Air conditioning apparatus

Information

  • Patent Grant
  • 11441802
  • Patent Number
    11,441,802
  • Date Filed
    Friday, June 26, 2020
    3 years ago
  • Date Issued
    Tuesday, September 13, 2022
    a year ago
Abstract
An air conditioning apparatus 1 includes a compressor (321), an indoor heat exchanger (242) that is a use-side heat exchanger that exchanges heat with first air (F1), an outdoor heat exchanger (323) that is a heat-source-side heat exchanger that exchanges heat with second air, a refrigerant, a first duct (209), and a casing (230). The refrigerant contains at least 1,2-difluoroethylene, and circulates in the compressor (321), the indoor heat exchanger (242), and the outdoor heat exchanger (323) to repeat a refrigeration cycle. The first duct (209) supplies the first air (F1) to a plurality of rooms in an interior. The casing (230) includes a use-side space (SP2) that is connected to the first duct (209) and that accommodates the indoor heat exchanger (242). The casing (230) is configured to allow the first air (F1) after heat exchange with the refrigerant at the indoor heat exchanger (242) to be sent out to the first duct (209).
Description
TECHNICAL FIELD

The present disclosure relates to an air conditioning apparatus.


BACKGROUND ART

Hitherto, as an air conditioning apparatus that air-conditions a plurality of rooms in an interior by one air conditioning apparatus, for example, a multi-type air conditioning apparatus that is described in Japanese Literature 1 (Japanese Unexamined Patent Application Publication No. 2018-25377) has been known.


SUMMARY OF THE INVENTION
Technical Problem

A multi-type air conditioning apparatus such as the multi-type air conditioning apparatus that is described in Japanese Literature 1 includes a first indoor unit and a second indoor unit that are disposed in different rooms. In such an air conditioning apparatus, since a refrigerant is caused to circulate in the first indoor unit and the second indoor unit, the amount of refrigerant with which the air conditioning apparatus is filled is large.


An air conditioning apparatus that air-conditions a plurality of rooms in an interior has a problem in that the amount of refrigerant with which the air conditioning apparatus needs to be reduced.


Solution to Problem

An air conditioning apparatus according to a first aspect includes a compressor, a use-side heat exchanger that exchanges heat with first air, a heat-source-side heat exchanger that exchanges heat with second air, a refrigerant that contains at least 1,2-difluoroethylene and that circulates in the compressor, the use-side heat exchanger, and the heat-source-side heat exchanger to repeat a refrigeration cycle, a first duct that supplies the first air to a plurality of rooms in an interior, and a casing that includes a use-side space that is connected to the first duct and that accommodates the use-side heat exchanger, the casing being configured to allow the first air after heat exchange with the refrigerant at the use-side heat exchanger to be sent out to the first duct.


Since the number of indoor-side heat exchangers of this air conditioning apparatus is smaller than the number of indoor-side heat exchangers of air conditioning apparatus in which a plurality of indoor units are disposed in a plurality of rooms, it is possible to reduce the amount of refrigerant with which the air conditioning apparatus is filled.


An air conditioning apparatus according to a second aspect is the air conditioning apparatus of the first aspect and includes a second duct that introduces the first air from the interior, a use-side unit that includes the casing and that is configured to guide the first air introduced from the interior to the use-side heat exchanger with the casing connected to the second duct, and a heat-source-side unit that accommodates the heat-source-side heat exchanger and that differs from the use-side unit.


In the air conditioning apparatus, since the use-side unit and the heat-source-side unit are different units, the air conditioning apparatus is easily installed.


An air conditioning apparatus according to a third aspect is the air conditioning apparatus of the first aspect and includes a third duct that introduces the first air from an exterior, a use-side unit that includes the casing and that is configured to guide the first air introduced from the exterior to the use-side heat exchanger with the casing connected to the third duct, and a heat-source-side unit that accommodates the heat-source-side heat exchanger and that differs from the use-side unit.


In the air conditioning apparatus, since the use-side unit and the heat-source-side unit are different units, the air conditioning apparatus is easily installed.


An air conditioning apparatus according to a fourth aspect is the air conditioning apparatus of the first aspect and includes a second duct that is connected to the casing and that supplies the first air introduced from the interior to the use-side space, wherein the casing is provided with a partition plate that partitions the casing into a heat-source-side space through which the second air introduced from an exterior passes and the use-side space to prevent circulation of air in the heat-source-side space and the use-side space, and wherein the heat-source-side heat exchanger is disposed in the heat-source-side space.


In the air conditioning apparatus, since, in one casing, the use-side heat exchanger and the heat-source-side heat exchanger are accommodated in the use-side space and the heat-source-side space that are separated by the partition plate in the same casing, the air conditioning apparatus is easily installed by using a limited space.


An air conditioning apparatus according to a 5th aspect is the air conditioning apparatus according to any of the first through 4th 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 air conditioning apparatus, it is possible to reduce the amount of refrigerant with which the air conditioning apparatus is filled 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.


An air conditioning apparatus according to a 6th aspect is the air conditioning apparatus according to the 5th 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.


An air conditioning apparatus according to a 7th aspect is the air conditioning apparatus according to the 5th 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.


An air conditioning apparatus according to a 8th aspect is the air conditioning apparatus according to the 5th 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 CJ are straight lines.


An air conditioning apparatus according to a 9th aspect is the air conditioning apparatus according to the 5th 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 CJ are straight lines.


An air conditioning apparatus according to a 10th aspect is the air conditioning apparatus according to the 5th 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.


An air conditioning apparatus according to a 11th aspect is the air conditioning apparatus according to the 5th 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.


An air conditioning apparatus according to a 12th aspect is the air conditioning apparatus according to the 5th 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.


An air conditioning apparatus according to a 13th aspect is the air conditioning apparatus according to any of the first through 4th 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 air conditioning apparatus, it is possible to reduce the amount of refrigerant with which the air conditioning apparatus is filled 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.


An air conditioning apparatus according to a 14th aspect is the air conditioning apparatus according to any of the first through 4th 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 air conditioning apparatus, it is possible to reduce the amount of refrigerant with which the air conditioning apparatus is filled 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.


An air conditioning apparatus according to a 15th aspect is the air conditioning apparatus according to any of the first through 4th 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 air conditioning apparatus, it is possible to reduce the amount of refrigerant with which the air conditioning apparatus is filled 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.


An air conditioning apparatus according to a 16th aspect is the air conditioning apparatus according to any of the first through 4th 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′ (0.1892a+29.443, 0.0, −0.8108a+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 air conditioning apparatus, it is possible to reduce the amount of refrigerant with which the air conditioning apparatus is filled 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.


An air conditioning apparatus according to a 17th aspect is the air conditioning apparatus according to any of the first through 4th 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 air conditioning apparatus, it is possible to reduce the amount of refrigerant with which the air conditioning apparatus is filled 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.


An air conditioning apparatus according to a 18th aspect is the air conditioning apparatus according to any of the first through 4th 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 air conditioning apparatus, it is possible to reduce the amount of refrigerant with which the air conditioning apparatus is filled 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.


An air conditioning apparatus according to a 19th aspect is the air conditioning apparatus according to any of the first through 4th 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 air conditioning apparatus, it is possible to reduce the amount of refrigerant with which the air conditioning apparatus is filled 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.


An air conditioning apparatus according to a 20th aspect is the air conditioning apparatus according to any of the first through 4th 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 air conditioning apparatus, it is possible to reduce the amount of refrigerant with which the air conditioning apparatus is filled 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.


An air conditioning apparatus according to a 21th aspect is the air conditioning apparatus according to any of the first through 4th 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 air conditioning apparatus, it is possible to reduce the amount of refrigerant with which the air conditioning apparatus is filled 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.


An air conditioning apparatus according to a 22th aspect is the air conditioning apparatus according to any of the first through 4th 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 air conditioning apparatus, it is possible to reduce the amount of refrigerant with which the air conditioning apparatus is filled when a refrigerant having a sufficiently low GWP, and a coefficient of performance (COP) equal to that of R410A is used.


An air conditioning apparatus according to a 23th aspect is the air conditioning apparatus according to any of the first through 4th 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 air conditioning apparatus, it is possible to reduce the amount of refrigerant with which the air conditioning apparatus is filled when a refrigerant having a sufficiently low GWP, and a coefficient of performance (COP) equal to that of R410A is used.


An air conditioning apparatus according to a 24th aspect is the air conditioning apparatus according to any of the first through 4th 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 air conditioning apparatus, it is possible to reduce the amount of refrigerant with which the air conditioning apparatus is filled when a refrigerant having a sufficiently low GWP, and a coefficient of performance (COP) equal to that of R410A is used.


An air conditioning apparatus according to a 25th aspect is the air conditioning apparatus according to any of the first through 4th 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 air conditioning apparatus, it is possible to reduce the amount of refrigerant with which the air conditioning apparatus is filled when a refrigerant having a sufficiently low GWP, and a coefficient of performance (COP) equal to that of R410A is used.


An air conditioning apparatus according to a 26th aspect is the air conditioning apparatus according to any of the first through 4th 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 air conditioning apparatus, it is possible to reduce the amount of refrigerant with which the air conditioning apparatus is filled when a refrigerant having a sufficiently low GWP, and a coefficient of performance (COP) equal to that of R410A is used.


An air conditioning apparatus according to a 27th aspect is the air conditioning apparatus according to any of the first through 4th 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 air conditioning apparatus, it is possible to reduce the amount of refrigerant with which the air conditioning apparatus is filled when a refrigerant having a sufficiently low GWP, and a coefficient of performance (COP) equal to that of R410A is used.





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 schematic view showing a disposition of an air conditioning apparatus according to a first embodiment.



FIG. 17 is a schematic structural view of the air conditioning apparatus.



FIG. 18 is a block diagram showing an electrical connection state of a controller and a thermostat in an air conditioning system according to the first embodiment.



FIG. 19 is a perspective view of a state in which an air conditioning apparatus according to a second embodiment is installed in a building.



FIG. 20 is a perspective view showing an external appearance of the air conditioning apparatus.



FIG. 21 is a perspective view showing the external appearance of the air conditioning apparatus.



FIG. 22 is a perspective view for describing an internal structure of the air conditioning apparatus.



FIG. 23 is a perspective view for describing the internal structure of the air conditioning apparatus.



FIG. 24 is a perspective view for describing the internal structure of the air conditioning apparatus.



FIG. 25 is a perspective view for describing ducts of the air conditioning apparatus.



FIG. 26 illustrates a refrigerant circuit of the air conditioning apparatus according to the second embodiment.



FIG. 27 is a block diagram for describing a control system of the air conditioning apparatus according to the second embodiment.



FIG. 28 is a partial enlarged perspective view of the vicinity of a left side portion of a use-side heat exchanger.



FIG. 29 is a schematic view for describing positional relationships between a first opening and a second opening and each member.



FIG. 30 is a schematic view showing a structure of an air conditioning apparatus according to a third embodiment.





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 CJ 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 CJ 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 O 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 l (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
% (relative
92.5
92.5
92.5
92.5
92.5
95.0
95.0
95.0



to 410A)


Refrigerating
% (relative
107.4
105.2
102.9
100.5
97.9
105.0
92.5
86.9


capacity ratio
to 410A)


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


glide


Discharge
% (relative
119.5
117.4
115.3
113.0
115.9
112.7
101.0
95.8


pressure
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
93.8
95.0
96.1
97.9
99.1
99.5



to 410A)


Refrigerating
% (relative
106.2
104.1
101.6
95.0
88.2
85.0


capacity ratio
to 410A)


Condensation
° C.
0.31
0.57
0.81
1.41
2.11
2.51


glide


Discharge
% (relative
115.8
111.9
107.8
99.0
91.2
87.7


pressure
to 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.
Example
Example




Ex. 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
96.6
98.2
99.9



to 410A)


Refrigerating
% (relative
103.1
95.1
86.6


capacity ratio
to 410A)


Condensation glide
° C.
0.46
1.27
1.71


Discharge pressure
% (relative
108.4
98.7
88.6



to 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







Example
Example
Example
Example
Example
Example
Example
Example


Item
Unit
114
115
116
117
118
119
120
121
























HFO-1132(E)
mass %
38.0
40.0
42.0
44.0
46.0
48.0
50.0
52.0


HFO-1123
mass %
40.0
38.0
36.0
34.0
32.0
30.0
28.0
26.0


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



to 410A)


Refrigerating
% (relative
94.9
94.7
94.5
94.3
94.0
93.8
93.6
93.3


capacity ratio
to 410A)


Condensation
° C.
2.36
2.35
2.33
2.32
2.30
2.27
2.25
2.21


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







Example
Example
Example
Example
Example
Example
Example
Example


Item
Unit
122
123
124
125
126
127
128
129
























HFO-1132(E)
mass %
54.0
56.0
58.0
60.0
32.0
34.0
36.0
38.0


HFO-1123
mass %
24.0
22.0
20.0
18.0
44.0
42.0
40.0
38.0


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



to 410A)


Refrigerating
% (relative
93.0
92.8
92.5
92.2
94.3
94.1
93.9
93.7


capacity ratio
to 410A)


