49
49
49
49
49
49
49


COP ratio
% (relative to
92.4
92.6
92.8
93.1
93.4
93.7
94.1
94.5



R410A)










Refrigerating
% (relative to
108.4
108.3
108.2
107. 9
107.6
107.2
106.8
106.3


capacity ratio
R410A)

































TABLE 51











Comp. Ex.
Ex.
Ex.
Ex.


Item
Unit
Ex. 14
Ex. 15
Ex. 16
Ex. 17
67
18
19
20
























HFO-1132(E)
Mass %
45.0
50.0
55.0
60.0
65.0
10.0
15.0
20.0


HFO-1123
Mass %
42.9
37.9
32.9
27.9
22.9
72.9
67.9
62.9


R1234yf
Mass %
5.0
5.0
5.0
5.0
5.0
10.0
10.0
10.0


R32
Mass %
7.1
7.1
7.1
7.1
7.1
7.1
7.1
7.1


GWP

49
49
49
49
49
49
49
49


COP ratio
% (relative to
95.0
95.4
95.9
96.4
96.9
93.0
93.3
93.6



R410A)










Refrigerating
% (relative to
105.8
105.2
104.5
103.9
103.1
105.7
105.5
105.2


capacity ratio
R410A)

























TABLE 52





Item
Unit
Ex. 21
Ex. 22
Ex. 23
Ex. 24
Ex. 25
Ex. 26
Ex. 27
Ex. 28
























HFO-1132(E)
Mass %
25.0
30.0
35.0
40.0
45.0
50.0
55.0
60.0


HFO-1123
Mass %
57.9
52.9
47.9
42.9
37.9
32.9
27.9
22.9


R1234yf
Mass %
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0


R32
Mass %
7.1
7.1
7.1
7.1
7.1
7.1
7.1
7.1


GWP

49
49
49
49
49
49
49
49


COP ratio
% (relative
93.9
94.2
94.6
95.0
95.5
96.0
96.4
96.9



to R410A)










Refrigerating
% (relative
104.9
104.5
104.1
103.6
103.0
102.4
101.7
101.0


capacity ratio
to R410A)

























TABLE 53







Comp. Ex.
Ex.
Ex.
Ex.
Ex.
Ex.
Ex.
Ex.


Item
Unit
68
29
30
31
32
33
34
35
























HFO-1132(E)
Mass %
65.0
10.0
15.0
20.0
25.0
30.0
35.0
40.0


HFO-1123
Mass %
17.9
67.9
62.9
57.9
52.9
47.9
42.9
37.9


R1234yf
Mass %
10.0
15.0
15.0
15.0
15.0
15.0
15.0
15.0


R32
Mass %
7.1
7.1
7.1
7.1
7.1
7.1
7.1
7.1


GWP

49
49
49
49
49
49
49
49


COP ratio
% (relative
97.4
93.5
93.8
94.1
94.4
94.8
95.2
95.6



to R410A)










Refrigerating
% (relative
100.3
102.9
102.7
102.5
102.1
101.7
101.2
100.7


capacity ratio
to R410A)

























TABLE 54







Ex.
Ex.
Ex.
Ex.
Comp. Ex.
Ex.
Ex.
Ex.


Item
Unit
36
37
38
39
69
40
41
42
























HFO-1132(E)
Mass %
45.0
50.0
55.0
60.0
65.0
10.0
15.0
20.0


HFO-1123
Mass %
32.9
27.9
22.9
17.9
12.9
62.9
57.9
52.9


R1234yf
Mass %
15.0
15.0
15.0
15.0
15.0
20.0
20.0
20.0


R32
Mass %
7.1
7.1
7.1
7.1
7.1
7.1
7.1
7.1


GWP

49
49
49
49
49
49
49
49


COP ratio
% (relative
96.0
96.5
97.0
97.5
98.0
94.0
94.3
94.6



to R410A)










Refrigerating
% (relative
100.1
99.5
98.9
98.1
97.4
100.1
99.9
99.6


capacity ratio
to R410A)

























TABLE 55





Item
Unit
Ex. 43
Ex. 44
Ex. 45
Ex. 46
Ex. 47
Ex. 48
Ex. 49
Ex. 50
























HFO-1132(E)
Mass %
25.0
30.0
35.0
40.0
45.0
50.0
55.0
60.0


HFO-1123
Mass %
47.9
42.9
37.9
32.9
27.9
22.9
17.9
12.9


R1234yf
Mass %
20.0
20.0
20.0
20.0
20.0
20.0
20.0
20.0


R32
Mass %
7.1
7.1
7.1
7.1
7.1
7.1
7.1
7.1


GWP

49
49
49
49
49
49
49
49


COP ratio
% (relative
95.0
95.3
95.7
96.2
96.6
97.1
97.6
98.1



to R410A)










Refrigerating
% (relative
99.2
98.8
98.3
97.8
97.2
96.6
95.9
95.2


capacity ratio
to R410A)

























TABLE 56







Comp. Ex.
Ex.
Ex.
Ex.
Ex.
Ex.
Ex.
Ex.


Item
Unit
70
51
52
53
54
55
56
57
























HFO-1132(E)
Mass %
65.0
10.0
15.0
20.0
25.0
30.0
35.0
40.0


HFO-1123
Mass %
7.9
57.9
52.9
47.9
42.9
37.9
32.9
27.9


R1234yf
Mass %
20.0
25.0
25.0
25.0
25.0
25.0
25.0
25.0


R32
Mass %
7.1
7.1
7.1
7.1
7.1
7.1
7.1
7.1


GWP

49
50
50
50
50
50
50
50


COP ratio
% (relative
98.6
94.6
94.9
95.2
95.5
95.9
96.3
96.8



to R410A)










Refrigerating
% (relative
94.4
97.1
96.9
96.7
96.3
95.9
95.4
94.8


capacity ratio
to R410A)

























TABLE 57







Ex.
Ex.
Ex.
Ex.
Comp. Ex.
Ex.
Ex.
Ex.


Item
Unit
58
59
60
61
71
62
63
64
























HFO-1132(E)
Mass %
45.0
50.0
55.0
60.0
65.0
10.0
15.0
20.0


HFO-1123
Mass %
7.1
7.1
7.1
7.1
7.1
7.1
7.1
7.1


R1234yf
Mass %
25.0
25.0
25.0
25.0
25.0
30.0
30.0
30.0


R32
Mass %
7.1
7.1
7.1
7.1
7.1
7.1
7.1
7.1


GWP

50
50
50
50
50
50
50
50


COP ratio
% (relative
97.2
97.7
98.2
98.7
99.2
95.2
95.5
95.8



to R410A)










Refrigerating
% (relative
94.2
93.6
92.9
92.2
91.4
94.2
93.9
93.7


capacity ratio
to R410A)

























TABLE 58





Item
Unit
Ex. 65
Ex. 66
Ex. 67
Ex. 68
Ex. 69
Ex. 70
Ex. 71
Ex. 72
























HFO-1132(E)
Mass %
25.0
30.0
35.0
40.0
45.0
50.0
55.0
60.0


HFO-1123
Mass %
37.9
32.9
27.9
22.9
17.9
12.9
7.9
2.9


R1234yf
Mass %
30.0
30.0
30.0
30.0
30.0
30.0
30.0
30.0


R32
Mass %
7.1
7.1
7.1
7.1
7.1
7.1
7.1
7.1


GWP

50
50
50
50
50
50
50
50


COP ratio
% (relative
96.2
96.6
97.0
97.4
97.9
98.3
98.8
99.3



to R410A)










Refrigerating
% (relative
93.3
92.9
92.4
91.8
91.2
90.5
89.8
89.1


capacity ratio
to R410A)

























TABLE 59





Item
Unit
Ex. 73
Ex. 74
Ex. 75
Ex. 76
Ex. 77
Ex. 78
Ex. 79
Ex. 80
























HFO-1132(E)
Mass %
10.0
15.0
20.0
25.0
30.0
35.0
40.0
45.0


HFO-1123
Mass %
47.9
42.9
37.9
32.9
27.9
22.9
17.9
12.9


R1234yf
Mass %
35.0
35.0
35.0
35.0
35.0
35.0
35.0
35.0


R32
Mass %
7.1
7.1
7.1
7.1
7.1
7.1
7.1
7.1


GWP

50
50
50
50
50
50
50
50


COP ratio
% (relative
95.9
96.2
96.5
96.9
97.2
97.7
98.1
98.5



to R410A)










Refrigerating
% (relative
91.1
90.9
90.6
90.2
89.8
89.3
88.7
88.1


capacity ratio
to R410A)

























TABLE 60





Item
Unit
Ex. 81
Ex. 82
Ex. 83
Ex. 84
Ex. 85
Ex. 86
Ex. 87
Ex. 88
























HFO-1132(E)
Mass %
50.0
55.0
10.0
15.0
20.0
25.0
30.0
35.0


HFO-1123
Mass %
7.9
2.9
42.9
37.9
32.9
27.9
22.9
17.9


R1234yf
Mass %
35.0
35.0
40.0
40.0
40.0
40.0
40.0
40.0


R32
Mass %
7.1
7.1
7.1
7.1
7.1
7.1
7.1
7.1


GWP

50
50
50
50
50
50
50
50


COP ratio
% (relative
99.0
99.4
96.6
96.9
97.2
97.6
98.0
98.4



to R410A)










Refrigerating
% (relative
87.4
86.7
88.0
87.8
87.5
87.1
86.6
86.1


capacity ratio
to R410A)

























TABLE 61







Comp.
Comp.
Comp.
Comp.
Comp.
Comp.
Comp.
Comp.


Item
Unit
Ex. 72
Ex. 73
Ex. 74
Ex. 75
Ex. 76
Ex. 77
Ex. 78
Ex. 79
























HFO-1132(E)
Mass %
40.0
45.0
50.0
10.0
15.0
20.0
25.0
30.0


HFO-1123
Mass %
12.9
7.9
2.9
37.9
32.9
27.9
22.9
17.9


R1234yf
Mass %
40.0
40.0
40.0
45.0
45.0
45.0
45.0
45.0


R32
Mass %
7.1
7.1
7.1
7.1
7.1
7.1
7.1
7.1


GWP

50
50
50
50
50
50
50
50


COP ratio
% (relative
98.8
99.2
99.6
97.4
97.7
98.0
98.3
98.7



to R410A)










Refrigerating
% (relative
85.5
84.9
84.2
84.9
84.6
84.3
83.9
83.5


capacity ratio
to R410A)




















TABLE 62







Comp.
Comp.
Comp.


Item
Unit
Ex. 80
Ex. 81
Ex. 82



















HFO-1132(E)
Mass %
35.0
40.0
45.0


HFO-1123
Mass %
12.9
7.9
2.9


R1234yf
Mass %
45.0
45.0
45.0


R32
Mass %
7.1
7.1
7.1


GWP

50
50
50


COP ratio
% (relative to R410A)
99.1
99.5
99.9


Refrigerating
% (relative to R410A)
82.9
82.3
81.7


capacity ratio





























TABLE 63





Item
Unit
Ex. 89
Ex. 90
Ex. 91
Ex. 92
Ex. 93
Ex. 94
Ex. 95
Ex. 96
























HFO-1132(E)
Mass %
10.0
15.0
20.0
25.0
30.0
35.0
40.0
45.0


HFO-1123
Mass %
70.5
65.5
60.5
55.5
50.5
45.5
40.5
35.5


R1234yf
Mass %
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0


R32
Mass %
14.5
14.5
14.5
14.5
14.5
14.5
14.5
14.5


GWP

99
99
99
99
99
99
99
99


COP ratio
% (relative
93.7
93.9
94.1
94.4
94.7
95.0
95.4
95.8



to R410A)










Refrigerating
% (relative
110.2
110.0
109.7
109.3
108.9
108.4
107.9
107.3


capacity ratio
to R410A)

























TABLE 64







Ex.
Comp. Ex.
Ex.
Ex.
Ex.
Ex.
Ex.
Ex.


Item
Unit
97
83
98
99
100
101
102
103
























HFO-1132(E)
Mass %
50.0
55.0
10.0
15.0
20.0
25.0
30.0
35.0


HFO-1123
Mass %
30.5
25.5
65.5
60.5
55.5
50.5
45.5
40.5


R1234yf
Mass %
5.0
5.0
10.0
10.0
10.0
10.0
10.0
10.0


R32
Mass %
14.5
14.5
14.5
14.5
14.5
14.5
14.5
14.5


GWP

99
99
99
99
99
99
99
99


COP ratio
% (relative
96.2
96.6
94.2
94.4
94.6
94.9
95.2
95.5



to R410A)










Refrigerating
% (relative
106.6
106.0
107.5
107.3
107.0
106.6
106.1
105.6


capacity ratio
to R410A)

























TABLE 65







Ex.
Ex.
Ex.
Comp. Ex.
Ex.
Ex.
Ex.
Ex.


Item
Unit
104
105
106
84
107
108
109
110
























HFO-1132(E)
Mass %
40.0
45.0
50.0
55.0
10.0
15.0
20.0
25.0


HFO-1123
Mass %
35.5
30.5
25.5
20.5
60.5
55.5
50.5
45.5


R1234yf
Mass %
10.0
10.0
10.0
10.0
15.0
15.0
15.0
15.0


R32
Mass %
14.5
14.5
14.5
14.5
14.5
14.5
14.5
14.5


GWP

99
99
99
99
99
99
99
99


COP ratio
% (relative
95.9
96.3
96.7
97.1
94.6
94.8
95.1
95.4



to R410A)










Refrigerating
% (relative
105.1
104.5
103.8
103.1
104.7
104.5
104.1
103.7


capacity ratio
to R410A)

























TABLE 66







Ex.
Ex.
Ex.
Ex.
Ex.
Comp. Ex.
Ex.
Ex.


Item
Unit
111
112
113
114
115
85
116
117
























HFO-1132(E)
Mass %
30.0
35.0
40.0
45.0
50.0
55.0
10.0
15.0


HFO-1123
Mass %
40.5
35.5
30.5
25.5
20.5
15.5
55.5
50.5


R1234yf
Mass %
15.0
15.0
15.0
15.0
15.0
15.0
20.0
20.0


R32
Mass %
14.5
14.5
14.5
14.5
14.5
14.5
14.5
14.5


GWP

99
99
99
99
99
99
99
99


COP ratio
% (relative
95.7
96.0
96.4
96.8
97.2
97.6
95.1
95.3



to R410A)










Refrigerating
% (relative
103.3
102.8
102.2
101.6
101.0
100.3
101.8
101.6


capacity ratio
to R410A)

























TABLE 67







Ex.
Ex.
Ex.
Ex.
Ex.
Ex.
Ex.
Comp. Ex.


Item
Unit
118
119
120
121
122
123
124
86
























HFO-1132(E)
Mass %
20.0
25.0
30.0
35.0
40.0
45.0
50.0
55.0


HFO-1123
Mass %
45.5
40.5
35.5
30.5
25.5
20.5
15.5
10.5


R1234yf
Mass %
20.0
20.0
20.0
20.0
20.0
20.0
20.0
20.0


R32
Mass %
14.5
14.5
14.5
14.5
14.5
14.5
14.5
14.5


GWP

99
99
99
99
99
99
99
99


COP ratio
% (relative
95.6
95.9
96.2
96.5
96.9
97.3
97.7
98.2



to R410A)










Refrigerating
% (relative
101.2
100.8
100.4
99.9
99.3
98.7
98.0
97.3


capacity ratio
to R410A)

























TABLE 68







Ex.
Ex.
Ex.
Ex.
Ex.
Ex.
Ex.
Ex.


Item
Unit
125
126
127
128
129
130
131
132
























HFO-1132 (E)
Mass %
10.0
15.0
20.0
25.0
30.0
35.0
40.0
45.0


HFO-1123
Mass %
50.5
45.5
40.5
35.5
30.5
25.5
20.5
15.5


R1234yf
Mass %
25.0
25.0
25.0
25.0
25.0
25.0
25.0
25.0


R32
Mass %
14.5
14.5
14.5
14.5
14.5
14.5
14.5
14.5


GWP

99
99
99
99
99
99
99
99


COP ratio
% (relative to
95.6
95.9
96.1
96.4
96.7
97.1
97.5
97.9



R410A)










Refrigerating capacity
% (relative to
98.9
98.6
98.3
97.9
97.4
96.9
96.3
95.7


ratio
R410A)

























TABLE 69







Ex.
Comp. Ex.
Ex.
Ex.
Ex.
Ex.
Ex.
Ex.


Item
Unit
133
87
134
135
136
137
138
139
























HFO-1132 (E)
Mass %
50.0
55.0
10.0
15.0
20.0
25.0
30.0
35.0


HFO-1123
Mass %
10.5
5.5
45.5
40.5
35.5
30.5
25.5
20.5


R1234yf
Mass %
25.0
25.0
30.0
30.0
30.0
30.0
30.0
30.0


R32
Mass %
14.5
14.5
14.5
14.5
14.5
14.5
14.5
14.5


GWP

99
99
100
100
100
100
100
100


COP ratio
% (relative to
98.3
98.7
96.2
96.4
96.7
97.0
97.3
97.7



R410A)










Refrigerating capacity
% (relative to
95.0
94.3
95.8
95.6
95.2
94.8
94.4
93.8


ratio
R410A)

























TABLE 70







Ex.
Ex.
Ex.
Ex.
Ex.
Ex.
Ex.
Ex.


Item
Unit
140
141
142
143
144
145
146
147
























HFO-1132 (E)
Mass %
40.0
45.0
50.0
10.0
15.0
20.0
25.0
30.0


HFO-1123
Mass %
15.5
10.5
5.5
40.5
35.5
30.5
25.5
20.5


R1234yf
Mass %
30.0
30.0
30.0
35.0
35.0
35.0
35.0
35.0


R32
Mass %
14.5
14.5
14.5
14.5
14.5
14.5
14.5
14.5


GWP

100
100
100
100
100
100
100
100


COP ratio
% (relative to
98.1
98.5
98.9
96.8
97.0
97.3
97.6
97.9



R410A)










Refrigerating capacity
% (relative to
93.3
92.6
92.0
92.8
92.5
92.2
91.8
91.3


ratio
R410A)

























TABLE 71







Ex.
Ex.
Ex.
Ex.
Ex.
Ex.
Ex.
Ex.


Item
Unit
148
149
150
151
152
153
154
155
























HFO-1132 (E)
Mass %
35.0
40.0
45.0
10.0
15.0
20.0
25.0
30.0


HFO-1123
Mass %
15.5
10.5
5.5
35.5
30.5
25.5
20.5
15.5


R1234yf
Mass %
35.0
35.0
35.0
40.0
40.0
40.0
40.0
40.0


R32
Mass %
14.5
14.5
14.5
14.5
14.5
14.5
14.5
14.5


GWP

100
100
100
100
100
100
100
100


COP ratio
% (relative to
98.3
98.7
99.1
97.4
97.7
98.0
98.3
98.6



R410A)










Refrigerating capacity
% (relative to
90.8
90.2
89.6
89.6
89.4
89.0
88.6
88.2


ratio
R410A)

























TABLE 72







Ex.
Ex.
Ex.
Ex.
Ex.
Comp. Ex.
Comp. Ex.
Comp. Ex.


Item
Unit
156
157
158
159
160
88
89
90
























HFO-1132 (E)
Mass %
35.0
40.0
10.0
15.0
20.0
25.0
30.0
35.0


HFO-1123
Mass %
10.5
5.5
30.5
25.5
20.5
15.5
10.5
5.5


R1234yf
Mass %
40.0
40.0
45.0
45.0
45.0
45.0
45.0
45.0


R32
Mass %
14.5
14.5
14.5
14.5
14.5
14.5
14.5
14.5


GWP

100
100
100
100
100
100
100
100


COP ratio
% (relative to
98.9
99.3
98.1
98.4
98.7
98.9
99.3
99.6



R410A)










Refrigerating
% (relative to
87.6
87.1
86.5
86.2
85.9
85.5
85.0
84.5


capacity ratio
R410A)






















TABLE 73







Comp. Ex.
Comp. Ex.
Comp. Ex.
Comp. Ex.
Comp. Ex.


Item
Unit
91
92
93
94
95





















HFO-1132 (E)
Mass %
10.0
15.0
20.0
25.0
30.0


HFO-1123
Mass %
25.5
20.5
15.5
10.5
5.5


R1234yf
Mass %
50.0
50.0
50.0
50.0
50.0


R32
Mass %
14.5
14.5
14.5
14.5
14.5


GWP

100
100
100
100
100


COP ratio
% (relative to
98.9
99.1
99.4
99.7
100.0



R410A)







Refrigerating capacity
% (relative to
83.3
83.0
82.7
82.2
81.8


ratio
R410A)

























TABLE 74







Ex.
Ex.
Ex.
Ex.
Ex.
Ex.
Ex.
Ex.


Item
Unit
161
162
163
164
165
166
167
168
























HFO-1132 (E)
Mass %
10.0
15.0
20.0
25.0
30.0
35.0
40.0
45.0


HFO-1123
Mass %
63.1
58.1
53.1
48.1
43.1
38.1
33.1
28.1


R1234yf
Mass %
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0


R32
Mass %
21.9
21.9
21.9
21.9
21.9
21.9
21.9
21.9


GWP

149
149
149
149
149
149
149
149


COP ratio
% (relative to
94.8
95.0
95.2
95.4
95.7
95.9
96.2
96.6



R410A)










Refrigerating capacity
% (relative to
111.5
111.2
110.9
110.5
110.0
109.5
108.9
108.3


ratio
R410A)

























TABLE 75







Comp. Ex.
Ex.
Ex.
Ex.
Ex.
Ex.
Ex.
Ex.


Item
Unit
96
169
170
171
172
173
174
175
























HFO-1132 (E)
Mass %
50.0
10.0
15.0
20.0
25.0
30.0
35.0
40.0


HFO-1123
Mass %
23.1
58.1
53.1
48.1
43.1
38.1
33.1
28.1


R1234yf
Mass %
5.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0


R32
Mass %
21.9
21.9
21.9
21.9
21.9
21.9
21.9
21.9


GWP

149
149
149
149
149
149
149
149


COP ratio
% (relative to
96.9
95.3
95.4
95.6
95.8
96.1
96.4
96.7



R410A)










Refrigerating capacity
% (relative to
107.7
108.7
108.5
108.1
107.7
107.2
106.7
106.1


ratio
R410A)

























TABLE 76







Ex.
Comp. Ex.
Ex.
Ex.
Ex.
Ex.
Ex.
Ex.


Item
Unit
176
97
177
178
179
180
181
182
























HFO-1132 (E)
Mass %
45.0
50.0
10.0
15.0
20.0
25.0
30.0
35.0


HFO-1123
Mass %
23.1
18.1
53.1
48.1
43.1
38.1
33.1
28.1


R1234yf
Mass %
10.0
10.0
15.0
15.0
15.0
15.0
15.0
15.0


R32
Mass %
21.9
21.9
21.9
21.9
21.9
21.9
21.9
21.9


GWP

149
149
149
149
149
149
149
149


COP ratio
% (relative to
97.0
97.4
95.7
95.9
96.1
96.3
96.6
96.9



R410A)










Refrigerating capacity
% (relative to
105.5
104.9
105.9
105.6
105.3
104.8
104.4
103.8


ratio
R410A)

























TABLE 77







Ex.
Ex.
Comp. Ex.
Ex.
Ex.
Ex.
Ex.
Ex.


Item
Unit
183
184
98
185
186
187
188
189
























HFO-1132 (E)
Mass %
40.0
45.0
50.0
10.0
15.0
20.0
25.0
30.0


HFO-1123
Mass %
23.1
18.1
13.1
48.1
43.1
38.1
33.1
28.1


R1234yf
Mass %
15.0
15.0
15.0
20.0
20.0
20.0
20.0
20.0


R32
Mass %
21.9
21.9
21.9
21.9
21.9
21.9
21.9
21.9


GWP

149
149
149
149
149
149
149
149


COP ratio
% (relative to
97.2
97.5
97.9
96.1
96.3
96.5
96.8
97.1



R410A)










Refrigerating capacity
% (relative to
103.3
102.6
102.0
103.0
102.7
102.3
101.9
101.4


ratio
R410A)

























TABLE 78







Ex.
Ex.
Ex.
Comp. Ex.
Ex.
Ex.
Ex.
Ex.