Condensation
° C.
2.18
2.14
2.09
2.04
2.61
2.60
2.59
2.58


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







Example
Example
Example
Example
Example
Example
Example
Example


Item
Unit
130
131
132
133
134
135
136
137
























HFO-1132(E)
mass %
40.0
42.0
44.0
46.0
48.0
50.0
52.0
54.0


HFO-1123
mass %
36.0
34.0
32.0
30.0
28.0
26.0
24.0
22.0


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



to 410A)


Refrigerating
% (relative
93.5
93.3
93.1
92.8
92.6
92.4
92.1
91.8


capacity ratio
to 410A)


Condensation
° C.
2.56
2.54
2.51
2.49
2.45
2.42
2.38
2.33


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







Example
Example
Example
Example
Example
Example
Example
Example


Item
Unit
138
139
140
141
142
143
144
145
























HFO-1132(E)
mass %
56.0
58.0
60.0
30.0
32.0
34.0
36.0
38.0


HFO-1123
mass %
20.0
18.0
16.0
44.0
42.0
40.0
38.0
36.0


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



to 410A)


Refrigerating
% (relative
91.6
91.3
91.0
93.2
93.1
92.9
92.7
92.5


capacity ratio
to 410A)


Condensation
° C.
2.28
2.22
2.16
2.86
2.85
2.83
2.81
2.79


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







Example
Example
Example
Example
Example
Example
Example
Example


Item
Unit
146
147
148
149
150
151
152
153
























HFO-1132(E)
mass %
40.0
42.0
44.0
46.0
48.0
50.0
52.0
54.0


HFO-1123
mass %
34.0
32.0
30.0
28.0
26.0
24.0
22.0
20.0


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



to 410A)


Refrigerating
% (relative
92.3
92.1
91.9
91.6
91.4
91.2
90.9
90.6


capacity ratio
to 410A)


Condensation
° C.
2.77
2.74
2.71
2.67
2.63
2.59
2.53
2.48


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







Example
Example
Example
Example
Example
Example
Example
Example


Item
Unit
154
155
156
157
158
159
160
161
























HFO-1132(E)
mass %
56.0
58.0
60.0
30.0
32.0
34.0
36.0
38.0


HFO-1123
mass %
18.0
16.0
14.0
42.0
40.0
38.0
36.0
34.0


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



to 410A)


Refrigerating
% (relative
90.3
90.1
89.8
92.1
91.9
91.7
91.5
91.3


capacity ratio
to 410A)


Condensation
° C.
2.42
2.35
2.27
3.10
3.09
3.06
3.04
3.01


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







Example
Example
Example
Example
Example
Example
Example
Example


Item
Unit
162
163
164
165
166
167
168
169
























HFO-1132(E)
mass %
40.0
42.0
44.0
46.0
48.0
50.0
52.0
54.0


HFO-1123
mass %
32.0
30.0
28.0
26.0
24.0
22.0
20.0
18.0


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



to 410A)


Refrigerating
% (relative
91.1
90.9
90.7
90.4
90.2
89.9
89.7
89.4


capacity ratio
to 410A)


Condensation
° C.
2.98
2.94
2.90
2.85
2.80
2.75
2.68
2.62


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







Example
Example
Example
Example
Example
Example
Example
Example


Item
Unit
170
171
172
173
174
175
176
177
























HFO-1132(E)
mass %
56.0
58.0
60.0
32.0
34.0
36.0
38.0
42.0


HFO-1123
mass %
16.0
14.0
12.0
38.0
36.0
34.0
32.0
28.0


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



to 410A)


Refrigerating
% (relative
89.1
88.8
88.5
90.7
90.5
90.3
90.1
89.7


capacity ratio
to 410A)


Condensation
° C.
2.54
2.46
2.38
3.32
3.30
3.26
3.22
3.14


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







Example
Example
Example
Example
Example
Example
Example
Example


Item
Unit
178
179
180
181
182
183
184
185
























HFO-1132(E)
mass %
44.0
46.0
48.0
50.0
52.0
54.0
56.0
58.0


HFO-1123
mass %
26.0
24.0
22.0
20.0
18.0
16.0
14.0
12.0


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



to 410A)


Refrigerating
% (relative
89.4
89.2
89.0
88.7
88.4
88.2
87.9
87.6


capacity ratio
to 410A)


Condensation
° C.
3.08
3.03
2.97
2.90
2.83
2.75
2.66
2.57


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







Example
Example
Example
Example
Example
Example
Example
Example


Item
Unit
186
187
188
189
190
191
192
193
























HFO-1132(E)
mass %
30.0
32.0
34.0
36.0
38.0
40.0
42.0
44.0


HFO-1123
mass %
38.0
36.0
34.0
32.0
30.0
28.0
26.0
24.0


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



to 410A)


Refrigerating
% (relative
89.6
89.5
89.3
89.1
88.9
88.7
88.4
88.2


capacity ratio
to 410A)


Condensation
° C.
3.60
3.56
3.52
3.48
3.43
3.38
3.33
3.26


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







Example
Example
Example
Example
Example
Example
Example
Example


Item
Unit
194
195
196
197
198
199
200
201
























HFO-1132(E)
mass %
46.0
48.0
50.0
52.0
54.0
56.0
58.0
60.0


HFO-1123
mass %
22.0
20.0
18.0
16.0
14.0
12.0
10.0
8.0


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



to 410A)


Refrigerating
% (relative
88.0
87.7
87.5
87.2
86.9
86.6
86.3
86.0


capacity ratio
to 410A)


Condensation
° C.
3.20
3.12
3.04
2.96
2.87
2.77
2.66
2.55


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







Example
Example
Example
Example
Example
Example
Example
Example


Item
Unit
202
203
204
205
206
207
208
209
























HFO-1132(E)
mass %
30.0
32.0
34.0
36.0
38.0
40.0
42.0
44.0


HFO-1123
mass %
36.0
34.0
32.0
30.0
28.0
26.0
24.0
22.0


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



to 410A)


Refrigerating
% (relative
88.4
88.2
88.0
87.8
87.6
87.4
87.2
87.0


capacity ratio
to 410A)


Condensation
° C.
3.84
3.80
3.75
3.70
3.64
3.58
3.51
3.43


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







Example
Example
Example
Example
Example
Example
Example
Example


Item
Unit
210
211
212
213
214
215
216
217
























HFO-1132(E)
mass %
46.0
48.0
50.0
52.0
54.0
30.0
32.0
34.0


HFO-1123
mass %
20.0
18.0
16.0
14.0
12.0
34.0
32.0
30.0


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



to 410A)


Refrigerating
% (relative
86.7
86.5
86.2
85.9
85.6
87.2
87.0
86.8


capacity ratio
to 410A)


Condensation
° C.
3.36
3.27
3.18
3.08
2.97
4.08
4.03
3.97


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







Example
Example
Example
Example
Example
Example
Example
Example


Item
Unit
218
219
220
221
222
223
224
225
























HFO-1132(E)
mass %
36.0
38.0
40.0
42.0
44.0
46.0
30.0
32.0


HFO-1123
mass %
28.0
26.0
24.0
22.0
20.0
18.0
32.0
30.0


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



to 410A)


Refrigerating
% (relative
86.6
86.4
86.2
85.9
85.7
85.5
85.9
85.7


capacity ratio
to 410A)


Condensation
° C.
3.91
3.84
3.76
3.68
3.60
3.50
4.32
4.25


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
97.4
97.6




to 410A)



Refrigerating
% (relative
85.6
85.3



capacity ratio
to 410A)



Condensation glide
° C.
4.18
4.11



Discharge pressure
% (relative
91.0
90.6




to 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, 0.00672x2−0.7607x+63.525, −0.00672x2−0.2393x+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-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













Leak condition that results in WCFF
Storage/
Storage/
Storage/
Storage/
Storage/
Storage/



Shipping
Shipping
Shipping
Shipping
Shipping
Shipping,



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



92% release,
90% release,
90% release,
66% release,
12% release,
0% release,



liquid phase
liquid phase
gas phase
gas phase
gas phase
gas phase



side
side
side
side
side
side















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



HFO-1123
mass %
28.0
17.8
17.4
13.6
12.3
9.8



R1234yf
mass %
0.0
10.2
10.6
14.4
15.7
18.2














Burning velocity (WCF)
cm/s
8 or
8 or
8 or
9
9
8 or




less
less
less


less


Burning velocity (WCFF)
cm/s
10
10
10
10
10
10









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







Comparative
Comparative











Example 1
Example 2
Comparative
Example
Example
Example
Example
Example
Comparative


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

























HFO-1132E
mass %

100
80
72
70
68
65
62
60


(WCF)


HFO-1123
mass %

0
20
28
30
32
35
38
40


(WCF)


GWP

2088
1
1
1
1
1
1
1
1


COP ratio
%
100
99.7
97.5
96.6
96.3
96.1
95.8
95.4
95.2



(relative



to R410A)


Refrigerating
%
100
98.3
101.9
103.1
103.4
103.8
104.1
104.5
104.8


capacity
(relative


ratio
to 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-flammable
20
13
10
9
9
8
8 or
8 or


velocity








less
less


(WCF)


























TABLE 38















Comparative




Comparative
Comparative
Example
Example
Example
Comparative
Comparative
Comparative
Example 10


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

























HFO-1132E
mass %
50
48
47.1
46.1
45.1
43
40
25
0


(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
% (relative
94.1
93.9
93.8
93.7
93.6
93.4
93.1
91.9
90.6



to R410A)


Refrigerating
% (relative
105.9
106.1
106.2
106.3
106.4
106.6
106.9
107.9
108.0


capacity
to R410A)


ratio


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 (WCFF)
Shipping
Shipping
Shipping
Shipping
Shipping
Shipping
Shipping
Shipping



−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
8 or
8 or
8 or
8 or
8 or
8 or
8 or
5


velocity

less
less
less
less
less
less
less
less


(WCF)


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


velocity







less
less


(WCFF)
















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


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′ (0.1892a+29.443, 0.0, −0.8108a+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.
Ex.




Comp.
Ex. 2
Ex. 3
Ex. 4
Ex. 5
Ex. 6
Ex. 7
Ex. 8
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
100
100.0
95.5
92.5
93.1
96.6
99.9
93.8
99.4



to R410A)


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


capacity ratio
to R410A)

























TABLE 40







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




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


Item
Unit
A
B
C
D′
G
I
J
K′
























HFO-1132(E)
Mass %
55.3
0.0
18.4
0.0
60.9
60.9
40.5
47.0


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
% (relative
99.8
96.9
92.5
92.5
95.9
99.6
94.0
99.2



to R410A)


Refrigerating
% (relative
85.0
85.0
110.5
106.0
106.5
87.7
108.9
85.5


capacity ratio
to R410A)
























TABLE 41







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




Ex. 16
Ex. 17
Ex. 18
Ex.19
Ex. 20
Ex. 21
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
% (relative
99.8
97.6
92.5
95.8
99.5
94.2
99.3



to R410A)


Refrigerating
% (relative
85.0
85.0
112.0
108.0
88.6
110.2
85.4


capacity ratio
to R410A)























TABLE 42







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




Ex. 22
Ex. 23
Ex. 24
Ex. 25
Ex. 26
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
99.9
98.1
95.8
99.5
94.4
99.5



to R410A)


Refrigerating
% (relative
85.0
85.0
109.1
89.6
111.1
85.3


capacity ratio
to R410A)























TABLE 43







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




Ex. 27
Ex. 28
Ex. 29
Ex. 30
Ex. 31
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
100.0
98.6
95.9
99.4
94.7
99.8



to R410A)


Refrigerating
% (relative
85.0
85.0
110.1
90.8
111.9
85.2


capacity ratio
to R410A)























TABLE 44







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




Ex. 32
Ex. 33
Ex. 34
Ex. 35
Ex. 36
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
100.2
99.1
96.0
99.4
95.1
100.0



to R410A)


Refrigerating
% (relative
85.0
85.0
111.0
92.1
112.6
85.1


capacity ratio
to R410A)























TABLE 45







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




Ex. 37
Ex. 38
Ex. 39
Ex. 40
Ex. 41
Ex. 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
100.4
99.8
96.3
99.4
95.6
100.4



to R410A)


Refrigerating
% (relative
85.0
85.0
111.9
93.8
113.2
85.0


capacity ratio
to R410A)























TABLE 46







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




Ex. 43
Ex.44
Ex. 45
Ex. 46
Ex. 47
Ex. 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
100.6
100.1
96.6
99.5
96.1
100.4



to R410A)


Refrigerating
% (relative
85.0
85.0
112.4
94.8
113.6
86.7


capacity ratio
to R410A)























TABLE 47







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




Ex. 49
Ex. 50
Ex. 51
Ex. 52
Ex. 53
Ex. 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
101.2
101.0
96.4
99.6
97.0
100.4



to R410A)


Refrigerating
% (relative
85.0
85.0
113.2
97.6
113.9
90.9


capacity ratio
to R410A)























TABLE 48







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




Ex. 55
Ex. 56
Ex. 57
Ex. 58
Ex. 59
Ex. 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
101.8
101.8
97.9
99.8
97.8
100.5



to R410A)


Refrigerating
% (relative
85.0
85.0
113.7
100.4
113.9
94.9


capacity ratio
to R410A)






















TABLE 49







Comp.
Comp.
Comp.
Comp.
Comp.




Ex. 61
Ex. 62
Ex. 63
Ex. 64
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
102.1
98.2
100.0
98.2
100.6



to R410A)


Refrigerating
% (relative
85.0
113.8
101.8
113.9
96.8


capacity ratio
to R410A)

























TABLE 50







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


Item
Unit
Ex. 66
7
8
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
92.4
92.6
92.8
93.1
93.4
93.7
94.1
94.5



to R410A)


Refrigerating
% (relative
108.4
108.3
108.2
107.9
107.6
107.2
106.8
106.3


capacity ratio
to R410A)

























TABLE 51







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


Item
Unit
14
15
16
17
Ex. 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
95.0
95.4
95.9
96.4
96.9
93.0
93.3
93.6



to R410A)


Refrigerating
% (relative
105.8
105.2
104.5
103.9
103.1
105.7
105.5
105.2


capacity ratio
to R410A)

























TABLE 52







Ex.
Ex.
Ex.
Ex.
Ex.
Ex.
Ex.
Ex.


Item
Unit
21
22
23
24
25
26
27
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.


Item
Unit
Ex. 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.


Item
Unit
36
37
38
39
Ex. 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







Ex.
Ex.
Ex.
Ex.
Ex.
Ex.
Ex.
Ex.


Item
Unit
43
44
45
46
47
48
49
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.


Item
Unit
Ex. 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.


Item
Unit
58
59
60
61
Ex. 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







Ex.
Ex.
Ex.
Ex.
Ex.
Ex.
Ex.
Ex.


Item
Unit
65
66
67
68
69
70
71
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







Ex.
Ex.
Ex.
Ex.
Ex.
Ex.
Ex.
Ex.


Item
Unit
73
74
75
76
77
78
79
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







Ex.
Ex.
Ex.
Ex.
Ex.
Ex.
Ex.
Ex.


Item
Unit
81
82
83
84
85
86
87
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
99.1
99.5
99.9



to R410A)


Refrigerating capacity ratio
% (relative
82.9
82.3
81.7



to R410A)

























TABLE 63







Ex.
Ex.
Ex.
Ex.
Ex.
Ex.
Ex.
Ex.


Item
Unit
89
90
91
92
93
94
95
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.


Item
Unit
97
Ex. 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.


Item
Unit
104
105
106
Ex. 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.


Item
Unit
111
112
113
114
115
Ex. 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.


Item
Unit
118
119
120
121
122
123
124
Ex. 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
95.6
95.9
96.1
96.4
96.7
97.1
97.5
97.9



to R410A)


Refrigerating
% (relative to
98.9
98.6
98.3
97.9
97.4
96.9
96.3
95.7


capacity ratio
R410A)

























TABLE 69







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


Item
Unit
133
Ex. 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
98.3
98.7
96.2
96.4
96.7
97.0
97.3
97.7



to R410A)


Refrigerating
% (relative
95.0
94.3
95.8
95.6
95.2
94.8
94.4
93.8


capacity ratio
to 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
98.1
98.5
98.9
96.8
97.0
97.3
97.6
97.9



to R410A)


Refrigerating
% (relative
93.3
92.6
92.0
92.8
92.5
92.2
91.8
91.3


capacity ratio
to 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
98.3
98.7
99.1
97.4
97.7
98.0
98.3
98.6



to R410A)


Refrigerating
% (relative
90.8
90.2
89.6
89.6
89.4
89.0
88.6
88.2


capacity ratio
to R410A)

























TABLE 72







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


Item
Unit
156
157
158
159
160
Ex. 88
Ex. 89
Ex. 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
98.9
99.3
98.1
98.4
98.7
98.9
99.3
99.6



to R410A)


Refrigerating
% (relative
87.6
87.1
86.5
86.2
85.9
85.5
85.0
84.5


capacity ratio
to R410A)






















TABLE 73







Comp.
Comp.
Comp.
Comp.
Comp.


Item
Unit
Ex. 91
Ex. 92
Ex. 93
Ex. 94
Ex. 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
98.9
99.1
99.4
99.7
100.0



to R410A)


Refrigerating
% (relative
83.3
83.0
82.7
82.2
81.8


capacity ratio
to 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
94.8
95.0
95.2
95.4
95.7
95.9
96.2
96.6



to R410A)


Refrigerating
% (relative
111.5
111.2
110.9
110.5
110.0
109.5
108.9
108.3


capacity ratio
to R410A)

























TABLE 75







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


Item
Unit
Ex. 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
96.9
95.3
95.4
95.6
95.8
96.1
96.4
96.7



to R410A)


Refrigerating
% (relative
107.7
108.7
108.5
108.1
107.7
107.2
106.7
106.1


capacity ratio
to R410A)

























TABLE 76







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


Item
Unit
176
Ex. 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
97.0
97.4
95.7
95.9
96.1
96.3
96.6
96.9



to R410A)


Refrigerating
% (relative
105.5
104.9
105.9
105.6
105.3
104.8
104.4
103.8


capacity ratio
to R410A)

























TABLE 77







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


Item
Unit
183
184
Ex. 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
97.2
97.5
97.9
96.1
96.3
96.5
96.8
97.1



to R410A)


Refrigerating
% (relative
103.3
102.6
102.0
103.0
102.7
102.3
101.9
101.4


capacity ratio
to R410A)

























TABLE 78







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


Item
Unit
190
191
192
Ex. 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
97.4
97.7
98.0
98.4
96.6
96.8
97.0
97.3



to R410A)


Refrigerating
% (relative
100.9
100.3
99.7
99.1
100.0
99.7
99.4
98.9


capacity ratio
to R410A)

























TABLE 79







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


Item
Unit
197
198
199
200
Ex. 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
97.6
97.9
98.2
98.5
98.9
97.1
97.3
97.6



to R410A)


Refrigerating
% (relative
98.5
97.9
97.4
96.8
96.1
97.0
96.7
96.3


capacity ratio
to 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
97.8
98.1
98.4
98.7
99.1
97.7
97.9
98.1



to R410A)


Refrigerating
% (relative
95.9
95.4
94.9
94.4
93.8
93.9
93.6
93.3


capacity ratio
to 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
98.4
98.7
99.0
99.3
98.3
98.5
98.7
99.0



to R410A)


Refrigerating
% (relative
92.9
92.4
91.9
91.3
90.8
90.5
90.2
89.7


capacity ratio
to R410A)

























TABLE 82







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


Item
Unit
220
221
222
223
224
225
226
Ex. 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
99.3
99.6
98.9
99.1
99.3
99.6
99.9
99.6



to R410A)


Refrigerating
% (relative
89.3
88.8
87.6
87.3
87.0
86.6
86.2
84.4


capacity ratio
to 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
99.8
100.0
100.2



to R410A)


Refrigerating
% (relative
84.1
83.8
83.4


capacity ratio
to R410A)

























TABLE 84







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


Item
Unit
227
228
229
230
231
232
233
Ex. 105
























HFO-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
95.9
96.0
96.2
96.3
96.6
96.8
97.1
97.3



to R410A)


Refrigerating
% (relative
112.2
111.9
111.6
111.2
110.7
110.2
109.6
109.0


capacity ratio
to R410A)

























TABLE 85







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


Item
Unit
234
235
236
237
238
239
240
Ex. 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
96.3
96.4
96.6
96.8
97.0
97.2
97.5
97.8



to 410A)


Refrigerating
% (relative
109.4
109.2
108.8
108.4
107.9
107.4
106.8
106.2


capacity ratio
to R410A)

























TABLE 86







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


Item
Unit
241
242
243
244
245
246
247
Ex. 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
96.7
96.8
97.0
97.2
97.4
97.7
97.9
98.2



to 410A)


Refrigerating
% (relative
106.6
106.3
106.0
105.5
105.1
104.5
104.0
103.4


capacity ratio
to R410A)

























TABLE 87







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


Item
Unit
248
249
250
251
252
253
254
Ex. 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
97.1
97.3
97.5
97.7
97.9
98.1
98.4
98.7



to R410A)


Refrigerating
% (relative
103.7
103.4
103.0
102.6
102.2
101.6
101.1
100.5


capacity ratio
to 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
97.6
97.7
97.9
98.1
98.4
98.6
98.9
98.1



to R410A)


Refrigerating
% (relative
100.7
100.4
100.1
99.7
99.2
98.7
98.2
97.7


capacity ratio
to 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
98.2
98.4
98.6
98.9
99.1
98.6
98.7
98.9



to R410A)


Refrigerating
% (relative
97.4
97.1
96.7
96.2
95.7
94.7
94.4
94.0


capacity ratio
to 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


COP ratio
% (relative
99.2
99.4
99.1
99.3
99.5
99.7
99.7
99.8



to R410A)


Refrigerating
% (relative
93.6
93.2
91.5
91.3
90.9
90.6
88.4
88.1


capacity ratio
to R410A)





















TABLE 91







Ex.
Ex.
Comp.
Comp.


Item
Unit
279
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.


Item
Unit
281
282
283
284
285
Ex. 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


COP ratio
% (relative
97.8
97.9
97.9
98.1
98.2
98.4
98.2
98.2



to R410A)


Refrigerating
% (relative
112.5
112.3
111.9
111.6
111.2
110.7
109.8
109.5


capacity ratio
to R410A)

























TABLE 93







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


Item
Unit
288
289
290
Ex. 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
98.3
98.5
98.6
98.8
98.6
98.6
98.7
98.9



to R410A)


Refrigerating
% (relative
109.2
108.8
108.4
108.0
107.0
106.7
106.4
106.0


capacity ratio
to R410A)

























TABLE 94







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


Item
Unit
295
Ex. 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
99.0
99.2
99.0
99.0
99.2
99.3
99.4
99.4



to R410A)


Refrigerating
% (relative
105.6
105.2
104.1
103.9
103.6
103.2
102.8
101.2


capacity ratio
to 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
99.5
99.6
99.7
99.8
99.9
100.0
100.3
100.4



to R410A)


Refrigerating
% (relative
101.0
100.7
100.3
98.3
98.0
97.8
95.3
95.1


capacity ratio
to R410A)




















TABLE 96









Ex.



Item
Unit
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
100.7




to R410A)



Refrigerating capacity ratio
% (relative
92.3




to R410A)










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.
Comp.
Comp.
Comp.
Comp.
Comp.



Item
Ex. 6
Ex. 13
Ex. 19
Ex. 24
Ex. 29
Ex. 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 (WCF)
cm/s
10
10
10
10
10
10





















TABLE 98






Comp.
Comp.
Comp.
Comp.
Comp.


Item
Ex. 39
Ex. 45
Ex. 51
Ex. 57
Ex. 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
21.8



R1234yf
Mass %
0
0
0
0
0



R32
Mass %
26.7
29.3
36.7
44.1
47.8













Burning velocity (WCF)
cm/s
10
10
10
10
10
























TABLE 99








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



Item
Ex. 7
Ex. 14
Ex. 20
Ex. 25
Ex. 30
Ex. 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 (WCF)
cm/s
10
10
10
10
10
10





















TABLE 100






Comp.
Comp.
Comp.
Comp.
Comp.


Item
Ex. 40
Ex. 46
Ex. 52
Ex. 58
Ex. 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 (WCF)
cm/s
10
10
10
10
10






















TABLE 101






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


Item
Ex. 8
Ex. 15
Ex. 21
Ex. 26
Ex. 31
Ex. 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 in WCFF
Storage/
Storage/
Storage/
Storage/
Storage/
Storage/



Shipping
Shipping
Shipping
Shipping
Shipping
Shipping



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



92% release,
92% release,
92% release,
92% release,
92% release,
92% release,



liquid
liquid
liquid
liquid
liquid
liquid



phase side
phase side
phase side
phase side
phase side
phase 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 (WCF)
cm/s
8 or
8 or
8 or
8 or
8 or
8 or




less
less
less
less
less
less


Burning velocity (WCFF)
cm/s
10
10
10
10
10
10





















TABLE 102






Comp.
Comp.
Comp.
Comp.
Comp.


Item
Ex. 41
Ex. 47
Ex. 53
Ex. 59
Ex. 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 WCFF
Storage/
Storage/
Storage/
Storage/
Storage/



Shipping −40°
Shipping −40°
Shipping −40°
Shipping −40°
Shipping −40°



C., 92%
C., 92%
C., 92%
C., 90%
C., 86%



release,
release,
release,
release,
release,



liquid
liquid
liquid
gas
gas



phase side
phase side
phase side
phase side
phase 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 (WCF)
cm/s
8 or less
8 or less
8.3
9.3
9.6


Burning velocity (WCFF)
cm/s
10
10
10
10
10






















TABLE 103






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


Item
Ex. 9
Ex. 16
Ex. 22
Ex. 27
Ex. 32
Ex. 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 WCFF
Storage/
Storage/
Storage/
Storage/
Storage/
Storage/



Shipping −40°
Shipping −40°
Shipping −40°
Shipping −40°
Shipping −40°
Shipping −40°



C., 0%
C., 0%
C., 0%
C., 92%
C., 0%
C., 0%



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



gas
gas
gas
liquid
gas
gas



phase side
phase side
phase side
phase side
phase side
phase 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 (WCF)
cm/s
8 or less
8 or less
8 or less
8 or less
8 or less
8 or less


Burning velocity (WCFF)
cm/s
10
10
10
10
10
10





















TABLE 104






Comp.
Comp.
Comp.
Comp.
Comp.