Item
Unit
190
191
192
99
193
194
195
196
























HFO-1132 (E)
Mass %
35.0
40.0
45.0
50.0
10.0
15.0
20.0
25.0


HFO-1123
Mass %
23.1
18.1
13.1
8.1
43.1
38.1
33.1
28.1


R1234yf
Mass %
20.0
20.0
20.0
20.0
25.0
25.0
25.0
25.0


R32
Mass %
21.9
21.9
21.9
21.9
21.9
21.9
21.9
21.9


GWP

149
149
149
149
149
149
149
149


COP ratio
% (relative to
97.4
97.7
98.0
98.4
96.6
96.8
97.0
97.3



R410A)










Refrigerating capacity
% (relative to
100.9
100.3
99.7
99.1
100.0
99.7
99.4
98.9


ratio
R410A)

























TABLE 79







Ex.
Ex.
Ex.
Ex.
Comp. Ex.
Ex.
Ex.
Ex.


Item
Unit
197
198
199
200
100
201
202
203
























HFO-1132 (E)
Mass %
30.0
35.0
40.0
45.0
50.0
10.0
15.0
20.0


HFO-1123
Mass %
23.1
18.1
13.1
8.1
3.1
38.1
33.1
28.1


R1234yf
Mass %
25.0
25.0
25.0
25.0
25.0
30.0
30.0
30.0


R32
Mass %
21.9
21.9
21.9
21.9
21.9
21.9
21.9
21.9


GWP

149
149
149
149
149
150
150
150


COP ratio
% (relative to
97.6
97.9
98.2
98.5
98.9
97.1
97.3
97.6



R410A)










Refrigerating capacity
% (relative to
98.5
97.9
97.4
96.8
96.1
97.0
96.7
96.3


ratio
R410A)

























TABLE 80







Ex.
Ex.
Ex.
Ex.
Ex.
Ex.
Ex.
Ex.


Item
Unit
204
205
206
207
208
209
210
211
























HFO-1132 (E)
Mass %
25.0
30.0
35.0
40.0
45.0
10.0
15.0
20.0


HFO-1123
Mass %
23.1
18.1
13.1
8.1
3.1
33.1
28.1
23.1


R1234yf
Mass %
30.0
30.0
30.0
30.0
30.0
35.0
35.0
35.0


R32
Mass %
21.9
21.9
21.9
21.9
21.9
21.9
21.9
21.9


GWP

150
150
150
150
150
150
150
150


COP ratio
% (relative to
97.8
98.1
98.4
98.7
99.1
97.7
97.9
98.1



R410A)










Refrigerating capacity
% (relative to
95.9
95.4
94.9
94.4
93.8
93.9
93.6
93.3


ratio
R410A)

























TABLE 81







Ex.
Ex.
Ex.
Ex.
Ex.
Ex.
Ex.
Ex.


Item
Unit
212
213
214
215
216
217
218
219
























HFO-1132 (E)
Mass %
25.0
30.0
35.0
40.0
10.0
15.0
20.0
25.0


HFO-1123
Mass %
18.1
13.1
8.1
3.1
28.1
23.1
18.1
13.1


R1234yf
Mass %
35.0
35.0
35.0
35.0
40.0
40.0
40.0
40.0


R32
Mass %
21.9
21.9
21.9
21.9
21.9
21.9
21.9
21.9


GWP

150
150
150
150
150
150
150
150


COP ratio
% (relative to
98.4
98.7
99.0
99.3
98.3
98.5
98.7
99.0



R410A)










Refrigerating capacity
% (relative to
92.9
92.4
91.9
91.3
90.8
90.5
90.2
89.7


ratio
R410A)

























TABLE 82







Ex.
Ex.
Ex.
Ex.
Ex.
Ex.
Ex.
Comp. Ex.


Item
Unit
220
221
222
223
224
225
226
101
























HFO-1132 (E)
Mass %
30.0
35.0
10.0
15.0
20.0
25.0
30.0
10.0


HFO-1123
Mass %
8.1
3.1
23.1
18.1
13.1
8.1
3.1
18.1


R1234yf
Mass %
40.0
40.0
45.0
45.0
45.0
45.0
45.0
50.0


R32
Mass %
21.9
21.9
21.9
21.9
21.9
21.9
21.9
21.9


GWP

150
150
150
150
150
150
150
150


COP ratio
% (relative to
99.3
99.6
98.9
99.1
99.3
99.6
99.9
99.6



R410A)










Refrigerating capacity
% (relative to
89.3
88.8
87.6
87.3
87.0
86.6
86.2
84.4


ratio
R410A)




















TABLE 83







Comp.
Comp.
Comp.


Item
Unit
Ex. 102
Ex. 103
Ex. 104



















HFO-1132(E)
Mass %
15.0
20.0
25.0


HFO-1123
Mass %
13.1
8.1
3.1


R1234yf
Mass %
50.0
50.0
50.0


R32
Mass %
21.9
21.9
21.9


GWP

150
150
150


COP ratio
% (relative to R410A)
99.8
100.0
100.2


Refrigerating
% (relative to R410A)
84.1
83.8
83.4


capacity ratio





























TABLE 84







Ex.
Ex.
Ex.
Ex.
Ex.
Ex.
Ex.
Comp. Ex.


Item
Unit
227
228
229
230
231
232
233
105
























HF-1132(E)
Mass %
10.0
15.0
20.0
25.0
30.0
35.0
40.0
45.0


HFO-1123
Mass %
55.7
50.7
45.7
40.7
35.7
30.7
25.7
20.7


R1234yf
Mass %
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0


R32
Mass %
29.3
29.3
29.3
29.3
29.3
29.3
29.3
29.3


GWP

199
199
199
199
199
199
199
199


COP ratio
% (relative to
95.9
96.0
96.2
96.3
96.6
96.8
97.1
97.3



R410A)










Refrigerating capacity
% (relative to
112.2
111.9
111.6
111.2
110.7
110.2
109.6
109.0


ratio
R410A)

























TABLE 85







Ex.
Ex.
Ex.
Ex.
Ex.
Ex.
Ex.
Comp. Ex.


Item
Unit
234
235
236
237
238
239
240
106
























HFO-1132(E)
Mass %
10.0
15.0
20.0
25.0
30.0
35.0
40.0
45.0


HFO-1123
Mass %
50.7
45.7
40.7
35.7
30.7
25.7
20.7
15.7


R1234yf
Mass %
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0


R32
Mass %
29.3
29.3
29.3
29.3
29.3
29.3
29.3
29.3


GWP

199
199
199
199
199
199
199
199


COP ratio
% (relative to
96.3
96.4
96.6
96.8
97.0
97.2
97.5
97.8



R410A)










Refrigerating capacity
% (relative to
109.4
109.2
108.8
108.4
107.9
107.4
106.8
106.2


ratio
R410A)

























TABLE 86







Ex.
Ex.
Ex.
Ex.
Ex.
Ex.
Ex.
Comp. Ex.


Item
Unit
241
242
243
244
245
246
247
107
























HFO-1132(E)
Mass %
10.0
15.0
20.0
25.0
30.0
35.0
40.0
45.0


HFO-1123
Mass %
45.7
40.7
35.7
30.7
25.7
20.7
15.7
10.7


R1234yf
Mass %
15.0
15.0
15.0
15.0
15.0
15.0
15.0
15.0


R32
Mass %
29.3
29.3
29.3
29.3
29.3
29.3
29.3
29.3


GWP

199
199
199
199
199
199
199
199


COP ratio
% (relative to
96.7
96.8
97.0
97.2
97.4
97.7
97.9
98.2



R410A)










Refrigerating capacity
% (relative to
106.6
106.3
106.0
105.5
105.1
104.5
104.0
103.4


ratio
R410A)

























TABLE 87







Ex.
Ex.
Ex.
Ex.
Ex.
Ex.
Ex.
Comp. Ex.


Item
Unit
248
249
250
251
252
253
254
108
























HFO-1132(E)
Mass %
10.0
15.0
20.0
25.0
30.0
35.0
40.0
45.0


HFO-1123
Mass %
40.7
35.7
30.7
25.7
20.7
15.7
10.7
5.7


R1234yf
Mass %
20.0
20.0
20.0
20.0
20.0
20.0
20.0
20.0


R32
Mass %
29.3
29.3
29.3
29.3
29.3
29.3
29.3
29.3


GWP

199
199
199
199
199
199
199
199


COP ratio
% (relative to
97.1
97.3
97.5
97.7
97.9
98.1
98.4
98.7



R410A)










Refrigerating capacity
% (relative to
103.7
103.4
103.0
102.6
102.2
101.6
101.1
100.5


ratio
R410A)

























TABLE 88







Ex.
Ex.
Ex.
Ex.
Ex.
Ex.
Ex.
Ex.


Item
Unit
255
256
257
258
259
260
261
262
























HFO-1132(E)
Mass %
10.0
15.0
20.0
25.0
30.0
35.0
40.0
10.0


HFO-1123
Mass %
35.7
30.7
25.7
20.7
15.7
10.7
5.7
30.7


R1234yf
Mass %
25.0
25.0
25.0
25.0
25.0
25.0
25.0
30.0


R32
Mass %
29.3
29.3
29.3
29.3
29.3
29.3
29.3
29.3


GWP

199
199
199
199
199
199
199
199


COP ratio
% (relative to
97.6
97.7
97.9
98.1
98.4
98.6
98.9
98.1



R410A)










Refrigerating capacity
% (relative to
100.7
100.4
100.1
99.7
99.2
98.7
98.2
97.7


ratio
R410A)

























TABLE 89







Ex.
Ex.
Ex.
Ex.
Ex.
Ex.
Ex.
Ex.


Item
Unit
263
264
265
266
267
268
269
270
























HFO-1132(E)
Mass %
15.0
20.0
25.0
30.0
35.0
10.0
15.0
20.0


HFO-1123
Mass %
25.7
20.7
15.7
10.7
5.7
25.7
20.7
15.7


R1234yf
Mass %
30.0
30.0
30.0
30.0
30.0
35.0
35.0
35.0


R32
Mass %
29.3
29.3
29.3
29.3
29.3
29.3
29.3
29.3


GWP

199
199
199
199
199
200
200
200


COP ratio
% (relative to
98.2
98.4
98.6
98.9
99.1
98.6
98.7
98.9



R410A)










Refrigerating capacity
% (relative to
97.4
97.1
96.7
96.2
95.7
94.7
94.4
94.0


ratio
R410A)

























TABLE 90







Ex.
Ex.
Ex.
Ex.
Ex.
Ex.
Ex.
Ex.


Item
Unit
271
272
273
274
275
276
277
278
























HFO-1132(E)
Mass %
25.0
30.0
10.0
15.0
20.0
25.0
10.0
15.0


HFO-1123
Mass %
10.7
5.7
20.7
15.7
10.7
5.7
15.7
10.7


R1234yf
Mass %
35.0
35.0
40.0
40.0
40.0
40.0
45.0
45.0


R32
Mass %
29.3
29.3
29.3
29.3
29.3
29.3
29.3
29.3


GWP

200
200
200
200
200
200
200
200



% (relative to










COP ratio
R410A)
99.2
99.4
99.1
99.3
99.5
99.7
99.7
99.8


Refrigerating capacity
% (relative to










ratio
R410A)
93.6
93.2
91.5
91.3
90.9
90.6
88.4
88.1





















TABLE 91









Comp.
Comp.


Item
Unit
Ex. 279
Ex. 280
Ex. 109
Ex. 110




















HFO-1132(E)
Mass %
20.0
10.0
15.0
10.0


HFO-1123
Mass %
5.7
10.7
5.7
5.7


R1234yf
Mass %
45.0
50.0
50.0
55.0


R32
Mass %
29.3
29.3
29.3
29.3


GWP

200
200
200
200


COP ratio
% (relative
100.0
100.3
100.4
100.9



to R410A)






Refrigerating
% (relative
87.8
85.2
85.0
82.0


capacity ratio
to R410A)





























TABLE 92







Ex.
Ex.
Ex.
Ex.
Ex.
Comp. Ex.
Ex.
Ex.


Item
Unit
281
282
283
284
285
111
286
287
























HFO-1132(E)
Mass %
10.0
15.0
20.0
25.0
30.0
35.0
10.0
15.0


HFO-1123
Mass %
40.9
35.9
30.9
25.9
20.9
15.9
35.9
30.9


R1234yf
Mass %
5.0
5.0
5.0
5.0
5.0
5.0
10.0
10.0


R32
Mass %
44.1
44.1
44.1
44.1
44.1
44.1
44.1
44.1


GWP

298
298
298
298
298
298
299
299



% (relative to
97.8
97.9
97.9
98.1
98.2
98.4
98.2
98.2


COP ratio
R410A)










Refrigerating capacity
% (relative to
112.5
112.3
111.9
111.6
111.2
110.7
109.8
109.5


ratio
R410A)

























TABLE 93







Ex.
Ex.
Ex.
Comp. Ex.
Ex.
Ex.
Ex.
Ex.


Item
Unit
288
289
290
112
291
292
293
294







HFO-1132 (E)
Mass %
20.0
25.0
30.0
35.0
10.0
15.0
20.0
25.0


HFO-1123
Mass %
25.9
20.9
15.9
10.9
30.9
25.9
20.9
15.9


R1234yf
Mass %
10.0
10.0
10.0
10.0
15.0
15.0
15.0
15.0


R32
Mass %
44.1
44.1
44.1
44.1
44.1
44.1
44.1
44.1


GWP

299
299
299
299
299
299
299
299


COP ratio
% (relative to
98.3
98.5
98.6
98.8
98.6
98.6
98.7
98.9



R410A)










Refrigerating capacity
% (relative to
109.2
108.8
108.4
108.0
107.0
106.7
106.4
106.0


ratio
R410A)

























TABLE 94







Ex.
Comp. Ex.
Ex.
Ex.
Ex.
Ex.
Ex.
Ex.


Item
Unit
295
113
296
297
298
299
300
301
























HFO-1132(E)
Mass %
30.0
35.0
10.0
15.0
20.0
25.0
30.0
10.0


HFO-1123
Mass %
10.9
5.9
25.9
20.9
15.9
10.9
5.9
20.9


R1234yf
Mass %
15.0
15.0
20.0
20.0
20.0
20.0
20.0
25.0


R32
Mass %
44.1
44.1
44.1
44.1
44.1
44.1
44.1
44.1


GWP

299
299
299
299
299
299
299
299


COP ratio
% (relative to
99.0
99.2
99.0
99.0
99.2
99.3
99.4
99.4



R410A)










Refrigerating capacity
% (relative to
105.6
105.2
104.1
103.9
103.6
103.2
102.8
101.2


ratio
R410A)

























TABLE 95







Ex.
Ex.
Ex.
Ex.
Ex.
Ex.
Ex.
Ex.


Item
Unit
302
303
304
305
306
307
308
309







HFO-1132(E)
Mass %
15.0
20.0
25.0
10.0
15.0
20.0
10.0
15.0


HFO-1123
Mass %
15.9
10.9
5.9
15.9
10.9
5.9
10.9
5.9


R1234yf
Mass %
25.0
25.0
25.0
30.0
30.0
30.0
35.0
35.0


R32
Mass %
44.1
44.1
44.1
44.1
44.1
44.1
44.1
44.1


GWP

299
299
299
299
299
299
299
299


COP ratio
% (relative to
99.5
99.6
99.7
99.8
99.9
100.0
100.3
100.4



R410A)










Refrigerating capacity
% (relative to
101.0
100.7
100.3
98.3
98.0
97.8
95.3
95.1


ratio
R410A)




















TABLE 96







Item
Unit
Ex. 400




















HFO-1132(E)
Mass %
10.0



HFO-1123
Mass %
5.9



R1234yf
Mass %
40.0



R32
Mass %
44.1



GWP

299



COP ratio
% (relative to R410A)
100.7



Refrigerating capacity ratio
% (relative to R410A)
92.3










The above results indicate that the refrigerating capacity ratio relative to R410A is 85% or more in the following cases:


When the mass % of HFO-1132(E), HFO-1123, R1234yf, and R32 based on their sum is respectively represented by x, y, z, and a, in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R1234yf is (100−a) mass %, a straight line connecting a point (0.0, 100.0−a, 0.0) and a point (0.0, 0.0, 100.0−a) is the base, and the point (0.0, 100.0−a, 0.0) is on the left side, if 0<a≤11.1, coordinates (x,y,z) in the ternary composition diagram are on, or on the left side of, a straight line AB that connects point A (0.0134a2−1.9681a+68.6, 0.0, −0.0134a2+0.9681a+31.4) and point B (0.0, 0.0144a2−1.6377a+58.7, −0.0144a2+0.6377a+41.3);


if 11.1<a≤18.2, coordinates (x,y,z) in the ternary composition diagram are on, or on the left side of, a straight line AB that connects point A (0.0112a2−1.9337a+68.484, 0.0, −0.0112a2+0.9337a+31.516) and point B (0.0, 0.0075a2−1.5156a+58.199, −0.0075a2+0.5156a+41.801);


if 18.2a<a≤26.7, coordinates (x,y,z) in the ternary composition diagram are on, or on the left side of, a straight line AB that connects point A (0.0107a2−1.9142a+68.305, 0.0, −0.0107a2+0.9142a+31.695) and point B (0.0, 0.009a2−1.6045a+59.318, −0.009a2+0.6045a+40.682);


if 26.7<a≤36.7, coordinates (x,y,z) in the ternary composition diagram are on, or on the left side of, a straight line AB that connects point A (0.0103a2−1.9225a+68.793, 0.0, −0.0103a2+0.9225a+31.207) and point B (0.0, 0.0046a2−1.41a+57.286, −0.0046a2+0.41a+42.714); and


if 36.7<a≤46.7, coordinates (x,y,z) in the ternary composition diagram are on, or on the left side of, a straight line AB that connects point A (0.0085a2−1.8102a+67.1, 0.0, −0.0085a2+0.8102a+32.9) and point B (0.0, 0.0012a2−1.1659a+52.95, −0.0012a2+0.1659a+47.05).


Actual points having a refrigerating capacity ratio of 85% or more form a curved line that connects point A and point B in FIG. 3, and that extends toward the 1234yf side. Accordingly, when coordinates are on, or on the left side of, the straight line AB, the refrigerating capacity ratio relative to R410A is 85% or more.


Similarly, it was also found that in the ternary composition diagram, if 0<a≤11.1, when coordinates (x,y,z) are on, or on the left side of, a straight line D′C that connects point D′ (0.0, 0.0224a2+0.968a+75.4, −0.0224a2−1.968a+24.6) and point C (−0.2304a2−0.4062a+32.9, 0.2304a2−0.5938a+67.1, 0.0); or if 11.1<a≤46.7, when coordinates are in the entire region, the COP ratio relative to that of R410A is 92.5% or more.


In FIG. 3, the COP ratio of 92.5% or more forms a curved line CD. In FIG. 3, an approximate line formed by connecting three points: point C (32.9, 67.1, 0.0) and points (26.6, 68.4, 5) (19.5, 70.5, 10) where the COP ratio is 92.5% when the concentration of R1234yf is 5 mass % and 10 mass was obtained, and a straight line that connects point C and point D′ (0, 75.4, 24.6), which is the intersection of the approximate line and a point where the concentration of HFO-1132(E) is 0.0 mass % was defined as a line segment D′C. In FIG. 4, point D′(0, 83.4, 9.5) was similarly obtained from an approximate curve formed by connecting point C (18.4, 74.5, 0) and points (13.9, 76.5, 2.5) (8.7, 79.2, 5) where the COP ratio is 92.5%, and a straight line that connects point C and point D′ was defined as the straight line D′C.


The composition of each mixture was defined as WCF. A leak simulation was performed using NIST Standard Reference Database REFLEAK Version 4.0 under the conditions of Equipment, Storage, Shipping, Leak, and Recharge according to the ASHRAE Standard 34-2013. The most flammable fraction was defined as WCFF.


For the flammability, the burning velocity was measured according to the ANSI/ASHRAE Standard 34-2013. Both WCF and WCFF having a burning velocity of 10 cm/s or less were determined to be classified as “Class 2L (lower flammability).”


A burning velocity test was performed using the apparatus shown in FIG. 1 in the following manner. First, the mixed refrigerants used had a purity of 99.5% or more, and were degassed by repeating a cycle of freezing, pumping, and thawing until no traces of air were observed on the vacuum gauge. The burning velocity was measured by the closed method. The initial temperature was ambient temperature. Ignition was performed by generating an electric spark between the electrodes in the center of a sample cell. The duration of the discharge was 1.0 to 9.9 ms, and the ignition energy was typically about 0.1 to 1.0 J. The spread of the flame was visualized using schlieren photographs. A cylindrical container (inner diameter: 155 mm, length: 198 mm) equipped with two light transmission acrylic windows was used as the sample cell, and a xenon lamp was used as the light source. Schlieren images of the flame were recorded by a high-speed digital video camera at a frame rate of 600 fps and stored on a PC.


The results are shown in Tables 97 to 104.

















TABLE 97










Comp. Ex.
Comp. Ex.
Comp. Ex.
Comp. Ex.
Comp. Ex.
Comp. Ex.













Item
6
13
19
24
29
34


















WCF
HFO-1132(E)
Mass
72.0
60.9
55.8
52.1
48.6
45.4




%









HFO-1123
Mass
28.0
32.0
33.1
33.4
33.2
32.7




%









R1234yf
Mass
0.0
0.0
0.0
0
0
0




%









R32
Mass
0.0
7.1
11.1
14.5
18.2
21.9




%




















Burning velocity
cm/s
10
10
10
10
10
10


(WCF)























TABLE 98










Comp. Ex.
Comp. Ex.
Comp. Ex.
Comp. Ex.
Comp. Ex.












Item
39
45
51
57
62

















WCF
HFO-1132(E)
Mass
41.8
40
35.7
32
30.4




%








HFO-1123
Mass
31.5
30.7
23.6
23.9
218




%








R1234yf
Mass
0
0
0
0
0




%








R32
Mass
26.7
29.3
36.7
44.1
47.8




%


















Burning velocity
cm/s
10
10
10
10
10


(WCF)
























TABLE 99










Comp. Ex.
Comp. Ex.
Comp. Ex.
Comp. Ex.
Comp. Ex.
Comp. Ex.













Item
7
14
20
25
30
35


















WCF
HFO-1132(E)
Mass
72.0
60.9
55.8
52.1
48.6
45.4




%









HFO-1123
Mass
0.0
0.0
0.0
0
0
0




%









R1234yf
Mass
28.0
32.0
33.1
33.4
33.2
32.7




%









R32
Mass
0.0
7.1
11.1
14.5
18.2
21.9




%




















Burning velocity
cm/s
10
10
10
10
10
10


(WCF)























TABLE 100










Comp. Ex.
Comp. Ex.
Comp. Ex.
Comp. Ex.
Comp. Ex.












Item
40
46
52
58
63

















WCF
HFO-1132(E)
Mass
41.8
40
35.7
32
30.4




%








HFO-1123
Mass
0
0
0
0
0




%








R1234yf
Mass
31.5
30.7
23.6
23.9
21.8




%








R32
Mass
26.7
29.3
36.7
44.1
47.8




%


















Burning velocity
cm/s
10
10
10
10
10


(WCF)
























TABLE 101










Comp. Ex.
Comp. Ex.
Comp. Ex.
Comp. Ex.
Comp. Ex.
Comp. Ex.