Item
Ex. 42
Ex. 48
Ex. 54
Ex. 60
Ex. 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 WCFF
Storage/
Storage/
Storage/
Storage/
Storage/



Shipping −40°
Shipping −40°
Shipping −40°
Shipping −40°
Shipping −40°



C., 0%
C., 0%
C., 0%
C., 0%
C., 0%



release,
release,
release,
release,
release,



gas
gas
gas
gas
gas



phase side
phase side
phase side
phase side
phase 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 (WCF)
cm/s
8 or less
8 or less
8 or less
8 or less
8 or less


Burning velocity (WCFF)
cm/s
10
10
10
10
10









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′(−0.1892a+29.443, 0.0, −0.8108a+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
−0.1892a + 29.443



Approximate





expression





HFO-1123
0
0



Approximate





expression





R1234yf
 0.0051a2 − 1.0929a + 74.05
 0.8108a + 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)
0



Approximate



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(E)
Mass %
72
57.2
48.5
41.2
35.6
32
28.9



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 (WCF)
cm/s
10
10
10
10
10
10
10























TABLE 114







Comparative

Example

Example





Example 14
Example
19
Example
21
Example


Item
Unit
M
18
W
20
N
22























WCF
HFO-1132(E)
Mass %
52.6
39.2
32.4
29.3
27.7
24.6



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 WCFF
Storage,
Storage,
Storage,
Storage,
Storage,
Storage,



Shipping, −40°
Shipping, −40°
Shipping, −40°
Shipping, −40°
Shipping, −40°
Shipping, −40°



C., 0%
C., 0%
C., 0%
C., 0%
C., 0%
C., 0%



release, on
release, on
release, on
release, on
release, on
release, on



the gas
the gas
the gas
the gas
the gas
the gas



phase side
phase side
phase side
phase side
phase side
phase side















WCF
HFO-1132(E)
Mass %
72.0
57.8
48.7
43.6
40.6
34.9



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 (WCF)
cm/s
8 or less
8 or less
8 or less
8 or less
8 or less
8 or less


Burning Velocity (WCFF)
cm/s
10
10
10
10
10
10




















TABLE 115







Example

Example




23
Example
25


Item
Unit
O
24
P




















WCF
HFO-1132 (E)
Mass %
22.6
21.2
20.5



HFO-1132
Mass %
36.8
44.2
51.7



R1234yf
Mass %
40.6
34.6
27.8










Leak condition that results in WCFF
Storage,
Storage,
Storage,



Shipping, −40°
Shipping, −40°
Shipping, −40°



C., 0%
C., 0%
C., 0%



release, on
release, on
release, on



the gas
the gas
the gas



phase side
phase side
phase side












WCF
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 (WCF)
cm/s
8 or less
8 or less
8 or less


Burning Velocity (WCFF)
cm/s
10
10
10









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 Ratio
to R410A)
























TABLE 117







Comparative

Comparative

Example

Example




Example 8
Comparative
Example 10
Example
2
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 Ratio
to R410A)

























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 Ratio
to R410A)

























TABLE 119







Comparative

Example

Example

Example
Example




Example 13
Example
12
Example
14
Example
16
17


Item
Unit
I
11
J
13
K
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 Ratio
to R410A)























TABLE 120







Comparative

Example

Example





Example 14
Example
19
Example
21
Example


Item
Unit
M
18
W
20
N
22






















HFO-1132(E)
Mass %
52.6
39.2
32.4
29.3
27.7
24.5


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 Ratio
% (relative
100.5
100.9
100.9
100.8
100.7
100.4



to R410A)


Refrigerating
% (relative
77.1
74.8
75.6
77.8
80.0
85.5


Capacity Ratio
to R410A)





















TABLE 121







Example

Example
Example




23
Example
25
26


Item
Unit
O
24
P
S




















HFO-
Mass %
22.6
21.2
20.5
21.9


1132(E)


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)


Refriger-
% (relative
91.0
95.0
99.1
92.5


ating
to R410A)


Capacity


Ratio

























TABLE 122







Comparative
Comparative
Comparative
Comparative
Example
Example
Comparative
Comparative


Item
Unit
Example 15
Example 16
Example 17
Example 18
27
28
Example 19
Example 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 Ratio
to R410A)

























TABLE 123







Comparative
Comparative
Example
Comparative
Example
Comparative
Comparative
Comparative


Item
Unit
Example 21
Example 22
29
Example 23
30
Example 24
Example 25
Example 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 Ratio
to R410A)

























TABLE 124







Comparative
Example
Comparative
Example
Example
Comparative
Comparative
Comparative


Item
Unit
Example 27
31
Example 28
32
33
Example 29
Example 30
Example 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 Ratio
to R410A)

























TABLE 125







Comparative
Comparative
Comparative
Comparative
Comparative
Comparative
Comparative
Comparative


Item
Unit
Example 32
Example 33
Example 34
Example 35
Example 36
Example 37
Example 38
Example 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 Ratio
to R410A)

























TABLE 126







Example
Comparative
Comparative
Comparative
Comparative
Comparative
Comparative
Example


Item
Unit
34
Example 40
Example 41
Example 42
Example 43
Example 44
Example 45
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 Ratio
to R410A)

























TABLE 127







Comparative
Comparative
Comparative
Comparative
Example
Example
Example
Comparative


Item
Unit
Example 46
Example 47
Example 48
Example 49
36
37
38
Example 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 Ratio
to R410A)

























TABLE 128







Comparative
Comparative
Comparative
Comparative
Example
Comparative
Comparative
Comparative


Item
Unit
Example 51
Example 52
Example 53
Example 54
39
Example 55
Example 56
Example 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 Ratio
to R410A)

























TABLE 129







Example
Example
Comparative
Comparative
Comparative
Example
Comparative
Comparative


Item
Unit
40
41
Example 58
Example 59
Example 60
42
Example 61
Example 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 Ratio
to R410A)

























TABLE 130







Comparative
Comparative
Comparative
Comparative
Example
Example
Example
Example


Item
Unit
Example 63
Example 64
Example 65
Example 66
43
44
45
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 Ratio
to R410A)

























TABLE 131







Example
Example
Example
Example
Example
Example
Example
Example


Item
Unit
47
48
49
50
51
52
53
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 Ratio
to R410A)

























TABLE 132







Example
Example
Example
Example
Example
Example
Example
Example


Item
Unit
55
56
57
58
59
60
61
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 Ratio
to R410A)

























TABLE 133







Example
Example
Example
Example
Example
Example
Example
Example


Item
Unit
63
64
65
66
67
68
69
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 Ratio
to R410A)

























TABLE 134







Example
Example
Example
Example
Example
Example
Example
Example


Item
Unit
71
72
73
74
75
76
77
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 Ratio
to R410A)

























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
610
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 Ratio
to R410A)

























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 Ratio
to R410A)

























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 Ratio
to R410A)

























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 Ratio
to R410A)

























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 Ratio
to R410A)

























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 Ratio
to R410A)

























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 Ratio
to R410A)

























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 Ratio
to R410A)

























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 Ratio
to R410A)



















TABLE 144







Example
Example


Item
Unit
151
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
100.3
100.1



to R410A)


Refrigerating Capacity
% (relative
99.8
101.3


Ratio
to 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 WCFF
Storage,
Storage,
Storage,
Storage,
Storage,
Storage,



Shipping, −40°
Shipping, −40°
Shipping, −40°
Shipping, −40°
Shipping, −40°
Shipping, −40°



C., 92%,
C., 92%,
C., 92%,
C., 92%,
C., 92%,
C., 92%,



release, on
release, on
release, on
release, on
release, on
release, on



the liquid
the liquid
the liquid
the liquid
the liquid
the liquid



phase side
phase side
phase side
phase side
phase side
phase 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 (WCF)
cm/s
8 or less
8 or less
8 or less
8 or less
8 or less
8 or less


Burning velocity (WCFF)
cm/s
10
10
10
10
10
10









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 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
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 ratio
to R410A)























TABLE 148







Comparative
Comparative

Example

Comparative




Example 8
Example 9
Comparative
1
Example
Example 11


Item
Unit
O
C
Example 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



Comparative




Example 15

Example 6

Example 16


Item
Unit
G
Example 5
R
Example 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 to
93.0
93.0
93.0
93.0
93.0



R410A)


Refrigerating
% (relative to
107.0
109.1
110.9
111.9
113.2


capacity ratio
R410A)






















TABLE 151







Comparative
Example
Example

Comparative




Example 17
8
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
96.6
95.8
95.9
96.4
97.1



to R410A)


Refrigerating
% (relative
103.1
107.4
110.1
112.1
113.2


capacity ratio
to R410A)





















TABLE 152







Comparative
Example
Example
Example




Example 20
10
11
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
Example
Example
Example
Comparative
Comparative


Item
Unit
Example 22
Example 23
Example 24
14
15
16
Example 25
Example 26
























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


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
% (relative
91.7
92.2
92.9
93.7
94.6
95.6
96.7
97.7



to R410A)


Refrigerating
% (relative
110.1
109.8
109.2
108.4
107.4
106.1
104.7
103.1


capacity ratio
to R410A)

























TABLE 154







Comparative
Comparative
Comparative
Example
Example
Example
Comparative
Comparative


Item
Unit
Example 27
Example 28
Example 29
17
18
19
Example 30
Example 31
























HFO-1132(E)
mass %
90.0
10.0
20.0
30.0
40.0
50.0
60.0
70.0


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
% (relative
98.8
92.4
92.9
93.5
94.3
95.1
96.1
97.0



to R410A)


Refrigerating
% (relative
101.4
111.7
111.3
110.6
109.6
108.5
107.2
105.7


capacity ratio
to R410A)

























TABLE 155







Comparative
Example
Example
Example
Example
Example
Comparative
Comparative


Item
Unit
Example 32
20
21
22
23
24
Example 33
Example 34
























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


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
% (relative
98.0
93.1
93.6
94.2
94.9
95.6
96.5
97.4



to R410A)


Refrigerating
% (relative
104.1
112.9
112.4
111.6
110.6
109.4
108.1
106.6


capacity ratio
to R410A)

























TABLE 156







Comparative
Comparative
Comparative
Comparative
Comparative
Comparative
Comparative
Comparative


Item
Unit
Example 35
Example 36
Example 37
Example 38
Example 39
Example 40
Example 41
Example 42
























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


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
% (relative
98.3
93.9
94.3
94.8
95.4
96.2
97.0
97.8



to R410A)


Refrigerating
% (relative
105.0
113.8
113.2
112.4
111.4
110.2
108.8
107.3


capacity ratio
to R410A)

























TABLE 157







Comparative
Comparative
Comparative
Comparative
Comparative
Comparative
Comparative
Comparative


Item
Unit
Example 43
Example 44
Example 45
Example 46
Example 47
Example 48
Example 49
Example 50
























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


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
% (relative
94.6
94.9
95.4
96.0
96.7
97.4
98.2
95.3



to R410A)


Refrigerating
% (relative
114.4
113.8
113.0
111.9
110.7
109.4
107.9
114.8


capacity ratio
to R410A)

























TABLE 158







Comparative
Comparative
Comparative
Comparative
Comparative
Example
Example
Comparative


Item
Unit
Example 51
Example 52
Example 53
Example 54
Example 55
25
26
Example 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 ratio
to R410A)

























TABLE 159







Comparative
Comparative
Comparative
Comparative
Comparative
Comparative
Comparative
Comparative


Item
Unit
Example 57
Example 58
Example 59
Example 60
Example 61
Example 62
Example 63
Example 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
97.1
97.7
98.3
96.6
96.9
97.2
97.7
98.2



to R410A)


Refrigerating
% (relative
112.6
111.5
110.2
115.1
114.6
113.8
112.8
111.7


capacity ratio
to 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) First Embodiment


FIG. 16 is a schematic view showing a disposition of an air conditioning apparatus 1 according to a first embodiment. FIG. 17 is a schematic structural view of the air conditioning apparatus 1. In FIGS. 16 and 17, the air conditioning apparatus 1 is a device that is used to air-condition houses or buildings.


Here, the air conditioning apparatus 1 is installed in a two-story house 100. The house 100 includes rooms 101 and 102 on the first floor and rooms 103 and 104 on the second floor. The house 100 includes a basement 105.


The air conditioning apparatus 1 is a so-called duct air conditioning system. The air conditioning apparatus 1 includes an indoor unit 2 that is a use-side unit, an outdoor unit 3 that is a heat-source-side unit, refrigerant connection pipes 306 and 307, and a first duct 209 that sends air that has been air-conditioned at the indoor unit 2 to the rooms 101 to 104. The first duct 209 branches into the rooms 101 to 104, and the branching portions are connected to ventilation ports 101a to 104a of the corresponding rooms 101 to 104. For convenience of explanation, the indoor unit 2, the outdoor unit 3, and the refrigerant connection pipes 306 and 307 are considered together as air conditioning equipment 80. The indoor unit 2 that is a use-side unit and the outdoor unit 3 that is a heat-source unit are different members.


In FIG. 17, the indoor unit 2, the outdoor unit 3, and the refrigerant connection pipes 306 and 307 constitute a heat pump section 360 that heats an interior in a vapor compression refrigeration cycle. A gas furnace unit 205 that is a part of the indoor unit 2 constitutes a different heat source section 270 that heats the interior by using a heat source (here, heat by gas combustion) that differs from that of the heat pump section 360.


In this way, the indoor unit 2 includes the gas furnace unit 205 that constitutes the different heat source section 270 in addition to the members that constitute the heat pump section 360. The indoor unit 2 also includes an indoor fan 240 for introducing air in the rooms 101 to 104 into a casing 230 and suppling air that has been air-conditioned at the heat pump section 360 and the different heat source section 270 (the gas furnace unit 205) into the rooms 101 to 104. The indoor unit 2 is provided with a blow-out air temperature sensor 233 that detects a blow-out air temperature Trd that is the temperature of air in an air outlet 231 of the casing 230 and an indoor temperature sensor 234 that detects an indoor temperature Tr that is the temperature of air in an air inlet 232 of the casing 230. The indoor temperature sensor 234 may be provided in the rooms 101 to 104 instead of in the indoor unit 2. A second duct 210 is connected to the air inlet 232 of the casing 230. The indoor unit 2 that is a use-side unit includes the casing 230 and equipment that is accommodated therein. The indoor unit 2 is configured to guide indoor air F1 that is first air introduced from the interior to an indoor heat exchanger 242 that is a use-side heat exchanger.


(6-1) Heat Pump Section 360


In the heat pump section 360 of the air conditioning equipment 80, a refrigerant circuit 320 is formed by connecting the indoor unit 2 and the outdoor unit 3 via the refrigerant connection pipes 306 and 307. The refrigerant connection pipes 306 and 307 are refrigerant pipes that are constructed at a site when installing the air conditioning equipment 80.


The indoor unit 2 is installed in the basement 105 of the house 100. The location of installation of the indoor unit 2 is not limited to the basement 105, and may be other locations in the interior. The indoor unit 2 includes the indoor heat exchanger 242 that serves as a refrigerant heat dissipater that heats air by heat dissipation of a refrigerant in a refrigeration cycle, and an indoor expansion valve 241.


At the time of a cooling operation, the indoor expansion valve 241 decompresses a refrigerant that circulates in the refrigerant circuit 320 and causes the refrigerant to flow to the indoor heat exchanger 242. Here, the indoor expansion valve 241 is an electric expansion valve that is connected to a liquid side of the indoor heat exchanger 242.


The indoor heat exchanger 242 is disposed closest to a downwind side in a ventilation path extending from the air inlet 232, formed in the casing 230, to the air outlet 231, formed in the casing 230.


The outdoor unit 3 is installed outside the house 100. The outdoor unit 3 includes a compressor 321, an outdoor heat exchanger 323, an outdoor expansion valve 324, and a four-way valve 328. The compressor 321 is a hermetic compressor in which a compression element (not shown) and a compressor motor 322 that rotationally drives the compression element are accommodated in a casing.


The compressor motor 322 is configured so that electric power is supplied thereto via an inverter device (not shown), and an operating capacity can be varied by changing the frequency (that is, the number of rotations) of the inverter device.


The outdoor heat exchanger 323 is a heat exchanger that functions as a refrigerant evaporator that evaporates a refrigerant in a refrigeration cycle by using outdoor air. An outdoor fan 325 for sending outdoor air to the outdoor heat exchanger 323 is provided in the vicinity of the outdoor heat exchanger 323. The outdoor fan 325 is rotationally driven by an outdoor fan motor 326.


At the time of a heating operation, the outdoor expansion valve 324 decompresses a refrigerant that circulates in the refrigerant circuit 320 and causes the refrigerant to flow to the outdoor heat exchanger 323. Here, the outdoor expansion valve 324 is an electric expansion valve that is connected to a liquid side of the outdoor heat exchanger 323. The outdoor unit 3 is provided with an outdoor temperature sensor 327 that detects the temperature of outdoor air that exists at the outside of the house 100, where the outdoor unit 3 is disposed, that is, an outside air temperature Ta.


In the present embodiment, the refrigerant circuit 320 is filled with a refrigerant for performing a vapor compression refrigeration cycle. The refrigerant is a mixed refrigerant containing 1,2-difluoroethylene, and any one of the refrigerants A to E above may be used.


The four-way valve 328 is a valve that switches the direction of flow of a refrigerant. At the time of the cooling operation, the four-way valve 328 connects a discharge side of the compressor 321 and a gas side of the outdoor heat exchanger 323, and connects a suction side of the compressor 321 and the gas refrigerant connection pipe 307 (a cooling operation state: refer to the solid line of the four-way valve 328 in FIG. 17). As a result, the outdoor heat exchanger 323 functions as a condenser for a refrigerant, and the indoor heat exchanger 242 functions as an evaporator for a refrigerant.


At the time of the heating operation, the four-way valve 328 connects the discharge side of the compressor 321 and the gas refrigerant connection pipe 307, and connects the suction side of the compressor 321 and the gas side of the outdoor heat exchanger 323 (a heating operation state: refer to the broken line of the four-way valve 328 in FIG. 17). As a result, the indoor heat exchanger 242 functions as a condenser for a refrigerant, and the outdoor heat exchanger 323 functions as an evaporator for a refrigerant.


(6-2) Outline of Important Structure of Air Conditioning Apparatus 1


When a heat pump heating operation is being performed, in the air conditioning apparatus 1, a refrigerant that contains at least 1,2-difluoroethylene circulates in the compressor 321, the indoor heat exchanger 242 that is a use-side heat exchanger, and the outdoor heat exchanger 323 that is a heat-source-side heat exchanger to repeat a refrigeration cycle. The indoor heat exchanger 242 causes heat to be exchanged between the indoor air F1 that is the first air, and the refrigerant. The indoor air F1 is supplied to the indoor heat exchanger 242 by the indoor fan 240. Indoor air F3 (the first air) that has been heated in the indoor heat exchanger 242 is sent to each of the rooms 101 to 104 from the indoor unit 2 via the first duct 209 to heat the rooms 101 to 104. The outdoor heat exchanger 323 causes heat to be exchanged between outdoor air that is second air, and the refrigerant. The casing 230 includes a use-side space SP2 that is connected to the first duct 209 and that accommodates the indoor heat exchanger 242, and is configured to allow the indoor air F3 that has exchanged heat with the refrigerant at the indoor heat exchanger 242 to be sent out to the first duct 209.


When a different heat source heating operation is being performed, a high-temperature combustion gas that has been sent to a furnace heat exchanger 255 exchanges heat with the indoor air F1 that is supplied by the indoor fan 240, is cooled, and becomes a low-temperature combustion gas in the furnace heat exchanger 255. The low-temperature combustion gas is discharged from the gas furnace unit 205 via a discharge pipe 257. On the other hand, the indoor air F2 that has been heated in the furnace heat exchanger 255 is sent to each of the rooms 101 to 104 from the indoor unit 2 via the first duct 209 to heat the rooms 101 to 104.


(6-3) Different Heat Source Section 270


The different heat source section 270 is constituted by the gas furnace unit 205 that is a part of the indoor unit 2 of the air conditioning equipment 80.


The gas furnace unit 205 is provided in the casing 230 that is installed in the basement 105 of the house 100. The gas furnace unit 205 is a gas-combustion heating device, and includes a fuel gas valve 251, a furnace fan 252, a combustion section 254, the furnace heat exchanger 255, an air supply pipe 256, and the discharge pipe 257.


The fuel gas valve 251 is, for example, an electromagnetic valve whose opening and closing are controllable, and is provided at a fuel gas supply pipe 258 that extends to the combustion section 254 from the outside of the casing 230. As the fuel gas, for example, natural gas or petroleum gas is used.


The furnace fan 252 is a fan that generates an airflow in which air is introduced into the combustion section 254 via the air supply pipe 256, then, the air is sent to the furnace heat exchanger 255, and the air is discharged from the discharge pipe 257. The furnace fan 252 is rotationally driven by a furnace fan motor 253.


The combustion section 254 is equipment that acquires a high-temperature combustion gas by igniting a mixed gas containing fuel gas and air by, for example, a gas burner (not shown).


The furnace heat exchanger 255 is a heat exchanger that heats air by heat dissipation of the combustion gas acquired at the combustion section 254, and functions as a different heat source heat dissipater that heats air by heat dissipation by using a heat source (here, heat by gas combustion) differing from that of the heat pump section 360.


The furnace heat exchanger 255 is disposed on an upwind side with respect to the indoor heat exchanger 242, serving as a refrigerant dissipater, in the ventilation path from the air inlet 232, formed in the casing 230, to the air outlet 231, formed in the casing 230.


(6-4) Indoor Fan 240


The indoor fan 240 is a fan for supplying air that is heated by the indoor heat exchanger 242, serving as a refrigerant heat dissipater, that constitutes the heat pump section 360 and by the furnace heat exchanger 255, serving as a different heat source dissipater, that constitutes the different heat source section 270 into the rooms 101 to 104.


In the ventilation path extending from the air inlet 232, formed in the casing 230, to the air outlet 231, formed in the casing 230, the indoor fan 240 is disposed on the upwind side with respect to both the indoor heat exchanger 242 and the furnace heat exchanger 255. The indoor fan 240 includes a blade 243 and a fan motor 244 that rotationally drives the blade 243.


(6-5) Controller 30


The indoor unit 2 is provided with an indoor-side control board 21 that controls the operation of each portion of the indoor unit 2. The outdoor unit 3 is provided with an outdoor-side control board 31 that controls the operation of each portion of the outdoor unit 3. The indoor-side control board 21 and the outdoor-side control board 31 each include, for example, a microcomputer, and each exchange, for example, control signals with a thermostat 40. Control signals are not exchanged between the indoor-side control board 21 and the outdoor-side control board 31. A control device including the indoor-side control board 21 and the outdoor-side control board 31 is called a controller 30.


(6-6) Detailed Structure of Controller 30



FIG. 18 is a block diagram showing an electrical connection state of the controller 30 and the thermostat 40 in the air conditioning apparatus 1 according to the first embodiment of the present invention. The thermostat 40 is mounted in an indoor space as with the indoor unit 2. The locations where the thermostat 40 and the indoor unit 2 are mounted may be different locations in the indoor space. The thermostat 40 is connected to a control system of the indoor unit 2 and a control system of the outdoor unit 3 by a communication line.


A transformer 20 applies a voltage of a commercial power source 90 after transformation to a usable low voltage to each of the indoor unit 2, the outdoor unit 3, and the thermostat 40 via power source lines 81 and 82.


(7) Second Embodiment

(7-1) Overall Structure


As shown in FIG. 19, an air conditioning apparatus 701 according to a second embodiment is installed on a roof 801 of a building 800, that is, on a rooftop. The air conditioning apparatus 701 is equipment that air-conditions the interior of the building 800. The building 800 includes a plurality of rooms 810. The rooms 810 of the building 800 are spaces to be air-conditioned by the air conditioning apparatus 701. FIG. 19 shows an example in which the air conditioning apparatus 701 includes one first duct 721 and one second duct 722. However, the air conditioning apparatus 701 may include a plurality of the first ducts 721 and a plurality of the second ducts 722. The first duct 721 shown in FIG. 19 is branched. The first duct 721 is provided for supply air, and the second duct 722 is provided for return air. Supply air that is supplied to the plurality of rooms 810 in the interior is first air. Return air that is introduced from the interior by the second duct 722 is also first air. In FIG. 19, arrows Ar1 and Ar2 in the first duct 721 and the second duct 722 indicate the directions in which the air flows in the first duct 721 and the second duct 722. The air is sent to the rooms 810 from the air conditioning apparatus 701 via the first duct 721, and indoor air in the rooms 810, which is air in the spaces to be air-conditioned, is sent to the air conditioning apparatus 701 via the second duct 722. A plurality of blow-out ports 723 are each provided at a boundary between the first duct 721 and a corresponding one of the rooms 810. The supply air that is supplied by the first duct 721 is blown out to the rooms 810 from the blow-out ports 723. At least one suction port 724 is provided at a boundary between the second duct 722 and a corresponding room 810. The indoor air sucked in from the suction port 724 is return air that is returned to the air conditioning apparatus 701 by the second duct 722.


(7-2) External Appearance of Air Conditioning Apparatus 701



FIG. 20 shows an external appearance of the air conditioning apparatus 701 when seen from obliquely above the air conditioning apparatus 701, and FIG. 21 shows the external appearance of the air conditioning apparatus 701 when seen from obliquely below the air conditioning apparatus 701. For convenience, the air conditioning apparatus 701 is described below by using upward, downward, forward, rearward, left, and right directions indicated by arrows in the figures. The air conditioning apparatus 701 includes a casing 730 having a shape based on a parallelepiped. The casing 730 includes metal plates that cover an upper surface 730a, a front surface 730b, a right surface 730c, a left surface 730d, a rear surface 730e, and a bottom surface 730f. The casing 730 has a third opening 733 in the upper surface 730a. The third opening 733 communicates with a heat-source-side space SP1 (see FIG. 22). A heat-source-side fan 747 that blows out air in the heat-source-side space SP1 to the outside of the casing 730 via the third opening 733 is mounted in the third opening 733. As the heat-source-side fan 747, for example, a propeller fan is used. The casing 730 has slits 734 in the front surface 730b, the left surface 730d, and the rear surface 730e. These slits 734 also communicate with the heat-source-side space SP1. Since, when the air is blown out toward the outer side of the casing 730 from the heat-source-side space SP1 by the heat-source-side fan 747, the pressure in the heat-source-side space SP1 becomes negative with respect to atmospheric pressure, outdoor air is sucked into the heat-source-side space SP1 from the outside of the casing 730 via the slits 734. The third opening 733 and the slits 734 do not communicate with a use-side space SP2 (see FIG. 22). Therefore, in an ordinary state, other than the first duct 721 and the second duct 722, there are no portions that communicate with the outside of the casing 730 from the use-side space SP2.