Item
8
15
21
26
31
36


















WCF
HFO-1132 (E)
Mass %
47.1
40.5
37.0
34.3
32.0
30.3



HFO-1123
Mass %
52.9
52.4
51.9
51.2
49.8
47.8



R1234yf
Mass %
0.0
0.0
0.0
0.0
0.0
0.0



R32
Mass %
0.0
7.1
11.1
14.5
18.2
21.9













Leak condition that results
Storage/
Storage/
Storage/
Storage/
Storage/
Storage/


in WCFF
Shipping
Shipping
Shipping
Shipping
Shipping
Shipping



−40° C.,
−40° C.,
−40° C.,
−40° C.,
−40° C.,
−40° C.,



92%
92%
92%
92%
92%
92%



release,
release,
release,
release,
release,
release,



liquid phase
liquid phase
liquid phase
liquid phase
liquid phase
liquid phase



side
side
side
side
side
side















WCFF
HFO-1132 (E)
Mass %
72.0
62.4
56.2
50.6
45.1
40.0



HFO-1123
Mass %
28.0
31.6
33.0
33.4
32.5
30.5



R1234yf
Mass %
0.0
0.0
0.0
20.4
0.0
0.0



R32
Mass %
0.0
50.9
10.8
16.0
22.4
29.5














Burning velocity
cm/s
8 or less
8 or less
8 or less
8 or less
8 or less
8 or less


(WCF)









Burning velocity
cm/s
10
10
10
10
10
10


(WCFF)






























TABLE 102










Comp. Ex.
Comp. Ex.
Comp. Ex.
Comp. Ex.
Comp. Ex.












Item
41
47
53
59
64

















WCF
HFO-1132 (E)
Mass %
29.1
28.8
29.3
29.4
28.9



HFO-1123
Mass %
44.2
41.9
34.0
26.5
23.3



R1234yf
Mass %
0.0
0.0
0.0
0.0
0.0



R32
Mass %
26.7
29.3
36.7
44.1
47.8












Leak condition that results in
Storage/
Storage/
Storage/
Storage/
Storage/


WCFF
Shipping
Shipping
Shipping
Shipping
Shipping



−40° C.,
−40° C.,
−40° C.,
−40° C.,
−40° C.,



92%
92%
92%
90%
86%



release,
release,
release,
release,
release,



liquid phase
liquid phase
liquid phase
gas phase
gas phase



side
side
side
side
side














WCFF
HFO-1132 (E)
Mass %
34.6
32.2
27.7
28.3
27.5



HFO-1123
Mass %
26.5
23.9
17.5
18.2
16.7



R1234yf
Mass %
0.0
0.0
0.0
0.0
0.0



R32
Mass %
38.9
43.9
54.8
53.5
55.8













Burning velocity
cm/s
8 or less
8 or less
8.3
9.3
9.6


(WCF)








Burning velocity
cm/s
10
10
10
10
10


(WCFF)




























TABLE 103






Comp. Ex.
Comp. Ex.
Comp. Ex.
Comp. Ex.
Comp. Ex.
Comp. Ex.


Item
9
16
22
27
32
37























WCF
HFO-1132 (E)
Mass %
61.7
47.0
41.0
36.5
32.5
28.8



HFO-1123
Mass %
5.9
7.2
6.5
5.6
4.0
2.4



R1234yf
Mass %
32.4
38.7
41.4
43.4
45.3
46.9



R32
Mass %
0.0
7.1
11.1
14.5
18.2
21.9













Leak condition that results in
Storage/
Storage/
Storage/
Storage/
Storage/
Storage/


WCFF
Shipping
Shipping
Shipping
Shipping
Shipping
Shipping



−40° C.,
−40° C.,
−40° C.,
−40° C.,
−40° C.,
−40° C.,



0%
0%
0%
92%
0%
0%



release,
release,
release,
release,
release,
release,



gas phase
gas phase
gas phase
liquid phase
gas phase
gas phase



side
side
side
side
side
side















WCFF
HFO-1132 (E)
Mass %
72.0
56.2
50.4
46.0
42.4
39.1



HFO-1123
Mass %
10.5
12.6
11.4
10.1
7.4
4.4



R1234yf
Mass %
17.5
20.4
21.8
22.9
24.3
25.7



R32
Mass %
0.0
10.8
16.3
21.0
25.9
30.8














Burning velocity
cm/s
8 or less
8 or less
8 or less
8 or less
8 or less
8 or less


(WCF)









Burning velocity
cm/s
10
10
10
10
10
10


(WCFF)






























TABLE 104










Comp. Ex.
Comp. Ex.
Comp. Ex.
Comp. Ex.
Comp. Ex.












Item
42
48
54
60
65

















WCF
HFO-1132 (E)
Mass %
24.8
24.3
22.5
21.1
20.4



HFO-1123
Mass %
0.0
0.0
0.0
0.0
0.0



R1234yf
Mass %
48.5
46.4
40.8
34.8
31.8



R32
Mass %
26.7
29.3
36.7
44.1
47.8












Leak condition that results in
Storage/
Storage/
Storage/
Storage/
Storage/


WCFF
Shipping
Shipping
Shipping
Shipping
Shipping



−40° C.,
−40° C.,
−40° C.,
−40° C.,
−40° C.,



0%
0%
0%
0%
0%



release,
release,
release,
release,
release,



gas phase
gas phase
gas phase
gas phase
gas phase



side
side
side
side
side














WCFF
HFO-1132 (E)
Mass %
35.3
34.3
31.3
29.1
28.1



HFO-1123
Mass %
0.0
0.0
0.0
0.0
0.0



R1234yf
Mass %
27.4
26.2
23.1
19.8
18.2



R32
Mass %
37.3
39.6
45.6
51.1
53.7













Burning velocity
cm/s
8 or less
8 or less
8 or less
8 or less
8 or less


(WCF)








Burning velocity
cm/s
10
10
10
10
10


(WCFF)















The results in Tables 97 to 100 indicate that the refrigerant has a WCF lower flammability in the following cases:


When the mass % of HFO-1132(E), HFO-1123, R1234yf, and R32 based on their sum in the mixed refrigerant of HFO-1132(E), HFO-1123, R1234yf, and R32 is respectively represented by x, y, z, and a, coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R1234yf is (100−a) mass % and a straight line connecting a point (0.0, 100.0−a, 0.0) and a point (0.0, 0.0, 100.0−a) is the base, if 0<a≤11.1, coordinates (x,y,z) in the ternary composition diagram are on or below a straight line GI that connects point G (0.026a2−1.7478a+72.0, −0.026a2+0.7478a+28.0, 0.0) and point I (0.026a2−1.7478a+72.0, 0.0, −0.026a2+0.7478a+28.0);


if 11.1<a≤18.2, coordinates (x,y,z) in the ternary composition diagram are on or below a straight line GI that connects point G (0.02a2−1.6013a+71.105, −0.02a2+0.6013a+28.895, 0.0) and point I (0.02a2−1.6013a+71.105, 0.0, −0.02a2+0.6013a+28.895); if 18.2<a≤26.7, coordinates (x,y,z) in the ternary composition diagram are on or below a straight line GI that connects point G (0.0135a2−1.4068a+69.727, −0.0135a2+0.4068a+30.273, 0.0) and point I (0.0135a2−1.4068a+69.727, 0.0, −0.0135a2+0.4068a+30.273); if 26.7<a≤36.7, coordinates (x,y,z) in the ternary composition diagram are on or below a straight line GI that connects point G (0.0111a2−1.3152a+68.986, −0.0111a2+0.3152a+31.014, 0.0) and point I (0.0111a2−1.3152a+68.986, 0.0, −0.0111a2+0.3152a+31.014); and if 36.7<a≤46.7, coordinates (x,y,z) in the ternary composition diagram are on or below a straight line GI that connects point G (0.0061a2−0.9918a+63.902, −0.0061a2−0.0082a+36.098,0.0) and point I (0.0061a2−0.9918a+63.902, 0.0, −0.0061a2−0.0082a+36.098).


Three points corresponding to point G (Table 105) and point I (Table 106) were individually obtained in each of the following five ranges by calculation, and their approximate expressions were obtained.












TABLE 105







Item
11.1 ≥ R32 > 0
18.2 ≥ R32 ≥ 11.1
26.7 ≥ R32 ≥ 18.2



















R32
0
7.1
11.1
11.1
14.5
18.2
18.2
21.9
26.7


HFO-1132 (E)
72.0
60.9
55.8
55.8
52.1
48.6
48.6
45.4
41.8


HFO-1123
28.0
32.0
33.1
33.1
33.4
33.2
33.2
32.7
31.5


R1234yf
0
0
0
0
0
0
0
0
0










R32
a
a
a


HFO-1132 (E)
0.026a2 − 1.7478a + 72.0
0.02a2 − 1.6013a + 71.105
0.0135a2 − 1.4068a + 69.727


Approximate





expression





HFO-1123
−0.026a2 + 0..7478a + 28.0
−0.02a2 + 0..6013a + 28.895
−0.0135a2 + 0.4068a + 30.273


Approximate





expression





R1234yf
0
0
0


Approximate





expression












Item
36.7 ≥ R32 ≥ 26.7
46.7 ≥ R32 ≥ 36.7
















R32
26.7
29.3
36.7
36.7
44.1
47.8


HFO-1132 (E)
41.8
40.0
35.7
35.7
32.0
30.4


HFO-1123
31.5
30.7
27.6
27.6
23.9
21.8


R1234yf
0
0
0
0
0
0









R32
a
a


HFO-1132 (E)
0.0111a2 − 1.3152a + 68.986
0.0061a2 − 0.9918a + 63.902


Approximate




expression




HFO-1123
−0.0111a2 + 0.3152a + 31.014
−0.0061a2 − 0.0082a + 36.098


Approximate




expression




R1234yf
0
0


Approximate




expression



















TABLE 106







Item
11.1 ≥ R32 > 0
18.2 ≥ R32 ≥ 11.1
26.7 ≥ R32 ≥ 18.2



















R32
0
7.1
11.1
11.1
14.5
18.2
18.2
21.9
26.7


HFO-1132 (E)
72.0
60.9
55.8
55.8
52.1
48.6
48.6
45.4
41.8


HFO-1123
0
0
0
0
0
0
0
0
0


R1234yf
28.0
32.0
33.1
33.1
33.4
33.2
33.2
32.7
31.5










R32
a
a
a


HFO-1132 (E)
0.026a2 − 1.7478a + 72.0
0.02a2 − 1.6013a + 71.105
0.0135a2 − 1.4068a + 69.727


Approximate





expression





HFO-1123
0
0
0


Approximate





expression





R1234yf
−0.026a2 + 0.7478a + 28.0
−0.02a2 + 0.6013a + 28.895
−0.0135a2 + 0.4068a + 30.273


Approximate





expression












Item
36.7 ≥ R32 ≥ 26.7
46.7 ≥ R32 ≥ 36.7
















R32
26.7
29.3
36.7
36.7
44.1
47.8


HFO-1132 (E)
41.8
40.0
35.7
35.7
32.0
30.4


HFO-1123
0
0
0
0
0
0


R1234yf
31.5
30.7
23.6
23.6
23.5
21.8









R32
x
x


HFO-1132 (E)
0.0111a2 − 1.3152a + 68.986
0.0061a2 − 0.9918a + 63.902


Approximate




expression




HFO-1123
0
0


Approximate




expression




R1234yf
−0.0111a2 + 0.3152a + 31.014
−0.0061a2 − 0.0082a + 36.098


Approximate




expression









The results in Tables 101 to 104 indicate that the refrigerant is determined to have a WCFF lower flammability, and the flammability classification according to the ASHRAE Standard is “2L (flammability)” in the following cases:


When the mass % of HFO-1132(E), HFO-1123, R1234yf, and R32 based on their sum in the mixed refrigerant of HFO-1132(E), HFO-1123, R1234yf, and R32 is respectively represented by x, y, z, and a, in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R1234yf is (100−a) mass % and a straight line connecting a point (0.0, 100.0−a, 0.0) and a point (0.0, 0.0, 100.0−a) is the base, if 0<a≤11.1, coordinates (x,y,z) in the ternary composition diagram are on or below a straight line JK′ that connects point J (0.0049a2−0.9645a+47.1, −0.0049a2−0.0355a+52.9, 0.0) and point K′(0.0514a2−2.4353a+61.7, −0.0323a2+0.4122a+5.9, −0.0191a2+1.0231a+32.4); if 11.1<a≤18.2, coordinates are on a straight line JK′ that connects point J (0.0243a2−1.4161a+49.725, −0.0243a2+0.4161a+50.275, 0.0) and point K′(0.0341a2−2.1977a+61.187, −0.0236a2+0.34a+5.636, −0.0105a2+0.8577a+33.177); if 18.2<a≤26.7, coordinates are on or below a straight line JK′ that connects point J (0.0246a2−1.4476a+50.184, −0.0246a2+0.4476a+49.816, 0.0) and point K′ (0.0196a2−1.7863a+58.515, −0.0079a2−0.1136a+8.702, −0.0117a2+0.8999a+32.783); if 26.7<a≤36.7, coordinates are on or below a straight line JK′ that connects point J (0.0183a2−1.1399a+46.493, −0.0183a2+0.1399a+53.507, 0.0) and point K′ (−0.0051a2+0.0929a+25.95, 0.0, 0.0051a2−1.0929a+74.05); and if 36.7<a≤46.7, coordinates are on or below a straight line JK′ that connects point J (−0.0134a2+1.0956a+7.13, 0.0134a2−2.0956a+92.87, 0.0) and point K′(−1.892a+29.443, 0.0, 0.892a+70.557).


Actual points having a WCFF lower flammability form a curved line that connects point J and point K′ (on the straight line AB) in FIG. 3 and extends toward the HFO-1132(E) side. Accordingly, when coordinates are on or below the straight line JK′, WCFF lower flammability is achieved.


Three points corresponding to point J (Table 107) and point K′ (Table 108) were individually obtained in each of the following five ranges by calculation, and their approximate expressions were obtained.












TABLE 107







Item
11.1 ≥ R32 > 0
18.2 ≥ R32 ≥ 11.1
26.7 ≥ R32 ≥ 18.2



















R32
0
7.1
11.1
11.1
14.5
18.2
18.2
21.9
26.7


HFO-1132 (E)
47.1
40.5
37
37.0
34.3
32.0
32.0
30.3
29.1


HFO-1123
52.9
52.4
51.9
51.9
51.2
49.8
49.8
47.8
44.2


R1234yf
0
0
0
0
0
0
0
0
0










R32
a
a
a


HFO-1132 (E)
0.0049a2 − 0.9645a + 47.1
0.0243a2 − 1.4161a + 49.725
0.0246a2 − 1.4476a + 50.184


Approximate





expression





HFO-1123
−0.0049a2 − 0.0355a + 52.9
−0.0243a2 + 0.4161a + 50.275
−0.0246a2 + 0.4476a + 49.816


Approximate





expression





R1234yf
0
0
0


Approximate





expression












Item
36.7 ≥ R32 ≥ 26.7
47.8 ≥ R32 ≥ 36.7
















R32
26.7
29.3
36.7
36.7
44.1
47.8


HFO-1132 (E)
29.1
28.8
29.3
29.3
29.4
28.9


HFO-1123
44.2
41.9
34.0
34.0
26.5
23.3


R1234yf
0
0
0
0
0
0









R32
a
a


HFO-1132 (E)
0.0183a2 − 1.1399a + 46.493
−0.0134a2 + 1.0956a + 7.13


Approximate




expression




HFO-1123
−0.0183a2 + 0.1399a + 53.507
0.0134a2 − 2.0956a + 92.87


Approximate




expression




R1234yf
0
0


Approximate




expression



















TABLE 108







Item
11.1 ≥ R32 > 0
18.2 ≥ R32 ≥ 11.1
26.7 ≥ R32 ≥ 18.2



















R32
0
7.1
11.1
11.1
14.5
18.2
18.2
21.9
26.7


HFO-1132 (E)
61.7
47.0
41.0
41.0
36.5
32.5
32.5
28.8
24.8


HFO-1123
5.9
7.2
6.5
6.5
5.6
4.0
4.0
2.4
0


R1234yf
32.4
38.7
41.4
41.4
43.4
45.3
45.3
46.9
48.5










R32
x
x
x


HFO-1132 (E)
0.0514a2 − 2.4353a + 61.7
0.0341a2 − 2.1977a + 61.187
0.0196a2 − 1.7863a + 58.515


Approximate





expression





HFO-1123
−0.0323a2 + 0.4122a + 5.9
−0.0236a2 + 0.34a + 5.636
−0.0079a2 − 0.1136a + 8.702


Approximate





expression





R1234yf
−0.0191a2 + 1.0231a + 32.4
−0.0105a2 + 0.8577a + 33.177
−0.0117a2 + 0.8999a + 32.783


Approximate





expression












Item
36.7 ≥ R32 ≥ 26.7
46.7 ≥ R32 ≥ 36.7
















R32
26.7
29.3
36.7
36.7
44.1
47.8


HFO-1132 (E)
24.8
24.3
22.5
22.5
21.1
20.4


HFO-1123
0
0
0
0
0
0


R1234yf
48.5
46.4
40.8
40.8
34.8
31.8









R32
x
x


HFO-1132 (E)
−0.0051a2 + 0.0929a + 25.95
−1.892a + 29.443


Approximate




expression




HFO-1123
0
0


Approximate




expression




R1234yf
0.0051a2 − 1.0929a + 74.05
0.892a + 70.557


Approximate




expression










FIGS. 3 to 13 show compositions whose R32 content a (mass %) is 0 mass %, 7.1 mass %, 11.1 mass %, 14.5 mass %, 18.2 mass %, 21.9 mass %, 26.7 mass %, 29.3 mass %, 36.7 mass %, 44.1 mass %, and 47.8 mass %, respectively.


Points A, B, C, and D′ were obtained in the following manner according to approximate calculation.


Point A is a point where the content of HFO-1123 is 0 mass %, and a refrigerating capacity ratio of 85% relative to that of R410A is achieved. Three points corresponding to point A were obtained in each of the following five ranges by calculation, and their approximate expressions were obtained (Table 109).












TABLE 109







Item
11.1 ≥ R32 > 0
18.2 ≥ R32 ≥ 11.1
26.7 ≥ R32 ≥ 18.2



















R32
0
7.1
11.1
11.1
14.5
18.2
18.2
21.9
26.7


HFO-1132 (E)
68.6
55.3
48.4
48.4
42.8
37
37
31.5
24.8


HFO-1123
0
0
0
0
0
0
0
0
0


R1234yf
31.4
37.6
40.5
40.5
42.7
44.8
44.8
46.6
48.5










R32
a
a
a


HFO-1132 (E)
0.0134a2 − 1.9681a + 68.6
0.0112a2 − 1.9337a + 68.484
0.0107a2 − 1.9142a + 68.305


Approximate





expression





HFO-1123
0
0
0


Approximate





expression





R1234yf
−0.0134a2 + 0.9681a + 31.4
−0.0112a2 + 0.9337a + 31.516
−0.0107a2 + 0.9142a + 31.695


Approximate





expression












Item
36.7 ≥ R32 ≥ 26.7
46.7 ≥ R32 ≥ 36.7
















R32
26.7
29.3
36.7
36.7
44.1
47.8


HFO-1132 (E)
24.8
21.3
12.1
12.1
3.8
0


HFO-1123
0
0
0
0
0
0


R1234yf
48.5
49.4
51.2
51.2
52.1
52.2









R32
a
a


HFO-1132 (E)
0.0103a2 − 1.9225a + 68.793
0.0085a2 − 1.8102a + 67.1


Approximate




expression




HFO-1123
0
0


Approximate




expression




R1234yf
−0.0103a2 + 0.9225a + 31..207
−0.0085a2 + 0.8102a + 32.9


Approximate




expression









Point B is a point where the content of HFO-1132(E) is 0 mass %, and a refrigerating capacity ratio of 85% relative to that of R410A is achieved.


Three points corresponding to point B were obtained in each of the following five ranges by calculation, and their approximate expressions were obtained (Table 110).












TABLE 110







Item
11.1 ≥ R32 > 0
18.2 ≥ R32 ≥ 11.1
26.7 ≥ R32 ≥ 18.2



















R32
0
7.1
11.1
11.1
14.5
18.2
18.2
21.9
26.7


HFO-1132 (E)
0
0
0
0
0
0
0
0
0


HFO-1123
58.7
47.8
42.3
42.3
37.8
33.1
33.1
28.5
22.9


R1234yf
41.3
45.1
46.6
46.6
47.7
48.7
48.7
49.6
50.4










R32
a
a
a


HFO-1132 (E)
0
0
0


Approximate





expression





HFO-1123
0.0144a2 − 1.6377a + 58.7
0.0075a2 − 1.5156a + 58.199
0.009a2 − 1.6045a + 59.318


Approximate





expression





R1234yf
−0.0144a2 + 0.6377a + 41.3
−0.0075a2 + 0.5156a + 41.801
−0.009a2 + 0.6045a + 40.682


Approximate





expression












Item
36.7 ≥ R32 ≥ 26.7
46.7 ≥ R32 ≥ 36.7
















R32
26.7
29.3
36.7
36.7
44.1
47.8


HFO-1132 (E)
0
0
0
0
0
0


HFO-1123
22.9
19.9
11.7
11.8
3.9
0


R1234yf
50.4
50.8
51.6
51.5
52.0
52.2









R32
a
a


HFO-1132 (E)
0
0


Approximate




expression




HFO-1123
0.0046a2 − 1.41a + 57.286
0.0012a2 − 1.1659a + 52.95


Approximate




expression




R1234yf
−0.0046a2 + 0.41a + 42.714
−0.0012a2 + 0.1659a + 47.05


Approximate




expression









Point D′ is a point where the content of HFO-1132(E) is 0 mass %, and a COP ratio of 95.5% relative to that of R410A is achieved.


Three points corresponding to point D′ were obtained in each of the following by calculation, and their approximate expressions were obtained (Table 111).












TABLE 111







Item
11.1 ≥ R32 > 0





















R32
0
7.1
11.1



HFO-1132(E)
0
0
0



HFO-1123
75.4
83.4
88.9



R1234yf
24.6
9.5
0










R32
a



HFO-1132(E)




Approximate
0



expression




HFO-1123
  0.0224a2 + 0.968a + 75.4



Approximate




expression




R1234yf
−0.0224a2 − 1.968a + 24.6



Approximate




expression










Point C is a point where the content of R1234yf is 0 mass %, and a COP ratio of 95.5% relative to that of R410A is achieved.


Three points corresponding to point C were obtained in each of the following by calculation, and their approximate expressions were obtained (Table 112).












TABLE 112







Item
11.1 ≥ R32 > 0





















R32
0
7.1
11.1



HFO-1132(E)
32.9
18.4
0



HFO-1123
67.1
74.5
88.9



R1234yf
0
0
0










R32
a



HFO-1132(E)
−0.2304a2 − 0.4062a + 32.9



Approximate




expression




HFO-1123
  0.2304a2 − 0.5938a + 67.1



Approximate




expression




R1234yf
0



Approximate




expression










(5-4) Refrigerant D

The refrigerant D according to the present disclosure is a mixed refrigerant comprising trans-1,2-difluoroethylene (HFO-1132(E)), difluoromethane (R32), and 2,3,3,3-tetrafluoro-1-propene (R1234yf).


The refrigerant D according to the present disclosure has various properties that are desirable as an R410A-alternative refrigerant; i.e., a refrigerating capacity equivalent to that of R410A, a sufficiently low GWP, and a lower flammability (Class 2L) according to the ASHRAE standard.


The refrigerant D according to the present disclosure is preferably a refrigerant wherein


when the mass % of HFO-1132(E), R32, and R1234yf based on their sum is respectively represented by x, y, and z, coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), R32, and R1234yf is 100 mass % are within the range of a figure surrounded by line segments IJ, JN, NE, and EI that connect the following 4 points:


point I (72.0, 0.0, 28.0),


point J (48.5, 18.3, 33.2),


point N (27.7, 18.2, 54.1), and


point E (58.3, 0.0, 41.7),


or on these line segments (excluding the points on the line segment EI);


the line segment IJ is represented by coordinates (0.0236y2−1.7616y+72.0, y, −0.0236y2+0.7616y+28.0);


the line segment NE is represented by coordinates (0.012y2−1.9003y+58.3, y, −0.012y2+0.9003y+41.7); and


the line segments JN and EI are straight lines. When the requirements above are satisfied, the refrigerant according to the present disclosure has a refrigerating capacity ratio of 80% or more relative to R410A, a GWP of 125 or less, and a WCF lower flammability.


The refrigerant D according to the present disclosure is preferably a refrigerant wherein


when the mass % of HFO-1132(E), R32, and R1234yf based on their sum is respectively represented by x, y, and z, coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), R32, and R1234yf is 100 mass % are within the range of a figure surrounded by line segments MM′, M′N, NV, VG, and GM that connect the following 5 points:


point M (52.6, 0.0, 47.4),


point M′ (39.2, 5.0, 55.8),


point N (27.7, 18.2, 54.1),


point V (11.0, 18.1, 70.9), and


point G (39.6, 0.0, 60.4),


or on these line segments (excluding the points on the line segment GM);


the line segment MM′ is represented by coordinates (0.132y2−3.34y+52.6, y, −0.132y2+2.34y+47.4);


the line segment M′N is represented by coordinates (0.0596y2−2.2541y+48.98, y, −0.0596y2+1.2541y+51.02);


the line segment VG is represented by coordinates (0.0123y2−1.8033y+39.6, y, −0.0123y2+0.8033y+60.4); and


the line segments NV and GM are straight lines. When the requirements above are satisfied, the refrigerant according to the present disclosure has a refrigerating capacity ratio of 70% or more relative to R410A, a GWP of 125 or less, and an ASHRAE lower flammability.


The refrigerant D according to the present disclosure is preferably a refrigerant wherein


when the mass % of HFO-1132(E), R32, and R1234yf based on their sum is respectively represented by x, y, and z, coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), R32, and R1234yf is 100 mass % are within the range of a figure surrounded by line segments ON, NU, and UO that connect the following 3 points:


point O (22.6, 36.8, 40.6),


point N (27.7, 18.2, 54.1), and


point U (3.9, 36.7, 59.4),


or on these line segments;


the line segment ON is represented by coordinates (0.0072y2−0.6701y+37.512, y, −0.0072y2−0.3299y+62.488);


the line segment NU is represented by coordinates (0.0083y2−1.7403y+56.635, y, −0.0083y2+0.7403y+43.365); and


the line segment UO is a straight line. When the requirements above are satisfied, the refrigerant according to the present disclosure has a refrigerating capacity ratio of 80% or more relative to R410A, a GWP of 250 or less, and an ASHRAE lower flammability.


The refrigerant D according to the present disclosure is preferably a refrigerant wherein


when the mass % of HFO-1132(E), R32, and R1234yf based on their sum is respectively represented by x, y, and z, coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), R32, and R1234yf is 100 mass % are within the range of a figure surrounded by line segments QR, RT, TL, LK, and KQ that connect the following 5 points:


point Q (44.6, 23.0, 32.4),


point R (25.5, 36.8, 37.7),


point T (8.6, 51.6, 39.8),


point L (28.9, 51.7, 19.4), and


point K (35.6, 36.8, 27.6),


or on these line segments;


the line segment QR is represented by coordinates (0.0099y2−1.975y+84.765, y, −0.0099y2+0.975y+15.235);


the line segment RT is represented by coordinates (0.0082y2−1.8683y+83.126, y, −0.0082y2+0.8683y+16.874);


the line segment LK is represented by coordinates (0.0049y2−0.8842y+61.488, y, −0.0049y2−0.1158y+38.512);


the line segment KQ is represented by coordinates (0.0095y2−1.2222y+67.676, y, −0.0095y2+0.2222y+32.324); and


the line segment TL is a straight line. When the requirements above are satisfied, the refrigerant according to the present disclosure has a refrigerating capacity ratio of 92.5% or more relative to R410A, a GWP of 350 or less, and a WCF lower flammability.


The refrigerant D according to the present disclosure is preferably a refrigerant wherein


when the mass % of HFO-1132(E), R32, and R1234yf based on their sum is respectively represented by x, y, and z, coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), R32, and R1234yf is 100 mass % are within the range of a figure surrounded by line segments PS, ST, and TP that connect the following 3 points:


point P (20.5, 51.7, 27.8),


point S (21.9, 39.7, 38.4), and


point T (8.6, 51.6, 39.8),


or on these line segments;


the line segment PS is represented by coordinates (0.0064y2−0.7103y+40.1, y, −0.0064y2−0.2897y+59.9);


the line segment ST is represented by coordinates (0.0082y2−1.8683y+83.126, y, −0.0082y2+0.8683y+16.874); and


the line segment TP is a straight line. When the requirements above are satisfied, the refrigerant according to the present disclosure has a refrigerating capacity ratio of 92.5% or more relative to R410A, a GWP of 350 or less, and an ASHRAE lower flammability.


The refrigerant D according to the present disclosure is preferably a refrigerant wherein


when the mass % of HFO-1132(E), R32, and R1234yf based on their sum is respectively represented by x, y, and z, coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), R32, and R1234yf is 100 mass % are within the range of a figure surrounded by line segments ac, cf, fd, and da that connect the following 4 points:


point a (71.1, 0.0, 28.9),


point c (36.5, 18.2, 45.3),


point f (47.6, 18.3, 34.1), and


point d (72.0, 0.0, 28.0),


or on these line segments;


the line segment ac is represented by coordinates (0.0181y2−2.2288y+71.096, y, −0.0181y2+1.2288y+28.904);


the line segment fd is represented by coordinates (0.02y2−1.7y+72, y, −0.02y2+0.7y+28); and


the line segments cf and da are straight lines. When the requirements above are satisfied, the refrigerant according to the present disclosure has a refrigerating capacity ratio of 85% or more relative to R410A, a GWP of 125 or less, and a lower flammability (Class 2L) according to the ASHRAE standard.


The refrigerant D according to the present disclosure is preferably a refrigerant wherein


when the mass % of HFO-1132(E), R32, and R1234yf based on their sum is respectively represented by x, y, and z, coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), R32, and R1234yf is 100 mass % are within the range of a figure surrounded by line segments ab, be, ed, and da that connect the following 4 points:


point a (71.1, 0.0, 28.9),


point b (42.6, 14.5, 42.9),


point e (51.4, 14.6, 34.0), and


point d (72.0, 0.0, 28.0),


or on these line segments;


the line segment ab is represented by coordinates (0.0181y2−2.2288y+71.096, y, −0.0181y2+1.2288y+28.904);


the line segment ed is represented by coordinates (0.02y2−1.7y+72, y, −0.02y2+0.7y+28); and


the line segments be and da are straight lines. When the requirements above are satisfied, the refrigerant according to the present disclosure has a refrigerating capacity ratio of 85% or more relative to R410A, a GWP of 100 or less, and a lower flammability (Class 2L) according to the ASHRAE standard.


The refrigerant D according to the present disclosure is preferably a refrigerant wherein


when the mass % of HFO-1132(E), R32, and R1234yf based on their sum is respectively represented by x, y, and z, coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), R32, and R1234yf is 100 mass % are within the range of a figure surrounded by line segments gi, ij, and jg that connect the following 3 points:


point g (77.5, 6.9, 15.6),


point i (55.1, 18.3, 26.6), and


point j (77.5. 18.4, 4.1),


or on these line segments;


the line segment gi is represented by coordinates (0.02y2−2.4583y+93.396, y, −0.02y2+1.4583y+6.604); and


the line segments ij and jg are straight lines. When the requirements above are satisfied, the refrigerant according to the present disclosure has a refrigerating capacity ratio of 95% or more relative to R410A and a GWP of 100 or less, undergoes fewer or no changes such as polymerization or decomposition, and also has excellent stability.


The refrigerant D according to the present disclosure is preferably a refrigerant wherein


when the mass % of HFO-1132(E), R32, and R1234yf based on their sum is respectively represented by x, y, and z, coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), R32, and R1234yf is 100 mass % are within the range of a figure surrounded by line segments gh, hk, and kg that connect the following 3 points:


point g (77.5, 6.9, 15.6),


point h (61.8, 14.6, 23.6), and


point k (77.5, 14.6, 7.9),


or on these line segments;


the line segment gh is represented by coordinates (0.02y2−2.4583y+93.396, y, −0.02y2+1.4583y+6.604); and


the line segments hk and kg are straight lines. When the requirements above are satisfied, the refrigerant according to the present disclosure has a refrigerating capacity ratio of 95% or more relative to R410A and a GWP of 100 or less, undergoes fewer or no changes such as polymerization or decomposition, and also has excellent stability.


The refrigerant D according to the present disclosure may further comprise other additional refrigerants in addition to HFO-1132(E), R32, and R1234yf, as long as the above properties and effects are not impaired. In this respect, the refrigerant according to the present disclosure preferably comprises HFO-1132(E), R32, and R1234yf in a total amount of 99.5 mass % or more, more preferably 99.75 mass % or more, and still more preferably 99.9 mass % or more based on the entire refrigerant.


Such additional refrigerants are not limited, and can be selected from a wide range of refrigerants. The mixed refrigerant may comprise a single additional refrigerant, or two or more additional refrigerants.


(Examples of Refrigerant D)

The present disclosure is described in more detail below with reference to Examples of refrigerant D. However, the refrigerant D is not limited to the Examples.


The composition of each mixed refrigerant of HFO-1132(E), R32, and R1234yf was defined as WCF. A leak simulation was performed using the NIST Standard Reference Database REFLEAK Version 4.0 under the conditions of Equipment, Storage, Shipping, Leak, and Recharge according to the ASHRAE Standard 34-2013. The most flammable fraction was defined as WCFF.


A burning velocity test was performed using the apparatus shown in FIG. 1 in the following manner. First, the mixed refrigerants used had a purity of 99.5% or more, and were degassed by repeating a cycle of freezing, pumping, and thawing until no traces of air were observed on the vacuum gauge. The burning velocity was measured by the closed method. The initial temperature was ambient temperature. Ignition was performed by generating an electric spark between the electrodes in the center of a sample cell. The duration of the discharge was 1.0 to 9.9 ms, and the ignition energy was typically about 0.1 to 1.0 J. The spread of the flame was visualized using schlieren photographs. A cylindrical container (inner diameter: 155 mm, length: 198 mm) equipped with two light transmission acrylic windows was used as the sample cell, and a xenon lamp was used as the light source. Schlieren images of the flame were recorded by a high-speed digital video camera at a frame rate of 600 fps and stored on a PC. Tables 113 to 115 show the results.


















TABLE 113










Comparative

Example

Example

Example





Example 13
Example
12
Example
14
Example
16















Item
Unit
I
11
J
13
K
15
L



















WCF
HFO-1132
Mass %
72
57.2
48.5
41.2
35.6
32
28.9



(E)











R32
Mass %
0
10
18.3
27.6
36.8
44.2
51.7



R1234yf
Mass %
28
32.8
33.2
31.2
27.6
23.8
19.4















Burning Velocity
cm/s
10
10
10
10
10
10
10


(WCF)
































TABLE 114










Comparative

Example

Example






Example 14
Example
19
Example
21
Example














Item
Unit
M
18
W
20
N
22


















WCF
HFO-1132
Mass %
52.6
39.2
32.4
29.3
27.7
24.6



(E)










R32
Mass %
0.0
5.0
10.0
14.5
18.2
27.6



R1234yf
Mass %
47.4
55.8
57.6
56.2
54.1
47.8













Leak condition that results in
Storage,
Storage,
Storage,
Storage,
Storage,
Storage,


WCFF
Shipping,
Shipping,
Shipping,
Shipping,
Shipping,
Shipping,



−40° C.,
−40° C.,
−40° C.,
−40° C.,
−40° C.,
−40° C.,



0%
0%
0%
0%
0%
0%



release,
release,
release,
release,
release,
release,



on the
on the
on the
on the
on the
on the



gas phase
gas phase
gas phase
gas phase
gas phase
gas phase



side
side
side
side
side
side















WCF
HFO-1132
Mass %
72.0
57.8
48.7
43.6
40.6
34.9



(E)










R32
Mass %
0.0
9.5
17.9
24.2
28.7
38.1



R1234yf
Mass %
28.0
32.7
33.4
32.2
30.7
27.0














Burning Velocity
cm/s
8 or less
8 or less
8 or less
8 or less
8 or less
8 or less


(WCF)









Burning Velocity
cm/s
10
10
10
10
10
10


(WCFF)




























TABLE 115










Example 23
Example
Example 25











Item
Unit
O
24
P















WCF
HFO-1132(E)
Mass %
22.6
21.2
20.5



HFO-1123
Mass %
36.8
44.2
51.7



R1234yf
Mass %
40.6
34.6
27.8










Leak condition that
Storage,
Storage,
Storage,


results in WCFF
Shipping,
Shipping,
Shipping,



−40° C.,
−40° C.,
−40° C.,



0% release,
0% release,
0% release,



on the gas
on the gas
on the gas



phase side
phase side
phase side












WCFF
HFO-1132(E)
Mass %
31.4
29.2
27.1



HFO-1123
Mass %
45.7
51.1
56.4



R1234yf
Mass %
23.0
19.7
16.5











Burning Velocity
cm/s
8 or less
8 or less
8 or less


(WCF)






Burning Velocity
cm/s
10
10
10


(WCFF)









The results indicate that under the condition that the mass % of HFO-1132(E), R32, and R1234yf based on their sum is respectively represented by x, y, and z, when coordinates (x,y,z) in the ternary composition diagram shown in FIG. 14 in which the sum of HFO-1132(E), R32, and R1234yf is 100 mass % are on the line segment that connects point I, point J, point K, and point L, or below these line segments, the refrigerant has a WCF lower flammability.


The results also indicate that when coordinates (x,y,z) in the ternary composition diagram shown in FIG. 14 are on the line segments that connect point M, point M′, point W, point J, point N, and point P, or below these line segments, the refrigerant has an ASHRAE lower flammability.


Mixed refrigerants were prepared by mixing HFO-1132(E), R32, and R1234yf in amounts (mass %) shown in Tables 116 to 144 based on the sum of HFO-1132(E), R32, and R1234yf. The coefficient of performance (COP) ratio and the refrigerating capacity ratio relative to R410 of the mixed refrigerants shown in Tables 116 to 144 were determined. The conditions for calculation were as described below.


Evaporating temperature: 5° C.


Condensation temperature: 45° C.


Degree of superheating: 5 K


Degree of subcooling: 5 K


Compressor efficiency: 70%


Tables 116 to 144 show these values together with the GWP of each mixed refrigerant.

















TABLE 116








Comparative
Comparative
Comparative
Comparative
Comparative
Comparative




Comparative
Example 2
Example 3
Example 4
Example 5
Example 6
Example 7


Item
Unit
Example 1
A
B
A′
B′
A″
B″























HFO-1132(E)
Mass %
R410A
81.6
0.0
63.1
0.0
48.2
0.0


R32
Mass %

18.4
18.1
36.9
36.7
51.8
51.5


R1234yf
Mass %

0.0
81.9
0.0
63.3
0.0
48.5


GWP

2088
125
125
250
250
350
350


COP Ratio
% (relative
100
98.7
103.6
98.7
102.3
99.2
102.2



to R410A)









Refrigerating
% (relative
100
105.3
62.5
109.9
77.5
112.1
87.3


Capacity
to R410A)









Ratio
























TABLE 117







Comparative

Comparative

Example

Example




Example 8
Comparative
Example 10
Example

Example
4


Item
Unit
C
Example 9
C'
1
R
3
T























HFO-1132 (E)
Mass %
85.5
66.1
52.1
37.8
25.5
16.6
8.6


R32
Mass %
0.0
10.0
18.2
27.6
36.8
44.2
51.6


R1234yf
Mass %
14.5
23.9
29.7
34.6
37.7
39.2
39.8


GWP

1
69
125
188
250
300
350


COP Ratio
% (relative
99.8
99.3
99.3
99.6
100.2
100.8
101.4



to R410A)









Refrigerating
% (relative
92.5
92.5
92.5
92.5
92.5
92.5
92.5


Capacity
to R410A)









Ratio

























TABLE 118







Comparative

Example

Example
Comparative

Example




Example 11
Example
6
Example
8
Example 12
Example
10


Item
Unit
E
5
N
7
U
G
9
V
























HFO-1132 (E)
Mass %
58.3
40.5
27.7
14.9
3.9
39.6
22.8
11.0


R32
Mass %
0.0
10.0
18.2
27.6
36.7
0.0
10.0
18.1


R1234yf
Mass %
41.7
49.5
54.1
57.5
59.4
60.4
67.2
70.9


GWP

2
70
125
189
250
3
70
125


COP Ratio
% (relative
100.3
100.3
100.7
101.2
101.9
101.4
101.8
102.3



to R410A)










Refrigerating
% (relative
80.0
80.0
80.0
80.0
80.0
70.0
70.0
70.0


Capacity
to R410A)










Ratio

























TABLE 119







Compar-











ative











Exam-

Exam-

Exam-

Exam-
Exam-




ple 13
Exam-
ple 12
Exam-
ple 14
Exam-
ple 16
ple 17


Item
Unit
I
ple 11
J
ple 13
K
ple 15
L
Q
























HFO-1132(E)
Mass %
72.0
57.2
48.5
41.2
35.6
32.0
28.9
44.6


R32
Mass %
0.0
10.0
18.3
27.6
36.8
44.2
51.7
23.0


R1234yf
Mass %
28.0
32.8
33.2
31.2
27.6
23.8
19.4
32.4


GWP

2
69
125
188
250
300
350
157


COP Ratio
% (relative
99.9
99.5
99.4
99.5
99.6
99.8
100.1
99.4



to R410A)










Refrigerating
% (relative
86.6
88.4
90.9
94.2
97.7
100.5
103.3
92.5


Capacity
to R410A)










Ratio























TABLE 120







Com-









para









tive









Exam-

Exam-

Exam-





ple 14
Exam-
ple 19
Exam-
ple 21
Exam-


Item
Unit
M
ple 18
W
ple 20
N
ple 22






















HFO-
Mass %
52.6
39.2
32.4
29.3
27.7
24.5


1132(E)









R32
Mass %
0.0
5.0
10.0
14.5
18.2
27.6


R1234yf
Mass %
47.4
55.8
57.6
56.2
54.1
47.9


GWP

2
36
70
100
125
188


COP
% (rela-
100.5
100.9
100.9
100.8
100.7
100.4


Ratio
tive to









R410A)








Refrig-
% (rela-
77.1
74.8
75.6
77.8
80.0
85.5


erating
tive to








Capacity
R410A)








Ratio





















TABLE 121







Example
Exam-
Example
Example




23
ple
25
26


Item
Unit
O
24
P
S




















HFO-1132(E)
Mass %
22.6
21.2
20.5
21.9


R32
Mass %
36.8
44.2
51.7
39.7


R1234yf
Mass %
40.6
34.6
27.8
38.4


GWP

250
300
350
270


COP Ratio
% (relative
100.4
100.5
100.6
100.4



to R410A)






Refrigerating
% (relative
91.0
95.0
99.1
92.5


Capacity
to R410A)






Ratio

























TABLE 122







Compar-
Compar-
Compar-
Compar-


Compar-
Compar-




ative
ative
ative
ative


ative
ative




Exam-
Exam-
Exam-
Exam-
Exam-
Exam-
Exam-
Exam-


Item
Unit
ple 15
ple 16
ple 17
ple 18
ple 27
ple 28
ple 19
ple 20
























HFO-1132(E)
Mass %
10.0
20.0
30.0
40.0
50.0
60.0
70.0
80.0


R32
Mass %
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0


R1234yf
Mass %
85.0
75.0
65.0
55.0
45.0
35.0
25.0
15.0


GWP

37
37
37
36
36
36
35
35


COP Ratio
% (relative
103.4
102.6
101.6
100.8
100.2
99.8
99.6
99.4



to R410A)










Refrigerating
% (relative
56.4
63.3
69.5
75.2
80.5
85.4
90.1
94.4


Capacity
to R410A)










Ratio

























TABLE 123







Compar-
Compar-

Compar-

Compar-
Compar-
Compar-




ative
ative

ative

ative
ative
ative




Exam-
Exam-
Exam-
Exam-
Exam-
Exam-
Exam-
Exam-


Item
Unit
ple 21
ple 22
ple 29
ple 23
ple 30
ple 24
ple 25
ple 26
























HFO-1132(E)
Mass %
10.0
20.0
30.0
40.0
50.0
60.0
70.0
80.0


R32
Mass %
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0


R1234yf
Mass %
80.0
70.0
60.0
50.0
40.0
30.0
20.0
10.0


GWP

71
71
70
70
70
69
69
69


COP Ratio
% (relative
103.1
102.1
101.1
100.4
99.8
99.5
99.2
99.1



to R410A)










Refrigerating
% (relative
61.8
68.3
74.3
79.7
84.9
89.7
94.2
98.4


Capacity
to R410A)










Ratio

























TABLE 124







Compar-

Compar-


Compar-
Compar-
Compar-




ative

ative


ative
ative
ative




Exam-
Exam-
Exam-
Exam-
Exam-
Exam-
Exam-
Exam-


Item
Unit
ple 27
ple 31
ple 28
ple 32
ple 33
ple 29
ple 30
ple 31
























HFO-1132(E)
Mass %
10.0
20.0
30.0
40.0
50.0
60.0
70.0
80.0


R32
Mass %
15.0
15.0
15.0
15.0
15.0
15.0
15.0
15.0


R1234yf
Mass %
75.0
65.0
55.0
45.0
35.0
25.0
15.0
5.0


GWP

104
104
104
103
103
103
103
102


COP Ratio
% (relative
102.7
101.6
100.7
100.0
99.5
99.2
99.0
98.9



to R410A)










Refrigerating
% (relative
66.6
72.9
78.6
84.0
89.0
93.7
98.1
102.2


Capacity
to R410A)










Ratio

























TABLE 125







Compar-
Compar-
Compar-
Compar-
Compar-
Compar-
Compar-
Compar-




ative
ative
ative
ative
ative
ative
ative
ative




Exam-
Exam-
Exam-
Exam-
Exam-
Exam-
Exam-
Exam-


Item
Unit
ple 32
ple 33
ple 34
ple 35
ple 36
ple 37
ple 38
ple 39
























HFO-1132(E)
Mass %
10.0
20.0
30.0
40.0
50.0
60.0
70.0
10.0


R32
Mass %
20.0
20.0
20.0
20.0
20.0
20.0
20.0
25.0


R1234yf
Mass %
70.0
60.0
50.0
40.0
30.0
20.0
10.0
65.0


GWP

138
138
137
137
137
136
136
171


COP Ratio
% (relative
102.3
101.2
100.4
99.7
99.3
99.0
98.8
101.9



to R410A)










Refrigerating
% (relative
71.0
77.1
82.7
88.0
92.9
97.5
101.7
75.0


Capacity
to R410A)










Ratio

























TABLE 126








Compar-
Compar-
Compar-
Compar-
Compar-
Compar-






ative
ative
ative
ative
ative
ative





Exam-
Exam-
Exam-
Exam-
Exam-
Exam-
Exam-
Exam-


Item
Unit
ple 34
ple 40
ple 41
ple 42
ple 43
ple 44
ple 45
ple 35
























HFO-1132(E)
Mass %
20.0
30.0
40.0
50.0
60.0
70.0
10.0
20.0


R32
Mass %
25.0
25.0
25.0
25.0
25.0
25.0
30.0
30.0


R1234yf
Mass %
55.0
45.0
35.0
25.0
15.0
5.0
60.0
50.0


GWP

171
171
171
170
170
170
205
205


COP Ratio
% (relative
100.9
100.1
99.6
99.2
98.9
98.7
101.6
100.7



to R410A)