A bottom plate 735 having a first opening 731 and a second opening 732 is mounted on the bottom surface 730f of the casing 730. As shown in FIG. 25, the first duct 721 is connected to the first opening 731 for supply air. As shown in FIG. 25, the second duct 722 is connected to the second opening 732 for return air. Air that has returned to the use-side space SP2 of the casing 730 via the second duct 722 from the rooms 810, which are the spaces to be air conditioned, is sent to the rooms 810 via the first duct 721 from the use-side space SP2. For reinforcing the strength of the bottom plate 735, ribs 731a and 732a having a height of less than 3 cm are formed around the first opening 731 and the second opening 732 (see FIG. 23). The ribs 731a and 732a are formed integrally with the bottom plate 735 by causing a metal plate, which is a material of the bottom plate 735, to stand by press-forming thereof when the first opening 731 and the second opening 732 are formed in the bottom plate 735 by, for example, press-forming thereof.


(7-3) Internal Structure of Air Conditioning Apparatus 701


(7-3-1) Heat-Source-Side Space SP1 and Use-Side Space SP2 in Casing 730



FIG. 22 shows a state in which the metal plate covering the front surface 730b of the casing 730 and the metal plate covering the left surface 730d of the casing 730 have been removed. FIG. 23 shows a state in which the metal plate covering the right surface 730c of the casing 730 and the metal plate covering a part of the rear surface 730e have been removed. In FIG. 23, of the metal plate covering the rear surface 730e, the removed part of the metal plate covering the rear surface 730e is the metal plate covering the use-side space SP2. Therefore, the metal plate covering the rear surface 730e shown in FIG. 23 only covers the heat-source-side space SP1. FIG. 24 shows a state in which the metal plate covering the right surface 730c of the casing 730, the metal plate covering the left surface 730d, and the metal plate covering a part of the upper surface 730a have been removed, and a heat-source-side heat exchanger 743 and the heat-source-side fan 747 have been removed.


The heat-source space SP1 and the use-side space SP2 are separated by a partition plate 739. Outdoor air flows to the heat-source-side space SP1 and indoor air flows to the use-side space SP2. By separating the heat-source space SP1 and the use-side space SP2 by the partition plate 739, the flow of air between the heat-source space SP1 and the use-side space SP2 is blocked. Therefore, in an ordinary state, the indoor air and the outdoor air do not mix in the casing 730 and the interior and the exterior do not communicate with each other via the air conditioning apparatus 701.


(7-3-2) Structure in Heat-Source-Side Space SP1


The heat-source-side space SP1 accommodates, in addition to the heat-source-side fan 747, a compressor 741, a four-way valve 742, the heat-source-side heat exchanger 743, and an accumulator 746. The heat-source-side heat exchanger 743 includes a plurality of heat-transfer tubes (not shown) in which a refrigerant flows, and a plurality of heat-transfer fins (not shown) in which air flows between gaps thereof. The plurality of heat-transfer tubes are arranged in an up-down direction (hereunder may be referred to as “row direction”), and each heat-transfer tube extends in a direction substantially orthogonal to the up-down direction (in a substantially horizontal direction). The plurality of heat-transfer tubes are arranged in a plurality of columns in order from a side close to the casing 730. At an end portion of the heat-source-side heat exchanger 743, for example, the heat-transfer tubes are connected to each other by being bent into a U shape or by using a U-shaped tube so that the flow of a refrigerant from a certain column to another column and/or a certain row to another row is turned back. The plurality of heat-transfer fins that extend so as to be long in the up-down direction are arranged side by side in a direction in which the heat-transfer tubes extend with a predetermined interval between the plurality of heat-transfer fins. The plurality of heat-transfer fins and the plurality of heat-transfer tubes are assembled to each other so that each heat-transfer fin extends through the plurality of heat-transfer tubes. The plurality of heat-transfer fins are also disposed in a plurality of columns.


In top view, the heat-source-side heat exchanger 743 has a C shape, and is disposed opposite to the front surface 730b, the left surface 730d, and the rear surface 730e of the casing 730. A portion that is not surrounded by the heat-source-side heat exchanger 743 is a portion that is opposite to the partition plate 739. Side end portions that are two ends of the C shape are disposed near the partition plate 739, and a portion between the two end portions of the heat-source-side heat exchanger 743 and the partition plate 739 is closed by a metal plate (not shown) that blocks air passage. The height of the heat-source-side heat exchanger 743 is substantially the same as the height from the bottom surface 730f to the upper surface 730a of the casing 730. Due to such a structure, a flow path of air that enters from the slits 734, passes through the heat-source-side heat exchanger 743, and exits from the third opening 733 is formed. When outdoor air sucked into the heat-source-side space SP1 via the slits 734 passes through the heat-source-side heat exchanger 743, the outdoor air exchanges heat with a refrigerant that flows in the heat-source-side heat exchanger 743. Air after the heat exchange by the heat-source-side heat exchanger 743 is discharged to the outside of the casing 730 from the third opening 733 by the heat-source-side fan 747.


(7-3-3) Structure in Use-Side Space SP2


An expansion valve 744, a use-side heat exchanger 745, and a use-side fan 748 are disposed in the use-side space SP2. As the use-side fan 748, for example, a centrifugal fan is used. As a centrifugal fan, for example, a sirocco fan exists. The expansion valve 744 may be disposed in the heat-source-side space SP1. As shown in FIG. 23, the use-side fan 748 is disposed above the first opening 731 by a support base 751. As shown in FIG. 29, in top view, a blow-out port 748b of the use-side fan 748 is disposed at a location so as not to overlap the first opening 731. Since portions other than the blow-out port 748b of the use-side fan 748 and the first opening 731 are surrounded by the support base 751 and the casing 730, substantially the entire air that is blown out from the blow-out port 748b of the use-side fan 748 is supplied into the interior via the first duct 721 from the first opening 731.


The use-side heat exchanger 745 includes a plurality of heat-transfer tubes 745a (see FIG. 28) in which a refrigerant flows, and a plurality of heat-transfer fins (not shown) in which air flows between gaps thereof. The plurality of heat-transfer tubes 745a are arranged in an up-down direction (row direction), and each heat-transfer tube 745a extends in a direction substantially orthogonal to the up-down direction (in the second embodiment, in a left-right direction). Here, a refrigerant flows in the left-right direction in the plurality of heat-transfer tubes 745a. The plurality of heat-transfer tubes 745a are provided in a plurality of columns in a front-rear direction. At an end portion of the use-side heat exchanger 745, for example, the heat-transfer tubes 745a are connected to each other by being bent into a U shape or by using a U-shaped tube so that the flow of a refrigerant from a certain column to another column and/or a certain row to another row is turned back. The plurality heat-transfer fins that extend so as to be long in the left-right direction are arranged in a direction in which the heat-transfer tubes 745a extend with a predetermined interval between the plurality of heat-transfer fins. The plurality of heat-transfer fins and the plurality of heat-transfer tubes 745a are assembled to each other so that each heat-transfer fin extends through the plurality of heat-transfer tubes 745a. For example, a copper tube is used for each heat-transfer tube 745a that constitutes the use-side heat exchanger 745 and aluminum may be used for each heat-transfer fin.


The use-side heat exchanger 745 has a shape that is short in the front-rear direction and long in the up-down direction and the left-right direction. A drain pan 752 has a shape like a shape formed by removing an upper surface of a parallelepiped that extends so as to be long in the left-right direction. In top view, the drain pan 752 has a front-rear-direction dimension that is longer than a front-rear length of the use-side heat exchanger 745. The use-side heat exchanger 745 is fitted in such a drain pan 752. The drain pan 752 receives dew condensation water that is produced at the use-side heat exchanger 745 and that falls dropwise downward. The drain pan 752 extends to the partition plate 739 from the right surface 730c of the casing 730. A drainage port 752a of the drain pan 752 extends through the right surface 730c of the casing 730, and the dew condensation water received by the drain pan 752 passes through the drainage port 752a and is caused to drain away to the outside of the casing 730.


The use-side heat exchanger 745 extends up to the vicinity of the partition plate 739 from the vicinity of the right surface 730c of the casing 730. A portion between the right surface 730c of the casing 730 and a right portion 745c of the use-side heat exchanger 745 and a portion between the partition plate 739 and a left portion 745d of the use-side heat exchanger 745 are closed by metal plates. The drain pan 752 is supported by a support frame 736 at a height h1 from the bottom plate 735 so as to be upwardly separated from the bottom plate 735. A support of the use-side heat exchanger 745 includes rod-shaped frame members combined around the upper, lower, left, and right sides of the use-side heat exchanger 745, and is helped by an auxiliary frame 753 that is directly or indirectly fixed to the casing 730 and the partition plate 739. A portion between the use-side heat exchanger 745 and the upper surface 730a of the casing 730 is closed by the use-side heat exchanger 745 itself or the auxiliary frame 753. An opening portion between the use-side heat exchanger 745 and the bottom plate 735 is closed by the support base 751 and the drain pan 752.


In this way, the use-side heat exchanger 745 divides the use-side space SP2 into a space on an upstream side with respect to the use-side heat exchanger 745 and a space on a downstream side with respect to the use-side heat exchanger 745. All air that flows to the downstream side from the upstream side with respect to the use-side heat exchanger 745 passes through the use-side heat exchanger 745. The use-side fan 748 is disposed in the space on the downstream side with respect to the use-side heat exchanger 745 and causes an airflow that passes through the use-side heat exchanger 745 to be generated. The support base 751 that has been already described further divides the space on the downstream side with respect to the use-side heat exchanger 745 into a space on a suction side of the use-side fan 748 and a space on a blow-out side of the use-side fan 748.


(7-3-4) Refrigerant Circuit



FIG. 26 illustrates a refrigerant circuit 711 that is formed in the air conditioning apparatus 701. The refrigerant circuit 711 includes the use-side heat exchanger 745 and the heat-source-side heat exchanger 743. In the refrigerant circuit 711, a refrigerant circulates between the use-side heat exchanger 745 and the heat-source-side heat exchanger 743. In the refrigerant circuit 711, when, in a cooling operation or a heating operation, a vapor compression refrigeration cycle is performed, heat is exchanged at the use-side heat exchanger 745 and the heat-source-side heat exchanger 743. In FIG. 26, an arrow Ar3 denotes supply air which is an airflow that is on the downstream side with respect to the use-side heat exchanger 745 and that is blown out from the use-side fan 748, and an arrow Ar4 denotes return air which is an airflow that is on the upstream side with respect to the use-side heat exchanger 745. An arrow Ar5 denotes an airflow that is on a downstream side with respect to the heat-source-side heat exchanger 743 and that is blown out from the third opening 733 by the heat-source-side fan 747, and an arrow Ar6 denotes an airflow that is on an upstream side with respect to the heat-source-side heat exchanger 743 and that is sucked from the slits 734 by the heat-source-side fan 747.


The refrigerant circuit 711 includes the compressor 741, the four-way valve 742, the heat-source-side heat exchanger 743, the expansion valve 744, the use-side heat exchanger 745, and the accumulator 746. The four-way valve 742 is switched to a connection state indicated by a solid line at the time of the cooling operation, and is switched to a connection state indicated by a broken line at the time of the heating operation.


At the time of the cooling operation, a gas refrigerant compressed by the compressor 741 passes through the four-way valve 742 and is sent to the heat-source-side heat exchanger 743. The refrigerant dissipates heat to outdoor air at the heat-source-side heat exchanger 743, passes along a refrigerant pipe 712, and is sent to the expansion valve 744. At the expansion valve 744, the refrigerant expands and is decompressed, passes along the refrigerant pipe 712, and is sent to the use-side heat exchanger 745. A refrigerant having a low temperature and a low pressure sent from the expansion valve 744 exchanges heat at the use-side heat exchanger 745, and takes away heat from indoor air. The air cooled by having its heat taken away at the use-side heat exchanger 745 passes through the first duct 721 and is supplied to the rooms 810. The gas refrigerant after the heat exchange at the use-side heat exchanger 745 or a gas-liquid two-phase refrigerant passes through a refrigerant pipe 713, the four-way valve 742, and the accumulator 746, and is sucked into the compressor 741.