Refrigerating
% (relative
81.0
86.6
91.7
96.5
101.0
105.2
78.9
84.8


Capacity
to R410A)










Ratio

























TABLE 127







Compar-
Compar-
Compar-
Compar-



Compar-




ative
ative
ative
ative



ative




Exam-
Exam-
Exam-
Exam-
Exam-
Exam-
Exam-
Exam-


Item
Unit
ple 46
ple 47
ple 48
ple 49
ple 36
ple 37
ple 38
ple 50
























HFO-1132(E)
Mass %
30.0
40.0
50.0
60.0
10.0
20.0
30.0
40.0


R32
Mass %
30.0
30.0
30.0
30.0
35.0
35.0
35.0
35.0


R1234yf
Mass %
40.0
30.0
20.0
10.0
55.0
45.0
35.0
25.0


GWP

204
204
204
204
239
238
238
238


COP Ratio
% (relative
100.0
99.5
99.1
98.8
101.4
100.6
99.9
99.4



to R410A)










Refrigerating
% (relative
90.2
95.3
100.0
104.4
82.5
88.3
93.7
98.6


Capacity
to R410A)










Ratio

























TABLE 128







Compar-
Compar-
Compar-
Compar-

Compar-
Compar-
Compar-




ative
ative
ative
ative

ative
ative
ative




Exam-
Exam-
Exam-
Exam-
Exam-
Exam-
Exam-
Exam-


Item
Unit
ple 51
ple 52
ple 53
ple 54
ple 39
ple 55
ple 56
ple 57
























HFO-1132(E)
Mass %
50.0
60.0
10.0
20.0
30.0
40.0
50.0
10.0


R32
Mass %
35.0
35.0
40.0
40.0
40.0
40.0
40.0
45.0


R1234yf
Mass %
15.0
5.0
50.0
40.0
30.0
20.0
10.0
45.0


GWP

237
237
272
272
272
271
271
306


COP Ratio
% (relative
99.0
98.8
101.3
100.6
99.9
99.4
99.0
101.3



to R410A)










Refrigerating
% (relative
103.2
107.5
86.0
91.7
96.9
101.8
106.3
89.3


Capacity
to R410A)










Ratio

























TABLE 129









Compar-
Compar-
Compar-

Compar-
Compar-






ative
ative
ative

ative
ative




Exam-
Exam-
Exam-
Exam-
Exam-
Exam-
Exam-
Exam-


Item
Unit
ple 40
ple 41
ple 58
ple 59
ple 60
ple 42
ple 61
ple 62
























HFO-1132(E)
Mass %
20.0
30.0
40.0
50.0
10.0
20.0
30.0
40.0


R32
Mass %
45.0
45.0
45.0
45.0
50.0
50.0
50.0
50.0


R1234yf
Mass %
35.0
25.0
15.0
5.0
40.0
30.0
20.0
10.0


GWP

305
305
305
304
339
339
339
338


COP Ratio
% (relative
100.6
100.0
99.5
99.1
101.3
100.6
100.0
99.5



to R410A)










Refrigerating
% (relative
94.9
100.0
104.7
109.2
92.4
97.8
102.9
107.5


Capacity
to R410A)










Ratio

























TABLE 130







Compar-
Compar-
Compar-
Compar-








ative
ative
ative
ative








Exam-
Exam-
Exam-
Exam-
Exam-
Exam-
Exam-
Exam-


Item
Unit
ple 63
ple 64
ple 65
ple 66
ple 43
ple 44
ple 45
ple 46
























HFO-1132(E)
Mass %
10.0
20.0
30.0
40.0
56.0
59.0
62.0
65.0


R32
Mass %
55.0
55.0
55.0
55.0
3.0
3.0
3.0
3.0


R1234yf
Mass %
35.0
25.0
15.0
5.0
41.0
38.0
35.0
32.0


GWP

373
372
372
372
22
22
22
22


COP Ratio
% (relative
101.4
100.7
100.1
99.6
100.1
100.0
99.9
99.8



to R410A)










Refrigerating
% (relative
95.3
100.6
105.6
110.2
81.7
83.2
84.6
86.0


Capacity
to R410A)










Ratio

























TABLE 131







Exam-
Exam-
Exam-
Exam-
Exam-
Exam-
Exam-
Exam-


Item
Unit
ple 47
ple 48
ple 49
ple 50
ple 51
ple 52
ple 53
ple 54
























HFO-1132(E)
Mass %
49.0
52.0
55.0
58.0
61.0
43.0
46.0
49.0


R32
Mass %
6.0
6.0
6.0
6.0
6.0
9.0
9.0
9.0


R1234yf
Mass %
45.0
42.0
39.0
36.0
33.0
48.0
45.0
42.0


GWP

43
43
43
43
42
63
63
63


COP Ratio
% (relative
100.2
100.0
99.9
99.8
99.7
100.3
100.1
99.9



to R410A)










Refrigerating
% (relative
80.9
82.4
83.9
85.4
86.8
80.4
82.0
83.5


Capacity
to R410A)










Ratio

























TABLE 132







Exam-
Exam-
Exam-
Exam-
Exam-
Exam-
Exam-
Exam-


Item
Unit
ple 55
ple 56
ple 57
ple 58
ple 59
ple 60
ple 61
ple 62
























HFO-1132(E)
Mass %
52.0
55.0
58.0
38.0
41.0
44.0
47.0
50.0


R32
Mass %
9.0
9.0
9.0
12.0
12.0
12.0
12.0
12.0


R1234yf
Mass %
39.0
36.0
33.0
50.0
47.0
44.0
41.0
38.0


GWP

63
63
63
83
83
83
83
83


COP Ratio
% (relative
99.8
99.7
99.6
100.3
100.1
100.0
99.8
99.7



to R410A)










Refrigerating
% (relative
85.0
86.5
87.9
80.4
82.0
83.5
85.1
86.6


Capacity
to R410A)










Ratio

























TABLE 133







Exam-
Exam-
Exam-
Exam-
Exam-
Exam-
Exam-
Exam-


Item
Unit
ple 63
ple 64
ple 65
ple 66
ple 67
ple 68
ple 69
ple 70
























HFO-1132(E)
Mass %
53.0
33.0
36.0
39.0
42.0
45.0
48.0
51.0


R32
Mass %
12.0
15.0
15.0
15.0
15.0
15.0
15.0
15.0


R1234yf
Mass %
35.0
52.0
49.0
46.0
43.0
40.0
37.0
34.0


GWP

83
104
104
103
103
103
103
103


COP Ratio
% (relative
99.6
100.5
100.3
100.1
99.9
99.7
99.6
99.5



to R410A)










Refrigerating
% (relative
88.0
80.3
81.9
83.5
85.0
86.5
88.0
89.5


Capacity
to R410A)










Ratio

























TABLE 134







Exam-
Exam-
Exam-
Exam-
Exam-
Exam-
Exam-
Exam-


Item
Unit
ple 71
ple 72
ple 73
ple 74
ple 75
ple 76
ple 77
ple 78
























HFO-1132(E)
Mass %
29.0
32.0
35.0
38.0
41.0
44.0
47.0
36.0


R32
Mass %
18.0
18.0
18.0
18.0
18.0
18.0
18.0
3.0


R1234yf
Mass %
53.0
50.0
47.0
44.0
41.0
38.0
35.0
61.0


GWP

124
124
124
124
124
123
123
23


COP Ratio
% (relative
100.6
100.3
100.1
99.9
99.8
99.6
99.5
101.3



to R410A)










Refrigerating
% (relative
80.6
82.2
83.8
85.4
86.9
88.4
89.9
71.0


Capacity
to R410A)










Ratio

























TABLE 135







Example
Example
Example
Example
Example
Example
Example
Example


Item
Unit
79
80
81
82
83
84
85
86
























HFO-1132(E)
Mass %
39.0
42.0
30.0
33.0
36.0
26.0
29.0
32.0


R32
Mass %
3.0
3.0
6.0
6.0
6.0
9.0
9.0
9.0


R1234yf
Mass %
58.0
55.0
64.0
61.0
58.0
65.0
62.0
59.0


GWP

23
23
43
43
43
64
64
63


COP Ratio
% (relative
101.1
100.9
101.5
101.3
101.0
101.6
101.3
101.1



to R410A)










Refrigerating
% (relative
72.7
74.4
70.5
72.2
73.9
71.0
72.8
74.5


Capacity
to R410A)










Ratio

























TABLE 136







Example
Example
Example
Example
Example
Example
Example
Example


Item
Unit
87
88
89
90
91
92
93
94
























HFO-1132(E)
Mass %
21.0
24.0
27.0
30.0
16.0
19.0
22.0
25.0


R32
Mass %
12.0
12.0
12.0
12.0
15.0
15.0
15.0
15.0


R1234yf
Mass %
67.0
64.0
61.0
58.0
69.0
66.0
63.0
60.0


GWP

84
84
84
84
104
104
104
104


COP Ratio
% (relative
101.8
101.5
101.2
101.0
102.1
101.8
101.4
101.2



to R410A)










Refrigerating
% (relative
70.8
72.6
74.3
76.0
70.4
72.3
74.0
75.8


Capacity
to R410A)










Ratio

























TABLE 137







Example
Example
Example
Example
Example
Example
Example
Example


Item
Unit
95
96
97
98
99
100
101
102
























HFO-1132(E)
Mass %
28.0
12.0
15.0
18.0
21.0
24.0
27.0
25.0


R32
Mass %
15.0
18.0
18.0
18.0
18.0
18.0
18.0
21.0


R1234yf
Mass %
57.0
70.0
67.0
64.0
61.0
58.0
55.0
54.0


GWP

104
124
124
124
124
124
124
144


COP Ratio
% (relative
100.9
102.2
101.9
101.6
101.3
101.0
100.7
100.7



to R410A)










Refrigerating
% (relative
77.5
70.5
72.4
74.2
76.0
77.7
79.4
80.7


Capacity
to R410A)










Ratio

























TABLE 138







Example
Example
Example
Example
Example
Example
Example
Example


Item
Unit
103
104
105
106
107
108
109
110
























HFO-1132(E)
Mass %
21.0
24.0
17.0
20.0
23.0
13.0
16.0
19.0


R32
Mass %
24.0
24.0
27.0
27.0
27.0
30.0
30.0
30.0


R1234yf
Mass %
55.0
52.0
56.0
53.0
50.0
57.0
54.0
51.0


GWP

164
164
185
185
184
205
205
205


COP Ratio
% (relative
100.9
100.6
101.1
100.8
100.6
101.3
101.0
100.8



to R410A)










Refrigerating
% (relative
80.8
82.5
80.8
82.5
84.2
80.7
82.5
84.2


Capacity
to R410A)










Ratio

























TABLE 139







Example
Example
Example
Example
Example
Example
Example
Example


Item
Unit
111
112
113
114
115
116
117
118
























HFO-1132(E)
Mass %
22.0
9.0
12.0
15.0
18.0
21.0
8.0
12.0


R32
Mass %
30.0
33.0
33.0
33.0
33.0
33.0
36.0
36.0


R1234yf
Mass %
48.0
58.0
55.0
52.0
49.0
46.0
56.0
52.0


GWP

205
225
225
225
225
225
245
245


COP Ratio
% (relative
100.5
101.6
101.3
101.0
100.8
100.5
101.6
101.2



to R410A)










Refrigerating
% (relative
85.9
80.5
82.3
84.1
85.8
87.5
82.0
84.4


Capacity
to R410A)










Ratio

























TABLE 140







Example
Example
Example
Example
Example
Example
Example
Example


Item
Unit
119
120
121
122
123
124
125
126
























HFO-1132(E)
Mass %
15.0
18.0
21.0
42.0
39.0
34.0
37.0
30.0


R32
Mass %
36.0
36.0
36.0
25.0
28.0
31.0
31.0
34.0


R1234yf
Mass %
49.0
46.0
43.0
33.0
33.0
35.0
32.0
36.0


GWP

245
245
245
170
191
211
211
231


COP Ratio
% (relative
101.0
100.7
100.5
99.5
99.5
99.8
99.6
99.9



to R410A)










Refrigerating
% (relative
86.2
87.9
89.6
92.7
93.4
93.0
94.5
93.0


Capacity
to R410A)










Ratio

























TABLE 141







Example
Example
Example
Example
Example
Example
Example
Example


Item
Unit
127
128
129
130
131
132
133
134
























HFO-1132(E)
Mass %
33.0
36.0
24.0
27.0
30.0
33.0
23.0
26.0


R32
Mass %
34.0
34.0
37.0
37.0
37.0
37.0
40.0
40.0


R1234yf
Mass %
33.0
30.0
39.0
36.0
33.0
30.0
37.0
34.0


GWP

231
231
252
251
251
251
272
272


COP Ratio
% (relative
99.8
99.6
100.3
100.1
99.9
99.8
100.4
100.2



to R410A)










Refrigerating
% (relative
94.5
96.0
91.9
93.4
95.0
96.5
93.3
94.9


Capacity
to R410A)










Ratio

























TABLE 142







Example
Example
Example
Example
Example
Example
Example
Example


Item
Unit
135
136
137
138
139
140
141
142
























HFO-1132(E)
Mass %
29.0
32.0
19.0
22.0
25.0
28.0
31.0
18.0


R32
Mass %
40.0
40.0
43.0
43.0
43.0
43.0
43.0
46.0


R1234yf
Mass %
31.0
28.0
38.0
35.0
32.0
29.0
26.0
36.0


GWP

272
271
292
292
292
292
292
312


COP Ratio
% (relative
100.0
99.8
100.6
100.4
100.2
100.1
99.9
100.7



to R410A)










Refrigerating
% (relative
96.4
97.9
93.1
94.7
96.2
97.8
99.3
94.4


Capacity
to R410A)










Ratio

























TABLE 143







Example
Example
Example
Example
Example
Example
Example
Example


Item
Unit
143
144
145
146
147
148
149
150
























HFO-1132(E)
Mass %
21.0
23.0
26.0
29.0
13.0
16.0
19.0
22.0


R32
Mass %
46.0
46.0
46.0
46.0
49.0
49.0
49.0
49.0


R1234yf
Mass %
33.0
31.0
28.0
25.0
38.0
35.0
32.0
29.0


GWP

312
312
312
312
332
332
332
332


COP Ratio
% (relative
100.5
100.4
100.2
100.0
101.1
100.9
100.7
100.5



to R410A)










Refrigerating
% (relative
96.0
97.0
98.6
100.1
93.5
95.1
96.7
98.3


Capacity
to R410A)










Ratio



















TABLE 144





Item
Unit
Example 151
Example 152


















HFO-1132(E)
Mass %
25.0
28.0


R32
Mass %
49.0
49.0


R1234yf
Mass %
26.0
23.0


GWP

332
332


COP Ratio
% (relative to
100.3
100.1



R410A)




Refrigerating Capacity
% (relative to
99.8
101.3


Ratio
R410A)











The results also indicate that under the condition that the mass % of HFO-1132(E), R32, and R1234yf based on their sum is respectively represented by x, y, and z, when coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), R32, and R1234yf is 100 mass % are within the range of a figure surrounded by line segments IJ, JN, NE, and EI that connect the following 4 points:


point I (72.0, 0.0, 28.0),


point J (48.5, 18.3, 33.2),


point N (27.7, 18.2, 54.1), and


point E (58.3, 0.0, 41.7),


or on these line segments (excluding the points on the line segment EI),


the line segment IJ is represented by coordinates (0.0236y2−1.7616y+72.0, y, −0.0236y2+0.7616y+28.0),


the line segment NE is represented by coordinates (0.012y2−1.9003y+58.3, y, −0.012y2+0.9003y+41.7), and


the line segments JN and EI are straight lines, the refrigerant D has a refrigerating capacity ratio of 80% or more relative to R410A, a GWP of 125 or less, and a WCF lower flammability.


The results also indicate that under the condition that the mass % of HFO-1132(E), R32, and R1234yf based on their sum is respectively represented by x, y, and z, when coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), R32, and R1234yf is 100 mass % are within the range of a figure surrounded by line segments MM′, M′N, NV, VG, and GM that connect the following 5 points:


point M (52.6, 0.0, 47.4),


point M′ (39.2, 5.0, 55.8),


point N (27.7, 18.2, 54.1),


point V (11.0, 18.1, 70.9), and


point G (39.6, 0.0, 60.4),


or on these line segments (excluding the points on the line segment GM),


the line segment MM′ is represented by coordinates (0.132y2−3.34y+52.6, y, −0.132y2+2.34y+47.4),


the line segment M′N is represented by coordinates (0.0596y2−2.2541y+48.98, y, −0.0596y2+1.2541y+51.02),


the line segment VG is represented by coordinates (0.0123y2−1.8033y+39.6, y, −0.0123y2+0.8033y+60.4), and


the line segments NV and GM are straight lines, the refrigerant D according to the present disclosure has a refrigerating capacity ratio of 70% or more relative to R410A, a GWP of 125 or less, and an ASHRAE lower flammability.


The results also indicate that under the condition that the mass % of HFO-1132(E), R32, and R1234yf based on their sum is respectively represented by x, y, and z, when coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), R32, and R1234yf is 100 mass % are within the range of a figure surrounded by line segments ON, NU, and UO that connect the following 3 points:


point O (22.6, 36.8, 40.6),


point N (27.7, 18.2, 54.1), and


point U (3.9, 36.7, 59.4),


or on these line segments,


the line segment ON is represented by coordinates (0.0072y2−0.6701y+37.512, y, −0.0072y2−0.3299y+62.488),


the line segment NU is represented by coordinates (0.0083y2−1.7403y+56.635, y, −0.0083y2+0.7403y+43.365), and


the line segment UO is a straight line, the refrigerant D according to the present disclosure has a refrigerating capacity ratio of 80% or more relative to R410A, a GWP of 250 or less, and an ASHRAE lower flammability.


The results also indicate that under the condition that the mass % of HFO-1132(E), R32, and R1234yf based on their sum is respectively represented by x, y, and z, when coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), R32, and R1234yf is 100 mass % are within the range of a figure surrounded by line segments QR, RT, TL, LK, and KQ that connect the following 5 points:


point Q (44.6, 23.0, 32.4),


point R (25.5, 36.8, 37.7),


point T (8.6, 51.6, 39.8),


point L (28.9, 51.7, 19.4), and


point K (35.6, 36.8, 27.6),


or on these line segments,


the line segment QR is represented by coordinates (0.0099y2−1.975y+84.765, y, −0.0099y2+0.975y+15.235),


the line segment RT is represented by coordinates (0.0082y2−1.8683y+83.126, y, −0.0082y2+0.8683y+16.874),


the line segment LK is represented by coordinates (0.0049y2−0.8842y+61.488, y, −0.0049y2−0.1158y+38.512),


the line segment KQ is represented by coordinates (0.0095y2−1.2222y+67.676, y, −0.0095y2+0.2222y+32.324), and


the line segment TL is a straight line, the refrigerant D according to the present disclosure has a refrigerating capacity ratio of 92.5% or more relative to R410A, a GWP of 350 or less, and a WCF lower flammability.


The results further indicate that under the condition that the mass % of HFO-1132(E), R32, and R1234yf based on their sum is respectively represented by x, y, and z, when coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), R32, and R1234yf is 100 mass % are within the range of a figure surrounded by line segments PS, ST, and TP that connect the following 3 points:


point P (20.5, 51.7, 27.8),


point S (21.9, 39.7, 38.4), and


point T (8.6, 51.6, 39.8),


or on these line segments,


the line segment PS is represented by coordinates (0.0064y2−0.7103y+40.1, y, −0.0064y2−0.2897y+59.9),


the line segment ST is represented by coordinates (0.0082y2−1.8683y+83.126, y, −0.0082y2+0.8683y+16.874), and


the line segment TP is a straight line, the refrigerant D according to the present disclosure has a refrigerating capacity ratio of 92.5% or more relative to R410A, a GWP of 350 or less, and an ASHRAE lower flammability.


(5-5) Refrigerant E

The refrigerant E according to the present disclosure is a mixed refrigerant comprising trans-1,2-difluoroethylene (HFO-1132(E)), trifluoroethylene (HFO-1123), and difluoromethane (R32).


The refrigerant E according to the present disclosure has various properties that are desirable as an R410A-alternative refrigerant, i.e., a coefficient of performance equivalent to that of R410A and a sufficiently low GWP.


The refrigerant E according to the present disclosure is preferably a refrigerant wherein


when the mass % of HFO-1132(E), HFO-1123, and R32 based on their sum is respectively represented by x, y, and z, coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R32 is 100 mass % are within the range of a figure surrounded by line segments IK, KB′, B′H, HR, RG, and GI that connect the following 6 points:


point I (72.0, 28.0, 0.0),


point K (48.4, 33.2, 18.4),


point B′ (0.0, 81.6, 18.4),


point H (0.0, 84.2, 15.8),


point R (23.1, 67.4, 9.5), and


point G (38.5, 61.5, 0.0),


or on these line segments (excluding the points on the line segments B′H and GI);


the line segment IK is represented by coordinates (0.025z2−1.7429z+72.00, −0.025z2+0.7429z+28.0, z),


the line segment HR is represented by coordinates (−0.3123z2+4.234z+11.06, 0.3123z2−5.234z+88.94, z),


the line segment RG is represented by coordinates (−0.0491z2−1.1544z+38.5, 0.0491z2+0.1544z+61.5, z), and


the line segments KB′ and GI are straight lines. When the requirements above are satisfied, the refrigerant according to the present disclosure has WCF lower flammability, a COP ratio of 93% or more relative to that of R410A, and a GWP of 125 or less.


The refrigerant E according to the present disclosure is preferably a refrigerant wherein


when the mass % of HFO-1132(E), HFO-1123, and R32 based on their sum is respectively represented by x, y, and z, coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R32 is 100 mass % are within the range of a figure surrounded by line segments IJ, JR, RG, and GI that connect the following 4 points:


point I (72.0, 28.0, 0.0),


point J (57.7, 32.8, 9.5),


point R (23.1, 67.4, 9.5), and


point G (38.5, 61.5, 0.0),


or on these line segments (excluding the points on the line segment GI);


the line segment IJ is represented by coordinates (0.025z2−1.7429z+72.0, −0.025z2+0.7429z+28.0, z),


the line segment RG is represented by coordinates (−0.0491z2−1.1544z+38.5, 0.0491z2+0.1544z+61.5, z), and


the line segments JR and GI are straight lines. When the requirements above are satisfied, the refrigerant according to the present disclosure has WCF lower flammability, a COP ratio of 93% or more relative to that of R410A, and a GWP of 125 or less.


The refrigerant E according to the present disclosure is preferably a refrigerant wherein


when the mass % of HFO-1132(E), HFO-1123, and R32 based on their sum is respectively represented by x, y, and z, coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R32 is 100 mass % are within the range of a figure surrounded by line segments MP, PB′, B′H, HR, RG, and GM that connect the following 6 points:


point M (47.1, 52.9, 0.0),


point P (31.8, 49.8, 18.4),


point B′ (0.0, 81.6, 18.4),


point H (0.0, 84.2, 15.8),


point R (23.1, 67.4, 9.5), and


point G (38.5, 61.5, 0.0),


or on these line segments (excluding the points on the line segments B′H and GM);


the line segment MP is represented by coordinates (0.0083z2−0.984z+47.1, −0.0083z2−0.016z+52.9, z),


the line segment HR is represented by coordinates (−0.3123z2+4.234z+11.06, 0.3123z2−5.234z+88.94, z),


the line segment RG is represented by coordinates (−0.0491z2−1.1544z+38.5, 0.0491z2+0.1544z+61.5, z), and


the line segments PB′ and GM are straight lines. When the requirements above are satisfied, the refrigerant according to the present disclosure has ASHRAE lower flammability, a COP ratio of 93% or more relative to that of R410A, and a GWP of 125 or less.


The refrigerant E according to the present disclosure is preferably a refrigerant wherein


when the mass % of HFO-1132(E), HFO-1123, and R32 based on their sum is respectively represented by x, y, and z, coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R32 is 100 mass % are within the range of a figure surrounded by line segments MN, NR, RG, and GM that connect the following 4 points:


point M (47.1, 52.9, 0.0),


point N (38.5, 52.1, 9.5),


point R (23.1, 67.4, 9.5), and


point G (38.5, 61.5, 0.0),


or on these line segments (excluding the points on the line segment GM);


the line segment MN is represented by coordinates (0.0083z2−0.984z+47.1, −0.0083z2−0.016z+52.9, z),


the line segment RG is represented by coordinates (−0.0491z2−1.1544z+38.5, 0.0491z2+0.1544z+61.5, z),


the line segments NR and GM are straight lines. When the requirements above are satisfied, the refrigerant according to the present disclosure has ASHRAE lower flammability, a COP ratio of 93% or more relative to that of R410A, and a GWP of 65 or less.


The refrigerant E according to the present disclosure is preferably a refrigerant wherein


when the mass % of HFO-1132(E), HFO-1123, and R32 based on their sum is respectively represented by x, y, and z, coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R32 is 100 mass % are within the range of a figure surrounded by line segments PS, ST, and TP that connect the following 3 points:


point P (31.8, 49.8, 18.4),


point S (25.4, 56.2, 18.4), and


point T (34.8, 51.0, 14.2),


or on these line segments;


the line segment ST is represented by coordinates (−0.0982z2+0.9622z+40.931, 0.0982z2−1.9622z+59.069, z),


the line segment TP is represented by coordinates (0.0083z2−0.984z+47.1, −0.0083z2−0.016z+52.9, z), and


the line segment PS is a straight line. When the requirements above are satisfied, the refrigerant according to the present disclosure has ASHRAE lower flammability, a COP ratio of 94.5% or more relative to that of R410A, and a GWP of 125 or less.


The refrigerant E according to the present disclosure is preferably a refrigerant wherein


when the mass % of HFO-1132(E), HFO-1123, and R32 based on their sum is respectively represented by x, y, and z, coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R32 is 100 mass % are within the range of a figure surrounded by line segments QB″, B″D, DU, and UQ that connect the following 4 points:


point Q (28.6, 34.4, 37.0),


point B″ (0.0, 63.0, 37.0),


point D (0.0, 67.0, 33.0), and


point U (28.7, 41.2, 30.1),


or on these line segments (excluding the points on the line segment B″D);


the line segment DU is represented by coordinates (−3.4962z2+210.71z−3146.1, 3.4962z2−211.71z+3246.1, z),


the line segment UQ is represented by coordinates (0.0135z2−0.9181z+44.133, −0.0135z2−0.0819z+55.867, z), and


the line segments QB″ and B″D are straight lines. When the requirements above are satisfied, the refrigerant according to the present disclosure has ASHRAE lower flammability, a COP ratio of 96% or more relative to that of R410A, and a GWP of 250 or less.


The refrigerant E according to the present disclosure is preferably a refrigerant wherein


when the mass % of HFO-1132(E), HFO-1123, and R32 based on their sum is respectively represented by x, y, and z, coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R32 is 100 mass % are within the range of a figure surrounded by line segments Oc′, c′d′, d′e′, e′a′, and a′O that connect the following 5 points:


point O (100.0, 0.0, 0.0),


point c′ (56.7, 43.3, 0.0),


point d′ (52.2, 38.3, 9.5),


point e′ (41.8, 39.8, 18.4), and


point a′ (81.6, 0.0, 18.4),


or on the line segments c′d′, d′e′, and e′a′ (excluding the points c′ and a′);


the line segment c′d′ is represented by coordinates (−0.0297z2−0.1915z+56.7, 0.0297z2+1.1915z+43.3, z),


the line segment d′e′ is represented by coordinates (−0.0535z2+0.3229z+53.957, 0.0535z2+0.6771z+46.043, z), and


the line segments Oc′, e′a′, and a′O are straight lines. When the requirements above are satisfied, the refrigerant according to the present disclosure has a COP ratio of 92.5% or more relative to that of R410A, and a GWP of 125 or less.


The refrigerant E according to the present disclosure is preferably a refrigerant wherein


when the mass % of HFO-1132(E), HFO-1123, and R32 based on their sum is respectively represented by x, y, and z, coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R32 is 100 mass % are within the range of a figure surrounded by line segments Oc, cd, de, ea′, and a′O that connect the following 5 points:


point O (100.0, 0.0, 0.0),


point c (77.7, 22.3, 0.0),


point d (76.3, 14.2, 9.5),


point e (72.2, 9.4, 18.4), and


point a′ (81.6, 0.0, 18.4),


or on the line segments cd, de, and ea′ (excluding the points c and a′);


the line segment cde is represented by coordinates (−0.017z2+0.0148z+77.684, 0.017z2+0.9852z+22.316, z), and


the line segments Oc, ea′, and a′O are straight lines. When the requirements above are satisfied, the refrigerant according to the present disclosure has a COP ratio of 95% or more relative to that of R410A, and a GWP of 125 or less.


The refrigerant E according to the present disclosure is preferably a refrigerant wherein


when the mass % of HFO-1132(E), HFO-1123, and R32 based on their sum is respectively represented by x, y, and z, coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R32 is 100 mass % are within the range of a figure surrounded by line segments Oc′, c′d′, d′a, and aO that connect the following 5 points:


point O (100.0, 0.0, 0.0),


point c′ (56.7, 43.3, 0.0),


point d′ (52.2, 38.3, 9.5), and


point a (90.5, 0.0, 9.5),


or on the line segments c′d′ and d′a (excluding the points c′ and a);


the line segment c′d′ is represented by coordinates (−0.0297z2−0.1915z+56.7, 0.0297z2+1.1915z+43.3, z), and


the line segments Oc′, d′a, and aO are straight lines. When the requirements above are satisfied, the refrigerant according to the present disclosure has a COP ratio of 93.5% or more relative to that of R410A, and a GWP of 65 or less.


The refrigerant E according to the present disclosure is preferably a refrigerant wherein


when the mass % of HFO-1132(E), HFO-1123, and R32 based on their sum is respectively represented by x, y, and z, coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R32 is 100 mass % are within the range of a figure surrounded by line segments Oc, cd, da, and aO that connect the following 4 points:


point O (100.0, 0.0, 0.0),


point c (77.7, 22.3, 0.0),


point d (76.3, 14.2, 9.5), and


point a (90.5, 0.0, 9.5),


or on the line segments cd and da (excluding the points c and a);


the line segment cd is represented by coordinates (−0.017z2+0.0148z+77.684, 0.017z2+0.9852z+22.316, z), and


the line segments Oc, da, and aO are straight lines. When the requirements above are satisfied, the refrigerant according to the present disclosure has a COP ratio of 95% or more relative to that of R410A, and a GWP of 65 or less.


The refrigerant E according to the present disclosure may further comprise other additional refrigerants in addition to HFO-1132(E), HFO-1123, and R32, as long as the above properties and effects are not impaired. In this respect, the refrigerant according to the present disclosure preferably comprises HFO-1132(E), HFO-1123, and R32 in a total amount of 99.5 mass % or more, more preferably 99.75 mass % or more, and even more preferably 99.9 mass % or more, based on the entire refrigerant.


Such additional refrigerants are not limited, and can be selected from a wide range of refrigerants. The mixed refrigerant may comprise a single additional refrigerant, or two or more additional refrigerants.


(Examples of Refrigerant E)

The present disclosure is described in more detail below with reference to Examples of refrigerant E. However, the refrigerant E is not limited to the Examples.


Mixed refrigerants were prepared by mixing HFO-1132(E), HFO-1123, and R32 at mass % based on their sum shown in Tables 145 and 146.


The composition of each mixture was defined as WCF. A leak simulation was performed using National Institute of Science and Technology (NIST) Standard Reference Data Base Refleak Version 4.0 under the conditions for equipment, storage, shipping, leak, and recharge according to the ASHRAE Standard 34-2013. The most flammable fraction was defined as WCFF.


For each mixed refrigerant, the burning velocity was measured according to the ANSI/ASHRAE Standard 34-2013. When the burning velocities of the WCF composition and the WCFF composition are 10 cm/s or less, the flammability of such a refrigerant is classified as Class 2L (lower flammability) in the ASHRAE flammability classification.


A burning velocity test was performed using the apparatus shown in FIG. 1 in the following manner. First, the mixed refrigerants used had a purity of 99.5% or more, and were degassed by repeating a cycle of freezing, pumping, and thawing until no traces of air were observed on the vacuum gauge. The burning velocity was measured by the closed method. The initial temperature was ambient temperature. Ignition was performed by generating an electric spark between the electrodes in the center of a sample cell. The duration of the discharge was 1.0 to 9.9 ms, and the ignition energy was typically about 0.1 to 1.0 J. The spread of the flame was visualized using schlieren photographs. A cylindrical container (inner diameter: 155 mm, length: 198 mm) equipped with two light transmission acrylic windows was used as the sample cell, and a xenon lamp was used as the light source. Schlieren images of the flame were recorded by a high-speed digital video camera at a frame rate of 600 fps and stored on a PC.


Tables 145 and 146 show the results.














TABLE 145





Item
Unit
I
J
K
L





















WCF
HFO-1132(E)
mass %
72.0
57.7
48.4
35.5



HFO-1123
mass %
28.0
32.8
33.2
27.5



R32
mass %
0.0
9.5
18.4
37.0












Burning velocity (WCF)
cm/s
10
10
10
10























TABLE 146





Item
Unit
M
N
T
P
U
Q























WCF
HFO-1132(E)
mass %
47.1
38.5
34.8
31.8
28.7
28.6



HFO-1123
mass %
52.9
52.1
51.0
49.8
41.2
34.4



R32
mass %
0.0
9.5
14.2
18.4
30.1
37.0













Leak condition that results in
Storage,
Storage,
Storage,
Storage,
Storage,
Storage,


WCFF
Shipping,
Shipping,
Shipping,
Shipping,
Shipping,
Shipping,



−40° C.,
−40° C.,
−40° C.,
−40° C.,
−40° C.,
−40° C.,



92%,
92%,
92%,
92%,
92%,
92%,



release,
release,
release,
release,
release,
release,



on the
on the
on the
on the
on the
on the



liquid
liquid
liquid
liquid
liquid
liquid



phase
phase
phase
phase
phase
phase



side
side
side
side
side
side















WCFF
HFO-1132(E)
mass %
72.0
58.9
51.5
44.6
31.4
27.1



HFO-1123
mass %
28.0
32.4
33.1
32.6
23.2
18.3



R32
mass %
0.0
8.7
15.4
22.8
45.4
54.6














Burning velocity
cm/s
8 or less
8 or less
8 or less
8 or less
8 or less
8 or less


(WCF)









Burning velocity
cm/s
10
10
10
10
10
10


(WCFF)









The results in Table 1 indicate that in a ternary composition diagram of a mixed refrigerant of HFO-1132(E), HFO-1123, and R32 in which their sum is 100 mass %, a line segment connecting a point (0.0, 100.0, 0.0) and a point (0.0, 0.0, 100.0) is the base, the point (0.0, 100.0, 0.0) is on the left side, and the point (0.0, 0.0, 100.0) is on the right side, when coordinates (x,y,z) are on or below line segments IK and KL that connect the following 3 points:


point I (72.0, 28.0, 0.0),


point K (48.4, 33.2, 18.4), and


point L (35.5, 27.5, 37.0);


the line segment IK is represented by coordinates (0.025z2−1.7429z+72.00, −0.025z2+0.7429z+28.00, z), and


the line segment KL is represented by coordinates (0.0098z2−1.238z+67.852, −0.0098z2+0.238z+32.148, z),


it can be determined that the refrigerant has WCF lower flammability.


For the points on the line segment IK, an approximate curve (x=0.025z2−1.7429z+72.00) was obtained from three points, i.e., I (72.0, 28.0, 0.0), J (57.7, 32.8, 9.5), and K (48.4, 33.2, 18.4) by using the least-square method to determine coordinates (x=0.025z2−1.7429z+72.00, y=100−z−x=−0.00922z2+0.2114z+32.443, z).


Likewise, for the points on the line segment KL, an approximate curve was determined from three points, i.e., K (48.4, 33.2, 18.4), Example 10 (41.1, 31.2, 27.7), and L (35.5, 27.5, 37.0) by using the least-square method to determine coordinates.


The results in Table 146 indicate that in a ternary composition diagram of a mixed refrigerant of HFO-1132(E), HFO-1123, and R32 in which their sum is 100 mass %, a line segment connecting a point (0.0, 100.0, 0.0) and a point (0.0, 0.0, 100.0) is the base, the point (0.0, 100.0, 0.0) is on the left side, and the point (0.0, 0.0, 100.0) is on the right side, when coordinates (x,y,z) are on or below line segments MP and PQ that connect the following 3 points:


point M (47.1, 52.9, 0.0),


point P (31.8, 49.8, 18.4), and


point Q (28.6, 34.4, 37.0),


it can be determined that the refrigerant has ASHRAE lower flammability.


In the above, the line segment MP is represented by coordinates (0.0083z2−0.984z+47.1, −0.0083z2−0.016z+52.9, z), and the line segment PQ is represented by coordinates (0.0135z2−0.9181z+44.133, −0.0135z2−0.0819z+55.867, z).


For the points on the line segment MP, an approximate curve was obtained from three points, i.e., points M, N, and P, by using the least-square method to determine coordinates. For the points on the line segment PQ, an approximate curve was obtained from three points, i.e., points P, U, and Q, by using the least-square method to determine coordinates.


The GWP of compositions each comprising a mixture of R410A (R32=50%/R125=50%) was evaluated based on the values stated in the Intergovernmental Panel on Climate Change (IPCC), fourth report. The GWP of HFO-1132(E), which was not stated therein, was assumed to be 1 from HFO-1132a (GWP=1 or less) and HFO-1123 (GWP=0.3, described in WO2015/141678). The refrigerating capacity of compositions each comprising R410A and a mixture of HFO-1132(E) and HFO-1123 was determined by performing theoretical refrigeration cycle calculations for the mixed refrigerants using the National Institute of Science and Technology (NIST) and Reference Fluid Thermodynamic and Transport Properties Database (Refprop 9.0) under the following conditions.


The COP ratio and the refrigerating capacity (which may be referred to as “cooling capacity” or “capacity”) ratio relative to those of R410 of the mixed refrigerants were determined. The conditions for calculation were as described below.


Evaporating temperature: 5° C.


Condensation temperature: 45° C.


Degree of superheating: 5K


Degree of subcooling: 5K


Compressor efficiency: 70%


Tables 147 to 166 show these values together with the GWP of each mixed refrigerant.

















TABLE 147








Comparative
Comparative
Comparative
Comparative
Comparative
Comparative




Comparative
Example
Example
Example
Example
Example
Example




Example
2
3
4
5
6
7


Item
Unit
1
A
B
A′
B′
A″
B″























HFO-1132(E)
mass %
R410A
90.5
0.0
81.6
0.0
63.0
0.0


HFO-1123
mass %

0.0
90.5
0.0
81.6
0.0
63.0


R32
mass %

9.5
9.5
18.4
18.4
37.0
37.0


GWP

2088
65
65
125
125
250
250


COP ratio
% (relative
100
99.1
92.0
98.7
93.4
98.7
96.1



to R410A)









Refrigerating
% (relative
100
102.2
111.6
105.3
113.7
110.0
115.4


capacity
to R410A)









ratio























TABLE 148







Comparative
Comparative



Comparative




Example
Example
Comparative
Example

Example




8
9
Example
1
Example
11


Item
Unit
O
C
10
U
2
D






















HFO-1132(E)
mass %
100.0
50.0
41.1
28.7
15.2
0.0


HFO-1123
mass %
0.0
31.6
34.6
41.2
52.7
67.0


R32
mass %
0.0
18.4
24.3
30.1
32.1
33.0


GWP

1
125
165
204
217
228


COP ratio
% (relative
99.7
96.0
96.0
96.0
96.0
96.0



to R410A)








Refrigerating
% (relative
98.3
109.9
111.7
113.5
114.8
115.4


capacity ratio
to R410A)






















TABLE 149







Comparative

Example
Example
Comparative




Example 12
Comparative
3
4
Example 14


Item
Unit
E
Example 13
T
S
F





















HFO-1132(E)
mass %
53.4
43.4
34.8
25.4
0.0


HFO-1123
mass %
46.6
47.1
51.0
56.2
74.1


R32
mass %
0.0
9.5
14.2
18.4
25.9


GWP

1
65
97
125
176


COP ratio
% (relative
94.5
94.5
94.5
94.5
94.5



to R410A)







Refrigerating
% (relative
105.6
109.2
110.8
112.3
114.8


capacity ratio
to R410A)






















TABLE 150







Comparative

Example

Comparative




Example 15
Example
6
Example
Example 16


Item
Unit
G
5
R
7
H





















HFO-1132(E)
mass %
38.5
31.5
23.1
16.9
0.0


HFO-1123
mass %
61.5
63.5
67.4
71.1
84.2


R32
mass %
0.0
5.0
9.5
12.0
15.8


GWP

1
35
65
82
107


COP ratio
% (relative
93.0
93.0
93.0
93.0
93.0



to R410A)







Refrigerating
% (relative
107.0
109.1
110.9
111.9
113.2


capacity ratio
to R410A)






















TABLE 151







Comparative



Comparative




Example 17
Example 8
Example 9
Comparative
Example 19


Item
Unit
I
J
K
Example 18
L





















HFO-1132(E)
mass %
72.0
57.7
48.4
41.1
35.5


HFO-1123
mass %
28.0
32.8
33.2
31.2
27.5


R32
mass %
0.0
9.5
18.4
27.7
37.0


GWP

1
65
125
188
250


COP ratio
% (relative to
96.6
95.8
95.9
96.4
97.1



R410A)







Refrigerating
% (relative to
103.1
107.4
110.1
112.1
113.2


capacity ratio
R410A)





















TABLE 152







Comparative
Exam-
Exam-
Exam-




Example 20
ple 10
ple 11
ple 12


Item
Unit
M
N
P
Q




















HFO-1132(E)
mass %
47.1
38.5
31.8
28.6


HFO-1123
mass %
52.9
52.1
49.8
34.4


R32
mass %
0.0
9.5
18.4
37.0


GWP

1
65
125
250


COP ratio
% (relative
93.9
94.1
94.7
96.9



to R410A)






Refrigerating
% (relative
106.2
109.7
112.0
114.1


capacity ratio
to R410A)





























TABLE 153







Comparative
Comparative
Comparative



Comparative
Comparative




Example
Example
Example
Example
Example
Example
Example
Example


Item
Unit
22
23
24
14
15
16
25
26
























HFO-
mass %
10.0
20.0
30.0
40.0
50.0
60.0
70.0
80.0


1132(E)











HFO-1123
mass %
85.0
75.0
65.0
55.0
45.0
35.0
25.0
15.0


R32
mass %
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0


GWP

35
35
35
35
35
35
35
35


COP ratio
%
91.7
92.2
92.9
93.7
94.6
95.6
96.7
97.7



(relative











to











R410A)










Refrigerating
%
110.1
109.8
109.2
108.4
107.4
106.1
104.7
103.1


capacity
(relative










ratio
to R410A)

























TABLE 154







Comparative
Comparative
Comparative



Comparative
Comparative




Example
Example
Example
Example
Example
Example
Example
Example


Item
Unit
27
28
29
17
18
19
30
31
























HFO-
mass %
90.0
10.0
20.0
30.0
40.0
50.0
60.0
70.0


1132(E)











HFO-1123
mass %
5.0
80.0
70.0
60.0
50.0
40.0
30.0
20.0


R32
mass %
5.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0


GWP

35
68
68
68
68
68
68
68


COP ratio
%
98.8
92.4
92.9
93.5
94.3
95.1
96.1
97.0



(relative











to











R410A)










Refrigerating
%
101.4
111.7
111.3
110.6
109.6
108.5
107.2
105.7


capacity
(relative










ratio
to R410A)

























TABLE 155







Comparative





Comparative
Comparative




Example
Example
Example
Example
Example
Example
Example
Example


Item
Unit
32
20
21
22
23
24
33
34
























HFO-
mass %
80.0
10.0
20.0
30.0
40.0
50.0
60.0
70.0


1132(E)











HFO-1123
mass %
10.0
75.0
65.0
55.0
45.0
35.0
25.0
15.0


R32
mass %
10.0
15.0
15.0
15.0
15.0
15.0
15.0
15.0


GWP

68
102
102
102
102
102
102
102


COP ratio
%
98.0
93.1
93.6
94.2
94.9
95.6
96.5
97.4



(relative











to R410A)










Refrigerating
%
104.1
112.9
112.4
111.6
110.6
109.4
108.1
106.6


capacity
(relative










ratio
to R410A)

























TABLE 156







Comparative
Comparative
Comparative
Comparative
Comparative
Comparative
Comparative
Comparative




Example
Example
Example
Example
Example
Example
Example
Example


Item
Unit
35
36
37
38
39
40
41
42
























HFO-
mass %
80.0
10.0
20.0
30.0
40.0
50.0
60.0
70.0


1132(E)











HFO-1123
mass %
5.0
70.0
60.0
50.0
40.0
30.0
20.0
10.0


R32
mass %
15.0
20.0
20.0
20.0
20.0
20.0
20.0
20.0


GWP

102
136
136
136
136
136
136
136


COP ratio
%
98.3
93.9
94.3
94.8
95.4
96.2
97.0
97.8



(relative











to R410A)










Refrigerating
%
105.0
113.8
113.2
112.4
111.4
110.2
108.8
107.3


capacity
(relative










ratio
to R410A)

























TABLE 157







Comparative
Comparative
Comparative
Comparative
Comparative
Comparative
Comparative
Comparative




Example
Example
Example
Example
Example
Example
Example
Example


Item
Unit
43
44
45
46
47
48
49
50
























HFO-
mass %
10.0
20.0
30.0
40.0
50.0
60.0
70.0
10.0


1132(E)











HFO-1123
mass %
65.0
55.0
45.0
35.0
25.0
15.0
5.0
60.0


R32
mass %
25.0
25.0
25.0
25.0
25.0
25.0
25.0
30.0


GWP

170
170
170
170
170
170
170
203


COP ratio
%
94.6
94.9
95.4
96.0
96.7
97.4
98.2
95.3



(relative











to











R410A)










Refrigerating
%
114.4
113.8
113.0
111.9
110.7
109.4
107.9
114.8


capacity
(relative










ratio
to R410A)

























TABLE 158







Comparative
Comparative
Comparative
Comparative
Comparative


Comparative




Example
Example
Example
Example
Example
Example
Example
Example


Item
Unit
51
52
53
54
55
25
26
56
























HFO-1132(E)
mass %
20.0
30.0
40.0
50.0
60.0
10.0
20.0
30.0


HFO-1123
mass %
50.0
40.0
30.0
20.0
10.0
55.0
45.0
35.0


R32
mass %
30.0
30.0
30.0
30.0
30.0
35.0
35.0
35.0


GWP

203
203
203
203
203
237
237
237


COP ratio
% (relative
95.6
96.0
96.6
97.2
97.9
96.0
96.3
96.6



to R410A)










Refrigerating
% (relative
114.2
113.4
112.4
111.2
109.8
115.1
114.5
113.6


capacity
to R410A)










ratio

























TABLE 159







Comparative
Comparative
Comparative
Comparative
Comparative
Comparative
Comparative
Comparative