At the time of the heating operation, a gas refrigerant compressed at the compressor 741 passes through the four-way valve 742 and the refrigerant pipe 713 and is sent to the use-side heat exchanger 745. The refrigerant exchanges heat with indoor air at the use-side heat exchanger 745 and applies heat to the indoor air. The air heated by the application of heat at the use-side heat exchanger 745 passes through the first duct 721 and is supplied to the rooms 810. The refrigerant after the heat exchange at the use-side heat exchanger 745 passes along the refrigerant pipe 712 and is sent to the expansion valve 744. A refrigerant having a low temperature and a low pressure that has expanded and that has been decompressed at the expansion valve 744 passes along the refrigerant pipe 712, is sent to the heat-source-side heat exchanger 743, exchanges heat at the heat-source-side heat exchanger 743, and acquires heat from outdoor air. The gas refrigerant after the heat exchange at the heat-source-side heat exchanger 743 or a gas-liquid two-phase refrigerant passes through the four-way valve 742 and the accumulator 746, and is sucked into the compressor 741.


(7-3-5) Control System



FIG. 27 illustrates, for example, a main controller 760 that controls the air conditioning apparatus 701 and main pieces of equipment that are controlled by the main controller 760. The main controller 760 controls the compressor 741, the four-way valve 742, the heat-source-side fan 747, and the use-side fan 748. The main controller 760 is configured to be capable of communicating with a remote controller 762. A user can send, for example, set values of indoor temperatures of the rooms 810 to the main controller 760 from the remote controller 762.


For controlling the air conditioning apparatus 701, a plurality of temperature sensors for measuring the temperature of a refrigerant at each portion of the refrigerant circuit 711 and/or a pressure sensor that measures the pressure of each portion and a temperature sensor for measuring the air temperature of each location are provided.


The main controller 760 performs at least on/off control of the compressor 741, on/off control of the heat-source-side fan 747, and on/off control of the use-side fan 748. When any or all of the compressor 741, the heat-source-side fan 747, and the use-side fan 748 include a motor of a type whose number of rotations is changeable, the main controller 760 may be configured to be capable of controlling the number of rotations of the motor or motors whose number of rotations is changeable among the motors of the compressor 741, the heat-source-side fan 747, and the use-side fan 748. In this case, the main controller 760 can control the circulation amount of the refrigerant that flows through the refrigerant circuit 711 by changing the number of rotations of the motor of the compressor 741. The main controller 760 can change the flow rate of outdoor air that flows between the heat-transfer fins of the heat-source-side heat exchanger 743 by changing the number of rotations of the motor of the heat-source-side fan 747. The main controller 760 can change the flow rate of indoor air that flows between the heat-transfer fins of the use-side heat exchanger 745 by changing the number of rotations of the motor of the use-side fan 748.


A refrigerant leakage sensor 761 is connected to the main controller 760. When the concentration of a refrigerant gas that has leaked into air becomes greater than or equal to a detected lower limit concentration, the refrigerant leakage sensor 761 sends a signal indicating the detection of the leakage of the gas refrigerant to the main controller 760.


The main controller 760 is realized by, for example, a computer. The computer that constitutes the main controller 760 includes a control calculation device and a storage device. For the control calculation device, a processor such as a CPU or a GPU may be used. The control calculation device reads a program that is stored in the storage device and performs a predetermined image processing operation and a computing processing operation in accordance with the program. Further, the control calculation device writes a calculated result to the storage device and reads information stored in the storage device in accordance with the program. However, the main controller 760 may be formed by using an integrated circuit (IC) that can perform control similar to the control that is performed by using a CPU and a memory. Here, IC includes, for example, LSI (large-scale integrated circuit), ASIC (application-specific integrated circuit), a gate array, and FPGA (field programmable gate array).


In the present embodiment, the refrigerant circuit 711 is filled with a refrigerant for performing a vapor compression refrigeration cycle. The refrigerant is a mixed refrigerant containing 1,2-difluoroethylene, and any one of the refrigerants A to E above may be used.


(8) Third Embodiment


FIG. 30 illustrates a structure of an air conditioning apparatus 601 according to a third embodiment. The air conditioning apparatus 601 is configured to perform indoor ventilation and humidity conditioning. A sensible heat exchanger 622 is provided in a central portion inside a casing 621 of the air conditioning apparatus 601. The sensible heat exchanger 622 does not exchange moisture between circulating air and circulating air. The sensible heat exchanger 622 has the function of exchanging sensible heat.


The air conditioning apparatus 601 includes a compressor 633, an outdoor heat exchanger 634 that is a heat-source-side heat exchanger, an air supply heat exchanger 625 that is a use-side heat exchanger, an air supply duct 651 that supplies supply air SA to a plurality of rooms in an interior, a return-air duct 652 that introduces indoor air RA from the interior, a suction duct 653 that introduces outdoor air OA from an exterior, and the casing 621. First air before heat exchange with a refrigerant at the air supply heat exchanger 625 is the outdoor air OA, and first air after the heat exchange with the refrigerant at the air supply heat exchanger 625 is the supply air SA. Outdoor air that is subjected to heat exchange at the outdoor heat exchanger 634 is second air. The outdoor air that is the second air and the outdoor air OA that is the first air differ from each other.


A refrigerant that contains at least 1,2-difluoroethylene circulates in the compressor 633, the air supply heat exchanger 625, and the outdoor heat exchanger 634, and a refrigeration cycle is repeated. More specifically, the refrigerant is compressed at the compressor 633, is condensed at the outdoor heat exchanger 634, is decompressed at a capillary tube 636, and is evaporated at the air supply heat exchanger 625. An evaporation valve may be used instead of the capillary tube 636.


A space including an air supply passage 641 and an outside air passage 643 in the casing 621 is a use-side space that is connected to the air supply duct 651 and that accommodates the air supply heat exchanger 625. The casing 621 is configured to be capable of allowing the supply air SA (the first air) after the heat exchange with the refrigerant at the air supply heat exchanger 625 to be sent out to the air supply duct 651. The air supply duct 651 is a first duct, and the suction duct 653 is a third duct.


Looking at it differently, the air conditioning apparatus 601 may be regarded as including a use-side unit 602 and a heat-source-side unit 603. The use-side unit 602 and the heat-source-side unit 603 are different units. The use-side unit 602 includes the casing 621, the sensible heat exchanger 622, the air supply heat exchanger 625, an exhaust fan 627, an air supply fan 628, and a humidifier 629. The heat-source-side unit 603 includes the compressor 633, the outdoor heat exchanger 634, and the capillary tube 636. The use-side unit 602 is configured to guide the outdoor air OA that is the first air introduced from the exterior to the air supply heat exchanger 625 that is a use-side heat exchanger with the casing 621 connected to the suction duct 653 that is the third duct.


The air supply passage 641 and a suction passage 644 are formed closer than the sensible heat exchanger 622 to an indoor side. An exhaust passage 642 and the outside air passage 643 are formed closer than the sensible heat exchanger 622 to an outdoor side. The air supply fan 628 and the humidifier 629 are provided in the air supply passage 641. The exhaust fan 627 is provided in the exhaust passage 642. The air supply heat exchanger 625 is provided in the outside air passage 643. The air supply heat exchanger 625 is connected to the heat-source-side unit 603. The compressor 633, the outdoor heat exchanger 634, and the capillary tube 636 that constitute a refrigerant circuit 610 along with the air supply heat exchanger 625 are provided in the heat-source-side unit 603. The compressor 633, the outdoor heat exchanger 634, and the capillary tube 636 are connected to a refrigerant pipe 645. An outdoor fan (not shown) is provided in parallel with the outdoor heat exchanger 634. In the air conditioning apparatus 601, the indoor air RA is sucked into the suction passage 644 by driving the exhaust fan 627, and the outdoor air OA is sucked into the outside air passage 643 by driving the air supply fan 628. At this time, the outdoor air OA sucked into the outside air passage 643 is cooled and dehumidified at the air supply heat exchanger 625 that functions as an evaporator, and reaches the sensible heat exchanger 622. In the sensible heat exchanger 622, the outdoor air OA exchanges sensible heat with the indoor air RA sucked into the suction passage 644. Due to the sensible heat exchange, the outdoor air OA is kept dehumidified and only its temperature becomes substantially equal to the temperature of the indoor air RA. The outdoor air OA is supplied into the interior as the supply air SA. On the other hand, the indoor air RA cooled at the sensible heat exchanger 622 is discharged to the exterior as exhaust EA.


The air conditioning apparatus 601 of the third embodiment cools the outdoor air OA at the air supply heat exchanger 625. The air cooled at the air supply heat exchanger 625 reaches the sensible heat exchanger 622. The air conditioning apparatus 601 causes the air cooled at the air supply heat exchanger 625 and the indoor air RA to exchange sensible heat at the sensible heat exchanger 622. The air conditioning apparatus 601 supplies the air that has exchanged sensible heat with the indoor air RA to be subsequently supplied as the supply air SA to the interior.


However, the structure of introducing the outdoor air is not limited thereto. For example, the air conditioning apparatus previously causes the outdoor air OA and the indoor air RA to exchange sensible heat at the sensible heat exchanger. Then, the air conditioning apparatus cools the air that has exchanged sensible heat with the indoor air RA at the use-side heat exchanger. The air conditioning apparatus supplies the air cooled at the use-side heat exchanger as the supply air SA into the interior.


The air conditioning apparatus may be configured to heat the outdoor air OA and supply the outdoor air OA into the interior so as to deal with seasons having low outdoor air temperatures. Such an air conditioning apparatus causes, for example, the outdoor air OA and the indoor air RA to exchange sensible heat at the sensible heat exchanger. The air conditioning apparatus then heats the air that has exchanged sensible heat with the indoor air RA at the use-side heat exchanger. The air conditioning apparatus supplies the air heated at the use-side heat exchanger as the supply air SA into the interior.


Since the air conditioning apparatus has a structure such as that described above, the outdoor air OA whose temperature has been previously adjusted at the sensible heat exchanger can be cooled or heated at the use-side heat exchanger afterwards, so that it is possible to increase the refrigeration cycle efficiency.


In the present embodiment, the refrigerant circuit 610 is filled with a refrigerant for performing a vapor compression refrigeration cycle. The refrigerant is a mixed refrigerant containing 1,2-difluoroethylene, and any one of the refrigerants A to E above may be used.


(9) Features

The air conditioning apparatus (1, 601, 701) of the first embodiment, the second embodiment, and the third embodiment above each include the compressor (321, 633, 741), the indoor heat exchanger 242, the air supply heat exchanger 625 or the use-side heat exchanger 745, the outdoor heat exchanger (323, 634) or the heat-source-side heat exchanger 743, any one of the refrigerants A to E, the first duct (209, 721) or the air supply duct 651, and the casing (230, 621, 730).


The indoor heat exchanger 242, the air supply heat exchanger 625, or the use-side heat exchanger 745 is a use-side heat exchanger that exchanges heat with the first air. The outdoor heat exchanger (323, 634) or the heat-source-side heat exchanger 743 is a heat-source-side heat exchanger that exchanges heat with the second air. The first duct (209, 721) or the air supply duct 651 is a first duct that supplies the first air into the plurality of rooms (101 to 104, 810). The refrigerants A to E contain at least 1,2-difluoroethylene, and circulate in the compressor, the use-side heat exchanger, and the heat-source-side heat exchanger to repeat the refrigeration cycle. The casings (230, 621, 730) each include the use-side space SP2 that is connected to the first duct (209, 721) or the air supply duct 651 and that accommodates the indoor heat exchanger 242, the air supply heat exchanger 625, or the use-side heat exchanger 745, and is configured to allow the first air after heat exchange with a refrigerant at the indoor heat exchanger 242, the air supply heat exchanger 625, or the use-side heat exchanger 745 to be sent out to the first duct (209, 721) or the air supply duct 651.


Since the air conditioning apparatus (1, 601, 701) having such a structure each supply the first air after heat exchange to the plurality of rooms via the first duct (209, 721) or the air supply duct 651, the structures of the refrigerant circuits (320, 711, 610) are simplified. Therefore, it is possible to reduce the amount of refrigerant with which the air conditioning apparatus (1, 601, 701) are filled.


Although the embodiments of the present disclosure are described above, it is to be understood that various changes may be made in the forms and details without departing from the spirit and the scope of the present disclosure described in the claims.