Example
Example
Example
Example
Example
Example
Example
Example


Item
Unit
57
58
59
60
61
62
63
64
























HFO-1132(E)
mass %
40.0
50.0
60.0
10.0
20.0
30.0
40.0
50.0


HFO-1123
mass %
25.0
15.0
5.0
50.0
40.0
30.0
20.0
10.0


R32
mass %
35.0
35.0
35.0
40.0
40.0
40.0
40.0
40.0


GWP

237
237
237
271
271
271
271
271


COP ratio
% (relative to
97.1
97.7
98.3
96.6
96.9
97.2
97.7
98.2



R410A)










Refrigerating
% (relative to
112.6
111.5
110.2
115.1
114.6
113.8
112.8
111.7


capacity ratio
R410A)

























TABLE 160







Example
Example
Example
Example
Example
Example
Example
Example


Item
Unit
27
28
29
30
31
32
33
34
























HFO-1132(E)
mass %
38.0
40.0
42.0
44.0
35.0
37.0
39.0
41.0


HFO-1123
mass %
60.0
58.0
56.0
54.0
61.0
59.0
57.0
55.0


R32
mass %
2.0
2.0
2.0
2.0
4.0
4.0
4.0
4.0


GWP

14
14
14
14
28
28
28
28


COP ratio
% (relative
93.2
93.4
93.6
93.7
93.2
93.3
93.5
93.7



to R410A)










Refrigerating
% (relative
107.7
107.5
107.3
107.2
108.6
108.4
108.2
108.0


capacity ratio
to R410A)

























TABLE 161







Example
Example
Example
Example
Example
Example
Example
Example


Item
Unit
35
36
37
38
39
40
41
42
























HFO-1132(E)
mass %
43.0
31.0
33.0
35.0
37.0
39.0
41.0
27.0


HFO-1123
mass %
53.0
63.0
61.0
59.0
57.0
55.0
53.0
65.0


R32
mass %
4.0
6.0
6.0
6.0
6.0
6.0
6.0
8.0


GWP

28
41
41
41
41
41
41
55


COP ratio
% (relative
93.9
93.1
93.2
93.4
93.6
93.7
93.9
93.0



to R410A)










Refrigerating
% (relative
107.8
109.5
109.3
109.1
109.0
108.8
108.6
110.3


capacity ratio
to R410A)

























TABLE 162







Example
Example
Example
Example
Example
Example
Example
Example


Item
Unit
43
44
45
46
47
48
49
50
























HFO-1132(E)
mass %
29.0
31.0
33.0
35.0
37.0
39.0
32.0
32.0


HFO-1123
mass %
63.0
61.0
59.0
57.0
55.0
53.0
51.0
50.0


R32
mass %
8.0
8.0
8.0
8.0
8.0
8.0
17.0
18.0


GWP

55
55
55
55
55
55
116
122


COP ratio
% (relative
93.2
93.3
93.5
93.6
93.8
94.0
94.5
94.7



to R410A)










Refrigerating
% (relative
110.1
110.0
109.8
109.6
109.5
109.3
111.8
111.9


capacity ratio
to R410A)

























TABLE 163







Example
Example
Example
Example
Example
Example
Example
Example


Item
Unit
51
52
53
54
55
56
57
58
























HFO-1132(E)
mass %
30.0
27.0
21.0
23.0
25.0
27.0
11.0
13.0


HFO-1123
mass %
52.0
42.0
46.0
44.0
42.0
40.0
54.0
52.0


R32
mass %
18.0
31.0
33.0
33.0
33.0
33.0
35.0
35.0


GWP

122
210
223
223
223
223
237
237


COP ratio
% (relative
94.5
96.0
96.0
96.1
96.2
96.3
96.0
96.0



to R410A)










Refrigerating
% (relative
112.1
113.7
114.3
114.2
114.0
113.8
115.0
114.9


capacity ratio
to R410A)

























TABLE 164







Example
Example
Example
Example
Example
Example
Example
Example


Item
Unit
59
60
61
62
63
64
65
66
























HFO-1132(E)
mass %
15.0
17.0
19.0
21.0
23.0
25.0
27.0
11.0


HFO-1123
mass %
50.0
48.0
46.0
44.0
42.0
40.0
38.0
52.0


R32
mass %
35.0
35.0
35.0
35.0
35.0
35.0
35.0
37.0


GWP

237
237
237
237
237
237
237
250


COP ratio
% (relative
96.1
96.2
96.2
96.3
96.4
96.4
96.5
96.2



to R410A)










Refrigerating
% (relative
114.8
114.7
114.5
114.4
114.2
114.1
113.9
115.1


capacity ratio
to R410A)

























TABLE 165







Example
Example
Example
Example
Example
Example
Example
Example


Item
Unit
67
68
69
70
71
72
73
74
























HFO-1132(E)
mass %
13.0
15.0
17.0
15.0
17.0
19.0
21.0
23.0


HFO-1123
mass %
50.0
48.0
46.0
50.0
48.0
46.0
44.0
42.0


R32
mass %
37.0
37.0
37.0
0.0
0.0
0.0
0.0
0.0


GWP

250
250
250
237
237
237
237
237


COP ratio
% (relative
96.3
96.4
96.4
96.1
96.2
96.2
96.3
96.4



to R410A)










Refrigerating
% (relative
115.0
114.9
114.7
114.8
114.7
114.5
114.4
114.2


capacity ratio
to R410A)

























TABLE 166







Example
Example
Example
Example
Example
Example
Example
Example


Item
Unit
75
76
77
78
79
80
81
82
























HFO-1132(E)
mass %
25.0
27.0
11.0
19.0
21.0
23.0
25.0
27.0


HFO-1123
mass %
40.0
38.0
52.0
44.0
42.0
40.0
38.0
36.0


R32
mass %
0.0
0.0
0.0
37.0
37.0
37.0
37.0
37.0


GWP

237
237
250
250
250
250
250
250


COP ratio
% (relative
96.4
96.5
96.2
96.5
96.5
96.6
96.7
96.8



to R410A)










Refrigerating
% (relative
114.1
113.9
115.1
114.6
114.5
114.3
114.1
114.0


capacity ratio
to R410A)









The above results indicate that under the condition that the mass % of HFO-1132(E), HFO-1123, and R32 based on their sum is respectively represented by x, y, and z, when coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R32 is 100 mass %, a line segment connecting a point (0.0, 100.0, 0.0) and a point (0.0, 0.0, 100.0) is the base, and the point (0.0, 100.0, 0.0) is on the left side are within the range of a figure surrounded by line segments that connect the following 4 points:


point O (100.0, 0.0, 0.0),


point A″ (63.0, 0.0, 37.0),


point B″ (0.0, 63.0, 37.0), and


point (0.0, 100.0, 0.0),


or on these line segments,


the refrigerant has a GWP of 250 or less.


The results also indicate that when coordinates (x,y,z) are within the range of a figure surrounded by line segments that connect the following 4 points:


point O (100.0, 0.0, 0.0),


point A′ (81.6, 0.0, 18.4),


point B′ (0.0, 81.6, 18.4), and


point (0.0, 100.0, 0.0),


or on these line segments,


the refrigerant has a GWP of 125 or less.


The results also indicate that when coordinates (x,y,z) are within the range of a figure surrounded by line segments that connect the following 4 points:


point O (100.0, 0.0, 0.0),


point A (90.5, 0.0, 9.5),


point B (0.0, 90.5, 9.5), and


point (0.0, 100.0, 0.0),


or on these line segments,


the refrigerant has a GWP of 65 or less.


The results also indicate that when coordinates (x,y,z) are on the left side of line segments that connect the following 3 points:


point C (50.0, 31.6, 18.4),


point U (28.7, 41.2, 30.1), and


point D (52.2, 38.3, 9.5),


or on these line segments,


the refrigerant has a COP ratio of 96% or more relative to that of R410A.


In the above, the line segment CU is represented by coordinates (−0.0538z2+0.7888z+53.701, 0.0538z2−1.7888z+46.299, z), and the line segment UD is represented by coordinates (−3.4962z2+210.71z−3146.1, 3.4962z2−211.71z+3246.1, z).


The points on the line segment CU are determined from three points, i.e., point C, Comparative Example 10, and point U, by using the least-square method.


The points on the line segment UD are determined from three points, i.e., point U, Example 2, and point D, by using the least-square method.


The results also indicate that when coordinates (x,y,z) are on the left side of line segments that connect the following 3 points:


point E (55.2, 44.8, 0.0),


point T (34.8, 51.0, 14.2), and


point F (0.0, 76.7, 23.3),


or on these line segments,


the refrigerant has a COP ratio of 94.5% or more relative to that of R410A.


In the above, the line segment ET is represented by coordinates (−0.0547z2−0.5327z+53.4, 0.0547z2−0.4673z+46.6, z), and the line segment TF is represented by coordinates (−0.0982z2+0.9622z+40.931, 0.0982z2−1.9622z+59.069, z).


The points on the line segment ET are determined from three points, i.e., point E, Example 2, and point T, by using the least-square method.


The points on the line segment TF are determined from three points, i.e., points T, S, and F, by using the least-square method.


The results also indicate that when coordinates (x,y,z) are on the left side of line segments that connect the following 3 points:


point G (0.0, 76.7, 23.3),


point R (21.0, 69.5, 9.5), and


point H (0.0, 85.9, 14.1),


or on these line segments,


the refrigerant has a COP ratio of 93% or more relative to that of R410A.


In the above, the line segment GR is represented by coordinates (−0.0491z2−1.1544z+38.5, 0.0491z2+0.1544z+61.5, z), and the line segment RH is represented by coordinates (−0.3123z2+4.234z+11.06, 0.3123z2−5.234z+88.94, z).


The points on the line segment GR are determined from three points, i.e., point G, Example 5, and point R, by using the least-square method.


The points on the line segment RH are determined from three points, i.e., point R, Example 7, and point H, by using the least-square method.


In contrast, as shown in, for example, Comparative Examples 8, 9, 13, 15, 17, and 18, when R32 is not contained, the concentrations of HFO-1132(E) and HFO-1123, which have a double bond, become relatively high; this undesirably leads to deterioration, such as decomposition, or polymerization in the refrigerant compound.


(6) Configuration of Air Conditioner 1


FIG. 16 is a refrigeration circuit diagram of an air conditioner 1 in which a compressor 100 according to an embodiment of the present invention is utilized. The air conditioner 1 is a refrigeration cycle apparatus provided with the compressor 100. As examples of the air conditioner 1 in which the compressor 100 is employed, an “air conditioner dedicated to cooling-operation”, an “air conditioner dedicated to heating-operation”, an “air conditioner switchable between cooling operation and heating operation by using a four-way switching valve”, and the like are presented. Here, description will be provided using the “air conditioner switchable between cooling operation and heating operation by using a four-way switching valve”.


Referring to FIG. 16, the air conditioner 1 is provided with an indoor unit 2 and an outdoor unit 3. The indoor unit 2 and the outdoor unit 3 are connected to each other by a liquid-refrigerant connection pipe 4 and a gas-refrigerant connection pipe 5. As illustrated in FIG. 16, the air conditioner 1 is of a pair-type having the indoor unit 2 and the outdoor unit 3 one each. The air conditioner 1 is, however, not limited thereto and may be of a multi-type having a plurality of the indoor units 2.


In the air conditioner 1, devices, such as an accumulator 15, the compressor 100, a four-way switching valve 16, an outdoor heat exchanger 17, an expansion valve 18, and an indoor heat exchanger 13, are connected together by pipes, thereby constituting a refrigerant circuit 11.


In the present embodiment, a refrigerant for performing a vapor compression refrigeration cycle is packed in the refrigerant circuit 11. The refrigerant is a mixed refrigerant containing 1,2-difluoroethylene, and, as the refrigerant, any one of the aforementioned refrigerants A to E is usable. A refrigerating machine oil is also packed together with the mixed refrigerant in the refrigerant circuit 11.


(6-1) Indoor Unit 2


The indoor heat exchanger 13 to be loaded in the indoor unit 2 is a cross-fin type fin-and-tube heat exchanger constituted by a heat transfer tube and a large number of heat transfer fins. The indoor heat exchanger 13 is connected at the liquid side thereof to the liquid-refrigerant connection pipe 4 and connected at the gas side thereof to the gas-refrigerant connection pipe 5, and the indoor heat exchanger 13 functions as a refrigerant evaporator during cooling operation.


(6-2) Outdoor Unit 3


The outdoor unit 3 is loaded with the accumulator 15, the compressor 100, the outdoor heat exchanger 17, and the expansion valve 18.


(6-2-1) Outdoor Heat Exchanger 17


The outdoor heat exchanger 17 is a cross-fin type fin-and-tube heat exchanger constituted by a heat transfer tube and a large number of heat transfer fins. The outdoor heat exchanger 17 is connected at one end thereof to the side of a discharge pipe 24 in which a refrigerant discharged from the compressor 100 flows and connected at the other end thereof to the side of the liquid-refrigerant connection pipe 4. The outdoor heat exchanger 17 functions as a condenser for a gas refrigerant supplied from the compressor 100 through the discharge pipe 24.


(6-2-2) Expansion Valve 18


The expansion valve 18 is disposed in a pipe that connects the outdoor heat exchanger 17 and the liquid-refrigerant connection pipe 4 to each other. The expansion valve 18 is an opening-degree adjustable electric valve for adjusting the pressure and the flow rate of a refrigerant that flows in the pipe.


(6-2-3) Accumulator 15


The accumulator 15 is disposed in a pipe that connects the gas-refrigerant connection pipe 5 and a suction pipe 23 of the compressor 100 to each other. The accumulator 15 separates, into a gas phase and a liquid phase, a refrigerant that flows from the indoor heat exchanger 13 toward the suction pipe 23 through the gas-refrigerant connection pipe 5 to prevent a liquid refrigerant from being supplied into the compressor 100. The compressor 100 is supplied with a gas-phase refrigerant accumulated in an upper space of the accumulator 15.


(6-2-4) Compressor 100



FIG. 17 is a longitudinal sectional view of the compressor 100 according to an embodiment of the present invention. The compressor 100 in FIG. 17 is a scroll compressor. The compressor 100 compresses a refrigerant sucked through the suction pipe 23 in a compression chamber Sc and discharges the compressed refrigerant through the discharge pipe 24. Regarding the compressor 100, details will be described in the section of “(7) Configuration of Compressor 100”.


(6-2-5) Four-Way Switching Valve 16


The four-way switching valve 16 has first to fourth ports. The four-way switching valve 16 is connected at the first port thereof to the discharge side of the compressor 100, connected at the second port thereof to the suction side of the compressor 100, connected at the third port thereof to the gas-side end portion of the outdoor heat exchanger 17, and connected at the fourth port thereof to a gas-side shutoff valve Vg.


The four-way switching valve 16 is switchable between a first state (the state indicated in the solid line in FIG. 16) and a second state (the state indicated by the dashed line in FIG. 16). In the four-way switching valve 16 in the first state, a first port and a third port are in communication with each other, and a second port and a fourth port are in communication with each other. In the four-way switching valve 16 in the second state, the first port and the fourth port are in communication with each other, and the second port and the third port are in communication with each other.


(7) Configuration of Compressor 100

A compressor 100 constitutes a refrigerant circuit in cooperation with an evaporator, a condenser, an expansion mechanism, and the like and plays a role of compressing a gas refrigerant in the refrigerant circuit. As illustrated in FIG. 17, the compressor 100 is constituted by, mainly, a casing 20 of a hermetically closed dome type having a vertically-elongated cylindrical shape, a motor 70, a compression mechanism 60, an oldham ring 39, a lower bearing 90, a suction pipe 23, and a discharge pipe 24.


(7-1) Casing 20


The casing 20 has a substantially cylindrical cylinder member 21, a bowl-shaped upper cover 22a welded to an upper end portion of the cylinder member 21 in an airtight manner, and a bowl-shaped lower cover 22b welded to a lower end portion of the cylinder member 21 in an airtight manner.


The casing 20 accommodates, mainly, the compression mechanism 60 that compresses a gas refrigerant and the motor 70 that is disposed on the lower side of the compression mechanism 60. The compression mechanism 60 and the motor 70 are coupled to each other by a crank shaft 80 disposed to extend in an up-down direction in the casing 20. A gap space 68 is generated between the compression mechanism 60 and the motor 70.


An oil reservoir space So is formed in a lower portion of the casing 20. The oil reservoir space So stores a refrigerating machine oil O for lubricating the compression mechanism 60 and the like. The refrigerating machine oil O is the refrigerating machine oil described in the section of “(4-1) Refrigerating Machine Oil”.


In the inner portion of the crank shaft 80, an oil supply path 83 for supplying the refrigerating machine oil O to the compression mechanism 60 and the like is formed. The lower end of a main shaft 82 of the crank shaft 80 is positioned in the oil reservoir space So formed in the lower portion of the casing 20. The refrigerating machine oil O in the oil reservoir space So is supplied to the compression mechanism 60 and the like through the oil supply path 83.


(7-2) Motor 70


The motor 70 is an induction motor and constituted by an annular stator 72 fixed to the inner wall surface of the casing 20, and a rotor 71 rotatably accommodated inside the stator 72 with a slight gap (air gap).


The motor 70 is disposed such that the upper end of a coil end of a coil 727 formed on the upper side of the stator 72 is at a height position substantially identical to the height position of the lower end of a bearing portion 61b of a housing 61.


A copper wire is wound around each tooth portion of the stator 72, and coil ends of the coil 727 are formed on the upper side and the lower side.


The rotor 71 is drive-coupled to a movable scroll 40 of the compression mechanism 60 via the crank shaft 80 disposed at the axial center of the cylinder member 21 so as to extend in the up-down direction. In addition, a guide plate 58 that guides a refrigerant that has flowed out through an outlet 49 of a connection passage 46 to a motor cooling passage 55 is formed in the gap space 68.


The stator 72 is a so-called distributed-winding stator and has a barrel portion 725, which is an iron core, and the coil 727 wound around the barrel portion 725. A narrow portion 727a, which is a narrow portion of the coil 727, recessed inward more than the outer circumferential surface of the barrel portion 725 is formed on each of an upper portion and a lower portion of the barrel portion 725.


Details of the motor 70 will be described in the section of “(9) Configuration of Motor 70”.


(7-3) Compression Mechanism 60


As illustrated in FIG. 17, the compression mechanism 60 is constituted by, mainly, the housing 61, a fixed scroll 30 disposed in close contact with the upper side of the housing 61, and the movable scroll 40 that engages the fixed scroll 30.


(7-3-1) Fixed Scroll 30


As illustrated in FIG. 17, the fixed scroll 30 is constituted by, mainly, an end plate 34 and a spiral (involute) lap 33 formed on the lower surface of the end plate 34.


A discharge hole 341 in communication with a compression chamber Sc and an extended concave portion 342 in communication with the discharge hole 341 are formed in the end plate 34. The discharge hole 341 is formed in a center portion of the end plate 34 to extend in the up-down direction.


The extended concave portion 342 is constituted by a concave portion extending horizontally on the upper surface of the end plate 34. A cover body 344 is fastened and fixed by a bolt 344a to the upper surface of the fixed scroll 30 so as to close the extended concave portion 342. As a result of the extended concave portion 342 being covered by the cover body 344, a muffler space 345 constituted by an expansion chamber that muffles an operation sound of the compression mechanism 60 is formed.


(7-3-2) Movable Scroll 40


As illustrated in FIG. 17, the movable scroll 40 is constituted by, mainly, an end plate 41, a spiral (involute) lap 42 formed on the upper surface of the end plate 41, and a boss portion 43 formed on the lower surface of the end plate 41.


The movable scroll 40 is a movable scroll of an outer drive. In other words, the movable scroll 40 has the boss portion 43 that is fitted on the outer side of the crank shaft 80.


The movable scroll 40 is supported by the housing 61 by the oldham ring 39 being filled into a groove portion formed in the end plate 41. The upper end of the crank shaft 80 is fitted into the boss portion 43. The movable scroll 40 revolves in the housing 61, without being rotated by the rotation of the crank shaft 80, by being thus incorporated in the compression mechanism 60. The lap 42 of the movable scroll 40 is engaged with the lap 33 of the fixed scroll 30, and the compression chamber Sc is formed between contact parts of the two laps 33 and 42. In the compression chamber Sc, the capacity of a gap between the two laps 33 and 42 contracts toward the center in response to the revolution of the movable scroll 40. It is thereby possible to compress a gas refrigerant.


(7-3-3) Housing 61


The housing 61 is press-fitted and fixed, at the entirety of the outer circumferential surface thereof in the circumferential direction, to the cylinder member 21. In other words, the cylinder member 21 and the housing 61 are in close contact with each other over the whole circumference in an airtight manner. Consequently, the inner portion of the casing 20 is divided into a high-pressure space on the lower side of the housing 61 and a low-pressure space on the upper side of the housing 61. In the housing 61, a housing concave portion 61a recessed at the center of the upper surface thereof and the bearing portion 61b extending from the center of the lower surface thereof on the lower side are formed. The bearing portion 61b has a bearing hole 63 formed to pass therethrough in the up-down direction, and the crank shaft 80 is rotatably fitted into the bearing portion 61b through the bearing hole 63.


(7-4) Oldham Ring 39


The oldham ring 39 is a member for preventing the rotation movement of the movable scroll 40 and is fitted into an oldham groove (not illustrated) formed in the housing 61. The oldham groove is an elongated-circular groove and is disposed at positions opposite each other in the housing 61.


(7-5) Lower Bearing 90


The lower bearing 90 is disposed in a lower space on the lower side of the motor 70. The lower bearing 90 is fixed to the cylinder member 21 while constituting the lower-end-side bearing of the crank shaft 80 and supports the crank shaft 80.


(7-6) Suction Pipe 23


The suction pipe 23 is a pipe for guiding a refrigerant of the refrigerant circuit to the compression mechanism 60 and is fitted into the upper cover 22a of the casing 20 in an airtight manner. The suction pipe 23 passes through a low-pressure space Sl in the up-down direction with an inner end portion thereof fitted into the fixed scroll 30.


(7-7) Discharge Pipe 24


The discharge pipe 24 is a pipe for discharging a refrigerant in the casing 20 to the outside of the casing 20 and is fitted into the cylinder member 21 of the casing 20 in an airtight manner. The discharge pipe 24 has an inner end portion 36 that has a cylindrical shape extending in the up-down direction and that is fixed to a lower end portion of the housing 61. An inner end opening, that is, an inflow port of the discharge pipe 24 opens downward.


(8) Operation of Compressor 100

When the motor 70 is driven, the crank shaft 80 rotates, and the movable scroll 40 performs revolving operation without rotating. A low-pressure gas refrigerant is then sucked from the peripheral side of the compression chamber Sc through the suction pipe 23 into the compression chamber Sc and compressed in response to a change in the capacity of the compression chamber Sc, thereby becoming a high-pressure gas refrigerant.


The high-pressure gas refrigerant is discharged from a center portion of the compression chamber Sc by passing through the discharge hole 341 into the muffler space 345, then flows out into the gap space 68 through the connection passage 46, a scroll-side passage 47, a housing-side passage 48, and the outlet 49, and flows downward between the guide plate 58 and the inner surface of the cylinder member 21.


When the gas refrigerant flows downward between the guide plate 58 and the inner surface of the cylinder member 21, a portion of the gas refrigerant branches to flow between the guide plate 58 and the motor 70 in the circumferential direction. At this time, a lubrication oil mixed in the gas refrigerant is separated.


The other portion of the branched gas refrigerant flows downward in the motor cooling passage 55 and, after flowing into a motor lower space, turns and flows upward in an air-gap passage between the stator 72 and the rotor 71 or in the motor cooling passage 55 on a side (left side in FIG. 17) opposite the connection passage 46.


After that, the gas refrigerant that has passed the guide plate 58 and the gas refrigerant that has flowed in the air-gap passage or in the motor cooling passage 55 merge together in the gap space 68, flow into the discharge pipe 24 from the inner end portion 36 of the discharge pipe 24, and are discharged to the outside of the casing 20.


After circulating in the refrigerant circuit, the gas refrigerant discharged to the outside of the casing 20 is sucked through the suction pipe 23 and compressed again by the compression mechanism 60.


(9) Configuration of Motor 70


FIG. 18 is a sectional view of the motor 70 sectioned along a plane perpendicular to the axis. FIG. 19 is a sectional view of the rotor 71 sectioned along a plane perpendicular to the axis. FIG. 20 is a perspective view of the rotor 71.


In FIG. 18 to FIG. 20, illustration of a shaft that is coupled to the rotor 71 to transmit a rotational force to an external portion is omitted. The motor 70 in FIG. 18 to FIG. 20 is an induction motor. The motor 70 has the rotor 71 and the stator 72.


(9-1) Stator 72


The stator 72 is provided with the barrel portion 725 and a plurality of tooth portions 726. The barrel portion 725 has a substantially cylindrical shape having an inner circumferential diameter larger than the outer circumferential diameter of the rotor 71. The barrel portion 725 is formed by machining each of thin electromagnetic steel plates having a thickness of 0.05 mm or more and 0.5 mm or less into a predetermined shape and laminating a predetermined number of the electromagnetic steel plates.


The plurality of tooth portions 726 project on the inner circumferential part of the barrel portion 725 in a form of being positioned at substantially equal intervals in the circumferential direction thereof. Each of the tooth portions 726 extend from the inner circumferential part of the barrel portion 725 toward the center in the radial direction of a circle centered on the axis and faces the rotor 71 with a predetermined gap.


The tooth portions 726 are magnetically coupled on the outer circumferential side via the barrel portion 725. The coil 727 is wound, as a coil, around each of the tooth portions 726 (only one of the coils 727 is illustrated in FIG. 18). Three-phase alternating current for generating a rotating magnetic field that rotates the rotor 71 is made to flow through the coils 727. The winding type of the coils 727 is not limited and may be wound with respect to the plurality of tooth portions 726 in a concentrated form or in a distributed form.


The rotor 71 and the stator 72 are incorporated in the casing 20 and used as a rotary electric machine.


(9-2) Rotor 71


The rotor 71 is a basket-shaped rotor. The rotor 71 has a substantially cylindrical external shape and has a center axis along which the main shaft 82 of the crank shaft 80 is coupled and fixed. The rotor 71 has a rotor core 710, a plurality of conducting bars 716, and an end ring 717.


(9-2-1) Rotor Core 710


The rotor core 710 is formed of a magnetic material into a substantially cylindrical shape. The rotor core 710 is formed by machining each of thin electromagnetic steel plates having a thickness of 0.05 mm or more and 0.5 mm or less into a predetermined shape and laminating, as illustrated in FIG. 20, a predetermined number of the electromagnetic steel plates.


The electromagnetic steel plates are desirably a plurality of electromagnetic steel plates each having a tensile strength of 400 MPa or more to improve durability of the rotor during high-speed rotation. As illustrated in FIG. 19, the rotor core 710 has a plurality of conducting-bar formation holes 718 and a shaft insertion hole 719.


In each one of electromagnetic steel plates 711, a [hole having a planar shape identical to that of the shaft insertion hole 719] is formed at the center thereof, and in addition, [holes each having a planar shape identical to those of the conducting-bar formation holes 718] are provided at predetermined intervals. As a result of the electromagnetic steel plates 711 being laminated in a state in which the [holes each having the planar shape identical to those of the conducting-bar formation holes 718] are displaced from each other by a predetermined angle, the conducting-bar formation holes 718 and the shaft insertion hole 719 are formed. The conducting-bar formation holes 718 are holes for molding the conducting bars 716 in the rotor core 710. Note that FIG. 20 only illustrates some of the conducting bars 716 and some of the conducting-bar formation holes 718.


The shaft insertion hole 719 is a hole for fixing the main shaft 82 (refer to FIG. 17) of the crank shaft 80 along the center axis of the rotor core 710.


(9-2-2) Conducting Bar 716 and End Ring 717


The conducting bars 716 packed in the conducting-bar formation holes 718 and the end ring 717 that holds the rotor core 710 from both ends are molded integrally. For example, when aluminum or an aluminum alloy is employed as a conductor, the conducting bars 716 and the end ring 717 are integrally molded by, after setting the rotor core 710 in an aluminum die-casting die, press-fitting the aluminum or the aluminum alloy that has melted into the die.


Consequently, the basket-shaped rotor 71 having the plurality of conducting bars 716 disposed in an annular form and the end ring 717 that short-circuits the plurality of conducting bars 716 at an end portion in the axial direction is realized.


(10) Feature

The compressor 100 is a compressor that compresses a mixed refrigerant containing at least 1,2-difluoroethylene and that enables high power at comparatively low costs by employing the induction motor 70.


(11) Modifications

(11-1) First Modification


In the aforementioned embodiment, the conducting bars 716 and the end ring 717 have been described in a form in which the conducting bars 716 and the end ring 717 are integrally molded with aluminum or an aluminum alloy. The conducting bars 716 and the end ring 717 are, however, not limited thereto.


For example, the conducting bars 716 and the end ring 717 may be molded with a metal whose electric resistance is lower than that of aluminum. Specifically, the conducting bars 716 and the end ring 717 may be molded with copper or a copper alloy.


According to a first modification, heat generation due to current that flows through the conducting bars 716 of the induction motor 70 is suppressed, which enables high power of the compressor 100.


In cases of being molded with copper and a copper alloy, it is not possible to mold the conducting bars 716 and the end ring 717 by a die-casting method. The conducting bars 716 and the end ring 717 are thus welded by brazing.


Needless to say, the conducting bars 716 and the end ring 717 may be molded with metals of different types. For example, the conducting bars 716 may be molded with copper or a copper alloy while the end ring 717 may be molded with aluminum or an aluminum alloy.


(11-2) Second Modification



FIG. 21 is a perspective view of the rotor 71 to be used in the induction motor 70 of the compressor 100 according to a second modification. The rotor 71 in FIG. 21 has a heat sink 717a as a heat-radiation structure.


The heat sink 717a has heat-radiation fins 717af projecting from an end surface of the end ring 717 in the direction of the center axis of the rotor 71 and extending in the radius direction of the rotor 71. In the present modification, six heat-radiation fins 717af are disposed around the center axis at center-angle 60° intervals.


In the compressor 100, the rotation of the rotor 71 rotates the heat sink 717a, and heat radiation properties of the heat-radiation fins 717af are thus improved, and, moreover, the rotation causes forced convection and suppresses an increase in the peripheral temperature, which enables high power of the compressor 100.


In addition, it is possible to suppress an increase in manufacturing costs because the heat sink 717a is formed on the end ring 717, and the heat sink 717a can be molded integrally with the end ring 717 when the end ring 717 is molded.


(11-3) Third Modification



FIG. 22 is a refrigerant circuit diagram of an air conditioner 1 in which the compressor 100 according to a third modification is utilized. The configuration in FIG. 22 differs from the configuration in FIG. 16 in terms of that a refrigerant circuit 11 has a cooling structure that includes a branch circuit 110 and is identical to that in FIG. 16 in other features.


In the branch circuit 110, a refrigerant that has branched from the refrigerant circuit 11 flows. The branch circuit 110 is provided in parallel from a portion between an outdoor heat exchanger 17 and an expansion valve 18 of the refrigerant circuit 11 to a portion between the expansion valve 18 and an indoor heat exchanger 13. A second expansion valve 112, a cooling portion 111, and a third expansion valve 113 are connected to the branch circuit 110.


The cooling portion 111 is mounted on the outer circumferential surface of the casing 20 of the compressor 100 via a heat transfer plate. The mounted position thereof corresponds to the side of the stator 72 of the induction motor 70. The cooling portion 111 is a portion that cools the stator 72 indirectly by using the cold heat of the refrigerant flowing in the refrigerant circuit 11. Specifically, the second expansion valve 112 is connected to one end of a pipe fitted, in a state of being bent in a serpentine shape, into the heat transfer plate, and the third expansion valve 113 is connected to the other end thereof.


During cooling operation, a portion of the refrigerant flowing in the refrigerant circuit 11 branches at a portion between the outdoor heat exchanger 17 and the expansion valve 18 into the branch circuit 110, flows through the second expansion valve 112 whose opening degree has been adjusted, the cooling portion 111, and the third expansion valve 113 whose opening degree has been set to be fully open, in this order, and merges at a portion between the expansion valve 18 and the indoor heat exchanger 13. The opening degree of the second expansion valve 112 is adjusted so as to enable the refrigerant decompressed in the second expansion valve 112 to absorb heat in the cooling portion 111 and evaporate.


During heating operation, a portion of the refrigerant flowing in the refrigerant circuit 11 branches at a portion between the indoor heat exchanger 13 and the expansion valve 18 into the branch circuit 110, flows through the third expansion valve 113 whose opening degree has been adjusted, the cooling portion 111, and the second expansion valve 112 whose opening degree has been set to be fully open, in this order, and merges at a portion between the expansion valve 18 and the outdoor heat exchanger 17. The opening degree of the third expansion valve 113 is adjusted to enable the refrigerant decompressed in the third expansion valve 113 to absorb heat in the cooling portion 111 and evaporate.


With the aforementioned cooling structure, it is possible to cool the stator 72 by using the cold heat of the refrigerant that flows in the refrigerant circuit 11, which enables high power of the compressor.


(12) Configuration of Compressor 300 According to Second Embodiment

In the first embodiment, a scroll compressor has been described as the compressor 100. The compressor is, however, not limited to a scroll compressor.



FIG. 23 is a longitudinal sectional view of the compressor 300 according to a second embodiment of the present disclosure. The compressor 300 in FIG. 23 is a rotary compressor. The compressor 300 constitutes a portion of a refrigerant circuit in which one of the aforementioned refrigerants A to E circulates. The compressor 300 compresses a refrigerant and discharges a high-pressure gas refrigerant. The arrows in FIG. 23 indicate the flow of the refrigerant.


(12-1) Casing 220


The compressor 300 has a vertically elongated cylindrical casing 220. The casing 220 has a substantially cylindrical cylinder member 221 that opens upward and downward, and an upper cover 222a and a lower cover 222b that are disposed on the upper end and the lower end of the cylinder member 221, respectively. The upper cover 222a and the lower cover 222b are fixed to the cylinder member 221 by welding to maintain airtightness.


The casing 220 accommodates constituent devices of the compressor 300, including a compression mechanism 260, a motor 270, a crank shaft 280, an upper bearing 263, and a lower bearing 290. The oil reservoir space So is formed in a lower portion of the casing 220.


In the lower portion of the casing 220, a suction pipe 223 that sucks a gas refrigerant and supplies the gas refrigerant to the compression mechanism 260 is disposed to pass through a lower portion of the cylinder member 221. One end of the suction pipe 223 is connected to a cylinder 230 of the compression mechanism 260. The suction pipe 223 is in communication with the compression chamber Sc of the compression mechanism 260. In the suction pipe 223, a low-pressure refrigerant of the refrigeration cycle before compression by the compressor 300 flows.


The upper cover 222a of the casing 220 is provided with a discharge pipe 224 through which a refrigerant that is to be discharged to the outside of the casing 220 passes. Specifically, an end portion of the discharge pipe 224 in the inner portion of the casing 220 is disposed in a high-pressure space 51 formed in the upper side of the motor 270. In the discharge pipe 224, a high-pressure refrigerant of the refrigeration cycle after compression by the compression mechanism 260 flows.


(12-2) Motor 270


The motor 270 has a stator 272 and a rotor 271. Except for being used in the compressor 300, which is a rotary compressor, the motor 270 is basically equivalent to the motor 70 of the first embodiment and exerts performance and actions/effects equivalent to those of the motor 70 of the first embodiment. Therefore, description of the motor 270 is omitted here.


(12-3) Crank Shaft 280, Upper Bearing 263, and Lower Bearing 290


The crank shaft 280 is fixed to the rotor 271. Further, the crank shaft 280 is supported by the upper bearing 263 and the lower bearing 290 to be rotatable about a rotation axis Rs. The crank shaft 280 has an eccentric portion 241.


(12-4) Compression Mechanism 260


The compression mechanism 260 has the single cylinder 230 and a single piston 242 disposed in the cylinder 230. The cylinder 230 has a predetermined capacity and is fixed to the casing 220.


The piston 242 is disposed on the eccentric portion 241 of the crank shaft 280. The cylinder 230 and the piston 242 define the compression chamber Sc. Rotation of the rotor 271 revolves the piston 242 via the eccentric portion 241. In response to the revolution, the capacity of the compression chamber Sc changes, thereby compressing a gaseous refrigerant.


Here, “the capacity of the cylinder” means so-called theoretical capacity and, in other words, corresponds to the volume of a gaseous refrigerant sucked into the cylinder 230 through the suction pipe 223 during one rotation of the piston 242.


(12-5) Oil Reservoir Space So


The oil reservoir space So is disposed in a lower portion of the casing 220. The oil reservoir space So stores the refrigerating machine oil O for lubricating the compression mechanism 260. The refrigerating machine oil O is the refrigerating machine oil described in the section of “(4-1) Refrigerating Machine Oil”.


(13) Operation of Compressor 300

Operation of the compressor 300 will be described. When the motor 270 is started, the rotor 271 rotates with respect to the stator 272, and the crank shaft 280 fixed to the rotor 271 rotates. When the crank shaft 280 rotates, the piston 242 coupled to the crank shaft 280 revolves with respect to the cylinder 230. Then, a low-pressure gas refrigerant of the refrigeration cycle is sucked into the compression chamber Sc through the suction pipe 223. As a result of the piston 242 revolving, the suction pipe 223 and the compression chamber Sc become not in communication with each other, and in response to the capacity of the compression chamber Sc decreasing, the pressure in the compression chamber Sc starts to increase.


The refrigerant in the compression chamber Sc is compressed in response to the capacity of the compression chamber Sc decreasing and eventually becomes a high-pressure gas refrigerant. The high-pressure gas refrigerant is discharged through a discharge port 232a. Then, the high-pressure gas refrigerant passes through a gap between the stator 272 and the rotor 271 and other parts and is discharged through the discharge pipe 224 disposed in the upper side of the casing 220.


(14) Features of Second Embodiment

(14-1)


The compressor 300 is a compressor that compresses a mixed refrigerant containing at least 1,2-difluoroethylene and that enables high power at comparatively low costs by employing an induction motor as the motor 270.


(14-2)


When using the compressor 300, which is a rotary compressor, as the compressor of the air conditioner 1, it is possible to reduce the packed amount of refrigerant compared with when a scroll compressor is used. Therefore, the compressor 300 is suitable for an air conditioner that uses a flammable refrigerant.


(15) Modification of Second Embodiment

Due to the compressor 300 employing the motor 270 equivalent to the motor 70 of the first embodiment, the modification is applicable to all described in “(11) Modifications” of the first embodiment.


(16) Other Embodiment

Regarding the form of the compressor, a screw compressor or a turbo compressor may be employed provided that a motor equivalent to the motor 70 is used.


Although embodiments of the present disclosure have been described above, it should be understood that various changes in the forms and the details are possible without deviating from the spirit and the scope of the present disclosure described in the claims.


REFERENCE SIGNS LIST






    • 11 refrigerant circuit


    • 60 compression unit


    • 70 induction motor


    • 71 rotor


    • 72 stator


    • 100 compressor


    • 260 compression unit


    • 270 induction motor


    • 271 rotor


    • 272 stator


    • 300 compressor


    • 716 conducting bar


    • 717 end ring


    • 717
      a heat sink (heat-radiation structure)


    • 717
      af heat-radiation fin (heat-radiation structure)


    • 110 branch circuit (cooling structure)


    • 111 cooling portion (cooling structure)


    • 112 second expansion valve (cooling structure)


    • 113 third expansion valve (cooling structure)





CITATION LIST
Patent Literature

PTL 1: Japanese Unexamined Patent Application Publication No. 2013-124848

Claims
  • 1. A compressor comprising: a compression unit that compresses a refrigerant containing at least 1,2-difluoroethylene; andan induction motor that drives the compression unit.
  • 2. The compressor according to claim 1, wherein a rotor of the induction motor has a plurality of conducting bars that are bar-shaped conductors and that are disposed in an annular form, andan end ring that short-circuits the plurality of conducting bars at an end portion in an axial direction, andat least the conducting bars are formed of a metal whose electric resistance is lower than electric resistance of aluminum.
  • 3. The compressor according to claim 1, wherein a rotor of the induction motor has a heat-radiation structure.
  • 4. The compressor according to claim 3, wherein the rotor of the induction motor has a plurality of conducting bars that are bar-shaped conductors and that are disposed in an annular form, andan end ring that short-circuits the plurality of conducting bars at an end portion in an axial direction, andthe heat-radiation structure is formed on the end ring.
  • 5. The compressor according to claim 3d, wherein the heat-radiation structure is a heat sink.
  • 6. The compressor according to claim 1, further comprising: a cooling structure that cools a stator of the induction motor by a refrigerant.
  • 7. The compressor according to claim 6, wherein the cooling structure cools the stator by cool heat of a refrigerant that flows in a refrigerant circuit to which the compressor is connected.
  • 8. The compressor according to claim 1, whereinthe refrigerant comprises trans-1,2-difluoroethylene (HFO-1132(E)), trifluoroethylene (HFO-1123), and 2,3,3,3-tetrafluoro-1-propene (R1234yf).
  • 9. The compressor according to claim 8, whereinwhen the mass % of HFO-1132(E), HFO-1123, and R1234yf based on their sum in the refrigerant is respectively represented by x, y, and z, coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R1234yf is 100 mass % are within the range of a figure surrounded by line segments AA′, A′B, BD, DC′, C′C, CO, and OA that connect the following 7 points:
  • 10. The compressor according to claim 8, whereinwhen the mass % of HFO-1132(E), HFO-1123, and R1234yf based on their sum in the refrigerant is respectively represented by x, y, and z, coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R1234yf is 100 mass % are within the range of a figure surrounded by line segments GI, IA, AA′, A′B, BD, DC′, C′C, and CG that connect the following 8 points:
  • 11. The compressor according to claim 8, whereinwhen the mass % of HFO-1132(E), HFO-1123, and R1234yf based on their sum in the refrigerant is respectively represented by x, y, and z, coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R1234yf is 100 mass % are within the range of a figure surrounded by line segments JP, PN, NK, KA′, A′B, BD, DC′, C′C, and CJ that connect the following 9 points:
  • 12. The compressor according to claim 8, whereinwhen the mass % of HFO-1132(E), HFO-1123, and R1234yf based on their sum in the refrigerant is respectively represented by x, y, and z, coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R1234yf is 100 mass % are within the range of a figure surrounded by line segments JP, PL, LM, MA′, A′B, BD, DC′, C′C, and CJ that connect the following 9 points:
  • 13. The compressor according to claim 8, whereinwhen the mass % of HFO-1132(E), HFO-1123, and R1234yf based on their sum in the refrigerant is respectively represented by x, y, and z, coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R1234yf is 100 mass % are within the range of a figure surrounded by line segments PL, LM, MA′, A′B, BF, FT, and TP that connect the following 7 points:
  • 14. The compressor according to claim 8, whereinwhen the mass % of HFO-1132(E), HFO-1123, and R1234yf based on their sum in the refrigerant is respectively represented by x, y, and z, coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R1234yf is 100 mass % are within the range of a figure surrounded by line segments PL, LQ, QR, and RP that connect the following 4 points:
  • 15. The compressor according to claim 8, whereinwhen the mass % of HFO-1132(E), HFO-1123, and R1234yf based on their sum in the refrigerant is respectively represented by x, y, and z, coordinates (x,y,z) in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R1234yf is 100 mass % are within the range of a figure surrounded by line segments SM, MA′, A′B, BF, FT, and TS that connect the following 6 points:
  • 16. The compressor according to claim 1, whereinthe refrigerant comprises trans-1,2-difluoroethylene (HFO-1132(E)) and trifluoroethylene (HFO-1123) in a total amount of 99.5 mass % or more based on the entire refrigerant, andthe refrigerant comprises 62.0 mass % to 72.0 mass % of HFO-1132(E) based on the entire refrigerant.
  • 17. The compressor according to claim 1, whereinthe refrigerant comprises trans-1,2-difluoroethylene (HFO-1132(E)), and trifluoroethylene (HFO-1123), in a total amount of 99.5 mass % or more based on the entire refrigerant, andthe refrigerant comprises 45.1 mass % to 47.1 mass % of HFO-1132(E) based on the entire refrigerant.
  • 18. The compressor according to claim 1, whereinthe refrigerant comprises trans-1,2-difluoroethylene (HFO-1132(E)), trifluoroethylene (HFO-1123), 2,3,3,3-tetrafluoro-1-propene (R1234yf), and difluoromethane (R32),
  • 19. The compressor according to claim 1, whereinthe refrigerant comprises trans-1,2-difluoroethylene (HFO-1132(E)), trifluoroethylene (HFO-1123), 2,3,3,3-tetrafluoro-1-propene (R1234yf), and difluoromethane (R32),
  • 20. The compressor according to claim 1, whereinthe refrigerant comprises trans-1,2-difluoroethylene (HFO-1132(E)), difluoromethane (R32), and 2,3,3,3-tetrafluoro-1-propene (R1234yf),
  • 21. The compressor according to claim 1, whereinthe refrigerant comprises trans-1,2-difluoroethylene (HFO-1132(E)), difluoromethane (R32), and 2,3,3,3-tetrafluoro-1-propene (R1234yf),
  • 22. The compressor according to claim 1, whereinthe refrigerant comprises trans-1,2-difluoroethylene (HFO-1132(E)), difluoromethane (R32), and 2,3,3,3-tetrafluoro-1-propene (R1234yf),
  • 23. The compressor according to claim 1, whereinthe refrigerant comprises trans-1,2-difluoroethylene (HFO-1132(E)), difluoromethane (R32), and 2,3,3,3-tetrafluoro-1-propene (R1234yf),
  • 24. The compressor according to claim 1, whereinthe refrigerant comprises trans-1,2-difluoroethylene (HFO-1132(E)), difluoromethane (R32), and 2,3,3,3-tetrafluoro-1-propene (R1234yf),
  • 25. The compressor according to claim 1, whereinthe refrigerant comprises trans-1,2-difluoroethylene (HFO-1132(E)), trifluoroethylene (HFO-1123), and difluoromethane (R32),
  • 26. The compressor according to claim 1, whereinthe refrigerant comprises trans-1,2-difluoroethylene (HFO-1132(E)), trifluoroethylene (HFO-1123), and difluoromethane (R32),
  • 27. The compressor according to claim 1, whereinthe refrigerant comprises trans-1,2-difluoroethylene (HFO-1132(E)), trifluoroethylene (HFO-1123), and difluoromethane (R32),
  • 28. The compressor according to claim 1, whereinthe refrigerant comprises trans-1,2-difluoroethylene (HFO-1132(E)), trifluoroethylene (HFO-1123), and difluoromethane (R32),
  • 29. The compressor according to claim 1, whereinthe refrigerant comprises trans-1,2-difluoroethylene (HFO-1132(E)), trifluoroethylene (HFO-1123), and difluoromethane (R32),
  • 30. The compressor according to claim 1, whereinthe refrigerant comprises trans-1,2-difluoroethylene (HFO-1132(E)), trifluoroethylene (HFO-1123), and difluoromethane (R32),
  • 31. A refrigeration cycle apparatus comprising the compressor according to claim 1.
Priority Claims (9)
Number Date Country Kind
2017-242183 Dec 2017 JP national
2017-242185 Dec 2017 JP national
2017-242186 Dec 2017 JP national
2017-242187 Dec 2017 JP national
PCT/JP2018/037483 Oct 2018 JP national
PCT/JP2018/038746 Oct 2018 JP national
PCT/JP2018/038747 Oct 2018 JP national
PCT/JP2018/038748 Oct 2018 JP national
PCT/JP2018/038749 Oct 2018 JP national
Continuation in Parts (1)
Number Date Country
Parent 16772976 US
Child 16913448 US