REFERENCE SIGNS LIST






    • 1, 601, 701 air conditioning apparatus


    • 2 indoor unit (example of use-side unit)


    • 3 outdoor unit (example of heat-source-side unit)


    • 209, 721 first duct


    • 210, 722 second duct


    • 230, 621, 730 casing


    • 242 indoor heat exchanger (example of use-side heat exchanger)


    • 321, 633, 741 compressor


    • 323, 634 outdoor heat exchanger (example of heat-source-side heat exchanger)


    • 602 use-side unit


    • 603 heat-source-side unit


    • 625 air supply heat exchanger (example of use-side heat exchanger)


    • 651 air supply duct (example of first duct)


    • 653 suction duct (example of third duct)


    • 739 partition plate


    • 743 heat-source-side heat exchanger


    • 745 use-side heat exchanger





CITATION LIST
Patent Literature



  • [Patent Literature 1] Japanese Unexamined Patent Application Publication No. 2018-25377


Claims
  • 1. An air conditioning apparatus comprising: a compressor;a use-side heat exchanger that exchanges heat with first air;a heat-source-side heat exchanger that exchanges heat with second air;a refrigerant that circulates in the compressor, the use-side heat exchanger, and the heat-source-side heat exchanger to repeat a refrigeration cycle;a first duct that supplies the first air to a plurality of rooms in an interior; anda casing that includes a use-side space that is connected to the first duct and that accommodates the use-side heat exchanger, the casing being configured to allow the first air after heat exchange with the refrigerant at the use-side heat exchanger to be sent out to the first duct,wherein the refrigerant comprises trans-1,2-difluoroethylene (HFO-1132(E)), trifluoroethylene (HFO-1123), and 2,3,3,3-tetrafluoro-1-propene (R1234yf), andwherein 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:
  • 2. The air conditioning apparatus according to claim 1, comprising: a second duct that introduces the first air from the interior;a use-side unit that includes the casing and that is configured to guide the first air introduced from the interior to the use-side heat exchanger with the casing connected to the second duct; anda heat-source-side unit that accommodates the heat-source-side heat exchanger and that differs from the use-side unit.
  • 3. The air conditioning apparatus according to claim 1, comprising: a third duct that introduces the first air from an exterior;a use-side unit that includes the casing and that is configured to guide the first air introduced from the exterior to the use-side heat exchanger with the casing connected to the third duct; anda heat-source-side unit that accommodates the heat-source-side heat exchanger and that differs from the use-side unit.
  • 4. The air conditioning apparatus according to claim 1, comprising: a second duct that is connected to the casing and that supplies the first air introduced from the interior to the use-side space,wherein the casing is provided with a partition plate that partitions the casing (730) into a heat-source-side space through which the second air introduced from an exterior passes and the use-side space to prevent circulation of air in the heat-source-side space and the use-side space, andwherein the heat-source-side heat exchanger is disposed in the heat-source-side space.
  • 5. An air conditioning apparatus comprising: a compressor;a use-side heat exchanger that exchanges heat with first air;a heat-source-side heat exchanger that exchanges heat with second air;a refrigerant that circulates in the compressor, the use-side heat exchanger, and the heat-source-side heat exchanger to repeat a refrigeration cycle;a first duct that supplies the first air to a plurality of rooms in an interior; anda casing that includes a use-side space that is connected to the first duct and that accommodates the use-side heat exchanger, the casing being configured to allow the first air after heat exchange with the refrigerant at the use-side heat exchanger to be sent out to the first duct,wherein the refrigerant comprises trans-1,2-difluoroethylene (HFO-1132(E)), difluoromethane (R32), and 2,3,3,3-tetrafluoro-1-propene (R1234yf), andwherein 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:
  • 6. The air conditioning apparatus according to claim 5, comprising: a second duct that introduces the first air from the interior;a use-side unit that includes the casing and that is configured to guide the first air introduced from the interior to the use-side heat exchanger with the casing connected to the second duct; anda heat-source-side unit that accommodates the heat-source-side heat exchanger and that differs from the use-side unit.
  • 7. The air conditioning apparatus according to claim 5, comprising: a third duct that introduces the first air from an exterior;a use-side unit that includes the casing and that is configured to guide the first air introduced from the exterior to the use-side heat exchanger with the casing connected to the third duct; anda heat-source-side unit that accommodates the heat-source-side heat exchanger and that differs from the use-side unit.
  • 8. The air conditioning apparatus according to claim 5, comprising: a second duct that is connected to the casing and that supplies the first air introduced from the interior to the use-side space,wherein the casing is provided with a partition plate that partitions the casing (730) into a heat-source-side space through which the second air introduced from an exterior passes and the use-side space to prevent circulation of air in the heat-source-side space and the use-side space, andwherein the heat-source-side heat exchanger is disposed in the heat-source-side space.
  • 9. An air conditioning apparatus comprising: a compressor;a use-side heat exchanger that exchanges heat with first air;a heat-source-side heat exchanger that exchanges heat with second air;a refrigerant that circulates in the compressor, the use-side heat exchanger, and the heat-source-side heat exchanger to repeat a refrigeration cycle;a first duct that supplies the first air to a plurality of rooms in an interior; anda casing that includes a use-side space that is connected to the first duct and that accommodates the use-side heat exchanger, the casing being configured to allow the first air after heat exchange with the refrigerant at the use-side heat exchanger to be sent out to the first duct,wherein the refrigerant comprises trans-1,2-difluoroethylene (HFO-1132(E)), difluoromethane (R32), and 2,3,3,3-tetrafluoro-1-propene (R1234yf), andwherein 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:
  • 10. The air conditioning apparatus according to claim 9, comprising: a second duct that introduces the first air from the interior;a use-side unit that includes the casing and that is configured to guide the first air introduced from the interior to the use-side heat exchanger with the casing connected to the second duct; anda heat-source-side unit that accommodates the heat-source-side heat exchanger and that differs from the use-side unit.
  • 11. The air conditioning apparatus according to claim 9, comprising: a third duct that introduces the first air from an exterior;a use-side unit that includes the casing and that is configured to guide the first air introduced from the exterior to the use-side heat exchanger with the casing connected to the third duct; anda heat-source-side unit that accommodates the heat-source-side heat exchanger and that differs from the use-side unit.
  • 12. The air conditioning apparatus according to claim 9, comprising: a second duct that is connected to the casing and that supplies the first air introduced from the interior to the use-side space,wherein the casing is provided with a partition plate that partitions the casing (730) into a heat-source-side space through which the second air introduced from an exterior passes and the use-side space to prevent circulation of air in the heat-source-side space and the use-side space, andwherein the heat-source-side heat exchanger is disposed in the heat-source-side space.
  • 13. An air conditioning apparatus comprising: a compressor;a use-side heat exchanger that exchanges heat with first air;a heat-source-side heat exchanger that exchanges heat with second air;a refrigerant that circulates in the compressor, the use-side heat exchanger, and the heat-source-side heat exchanger to repeat a refrigeration cycle;a first duct that supplies the first air to a plurality of rooms in an interior; anda casing that includes a use-side space that is connected to the first duct and that accommodates the use-side heat exchanger, the casing being configured to allow the first air after heat exchange with the refrigerant at the use-side heat exchanger to be sent out to the first duct,wherein the refrigerant comprises trans-1,2-difluoroethylene (HFO-1132(E)), difluoromethane (R32), and 2,3,3,3-tetrafluoro-1-propene (R1234yf), andwherein 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:
  • 14. The air conditioning apparatus according to claim 13, comprising: a second duct that introduces the first air from the interior;a use-side unit that includes the casing and that is configured to guide the first air introduced from the interior to the use-side heat exchanger with the casing connected to the second duct; anda heat-source-side unit that accommodates the heat-source-side heat exchanger and that differs from the use-side unit.
  • 15. The air conditioning apparatus according to claim 13, comprising: a third duct that introduces the first air from an exterior;a use-side unit that includes the casing and that is configured to guide the first air introduced from the exterior to the use-side heat exchanger with the casing connected to the third duct; anda heat-source-side unit that accommodates the heat-source-side heat exchanger and that differs from the use-side unit.
  • 16. The air conditioning apparatus according to claim 13, comprising: a second duct that is connected to the casing and that supplies the first air introduced from the interior to the use-side space,wherein the casing is provided with a partition plate that partitions the casing (730) into a heat-source-side space through which the second air introduced from an exterior passes and the use-side space to prevent circulation of air in the heat-source-side space and the use-side space, andwherein the heat-source-side heat exchanger is disposed in the heat-source-side space.
  • 17. An air conditioning apparatus comprising: a compressor;a use-side heat exchanger that exchanges heat with first air;a heat-source-side heat exchanger that exchanges heat with second air;a refrigerant that circulates in the compressor, the use-side heat exchanger, and the heat-source-side heat exchanger to repeat a refrigeration cycle;a first duct that supplies the first air to a plurality of rooms in an interior; anda casing that includes a use-side space that is connected to the first duct and that accommodates the use-side heat exchanger, the casing being configured to allow the first air after heat exchange with the refrigerant at the use-side heat exchanger to be sent out to the first duct,wherein the refrigerant comprises trans-1,2-difluoroethylene (HFO-1132(E)), difluoromethane (R32), and 2,3,3,3-tetrafluoro-1-propene (R1234yf), andwherein 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:
  • 18. The air conditioning apparatus according to claim 17, comprising: a second duct that introduces the first air from the interior;a use-side unit that includes the casing and that is configured to guide the first air introduced from the interior to the use-side heat exchanger with the casing connected to the second duct; anda heat-source-side unit that accommodates the heat-source-side heat exchanger and that differs from the use-side unit.
  • 19. The air conditioning apparatus according to claim 17, comprising: a third duct that introduces the first air from an exterior;a use-side unit that includes the casing and that is configured to guide the first air introduced from the exterior to the use-side heat exchanger with the casing connected to the third duct; anda heat-source-side unit that accommodates the heat-source-side heat exchanger and that differs from the use-side unit.
  • 20. The air conditioning apparatus according to claim 17, comprising: a second duct that is connected to the casing and that supplies the first air introduced from the interior to the use-side space,wherein the casing is provided with a partition plate that partitions the casing (730) into a heat-source-side space through which the second air introduced from an exterior passes and the use-side space to prevent circulation of air in the heat-source-side space and the use-side space, andwherein the heat-source-side heat exchanger is disposed in the heat-source-side space.
  • 21. An air conditioning apparatus comprising: a compressor;a use-side heat exchanger that exchanges heat with first air;a heat-source-side heat exchanger that exchanges heat with second air;a refrigerant that circulates in the compressor, the use-side heat exchanger, and the heat-source-side heat exchanger to repeat a refrigeration cycle;a first duct that supplies the first air to a plurality of rooms in an interior; anda casing that includes a use-side space that is connected to the first duct and that accommodates the use-side heat exchanger, the casing being configured to allow the first air after heat exchange with the refrigerant at the use-side heat exchanger to be sent out to the first duct,wherein the refrigerant comprises trans-1,2-difluoroethylene (HFO-1132(E)), difluoromethane (R32), and 2,3,3,3-tetrafluoro-1-propene (R1234yf), andwherein 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:
  • 22. The air conditioning apparatus according to claim 21, comprising: a second duct that introduces the first air from the interior;a use-side unit that includes the casing and that is configured to guide the first air introduced from the interior to the use-side heat exchanger with the casing connected to the second duct; anda heat-source-side unit that accommodates the heat-source-side heat exchanger and that differs from the use-side unit.
  • 23. The air conditioning apparatus according to claim 21, comprising: a third duct that introduces the first air from an exterior;a use-side unit that includes the casing and that is configured to guide the first air introduced from the exterior to the use-side heat exchanger with the casing connected to the third duct; anda heat-source-side unit that accommodates the heat-source-side heat exchanger and that differs from the use-side unit.
  • 24. The air conditioning apparatus according to claim 21, comprising: a second duct that is connected to the casing and that supplies the first air introduced from the interior to the use-side space,wherein the casing is provided with a partition plate that partitions the casing (730) into a heat-source-side space through which the second air introduced from an exterior passes and the use-side space to prevent circulation of air in the heat-source-side space and the use-side space, andwherein the heat-source-side heat exchanger is disposed in the heat-source-side space.
Priority Claims (9)
Number Date Country Kind
JP2017-242183 Dec 2017 JP national
JP2017-242185 Dec 2017 JP national
JP2017-242186 Dec 2017 JP national
JP2017-242187 Dec 2017 JP national
PCT/JP2018/037483 Oct 2018 WO international
PCT/JP2018/038746 Oct 2018 WO international
PCT/JP2018/038747 Oct 2018 WO international
PCT/JP2018/038748 Oct 2018 WO international
PCT/JP2018/038749 Oct 2018 WO international
US Referenced Citations (101)
Number Name Date Kind
5185092 Fukuda et al. Feb 1993 A
5344069 Narikiyo Sep 1994 A
5851968 Schnur Dec 1998 A
6591631 Taira Jul 2003 B1
6667285 Kawahara et al. Dec 2003 B1
8358040 Komuro et al. Jan 2013 B2
10131827 Fukushima et al. Nov 2018 B2
10883745 Higashiiue et al. Jan 2021 B2
20020140309 Yanashima et al. Oct 2002 A1
20020193262 Kaimai et al. Dec 2002 A1
20040011062 Taira Jan 2004 A1
20060000224 Matsuoka Jan 2006 A1
20070209373 Taira et al. Sep 2007 A1
20080184723 Sato et al. Aug 2008 A1
20080184731 Sienel et al. Aug 2008 A1
20080188173 Chen et al. Aug 2008 A1
20090260382 Takeichi et al. Oct 2009 A1
20100067264 Ohashi et al. Mar 2010 A1
20100082162 Mundy Apr 2010 A1
20100122545 Minor et al. May 2010 A1
20110108756 Tsuchiya et al. May 2011 A1
20110167848 Wakashima et al. Jul 2011 A1
20120260679 Huerta-Ochoa Oct 2012 A1
20140070132 Fukushima Mar 2014 A1
20140077123 Fukushima Mar 2014 A1
20140291411 Tamaki et al. Oct 2014 A1
20140314606 Maeyama et al. Oct 2014 A1
20140373569 Tsuboe et al. Dec 2014 A1
20150001981 Hattori et al. Jan 2015 A1
20150075203 Mochizuki et al. Mar 2015 A1
20150096321 Kawano et al. Apr 2015 A1
20150143841 Kawano et al. May 2015 A1
20150256038 Nigo et al. Sep 2015 A1
20150362199 Yumoto et al. Dec 2015 A1
20150376486 Hashimoto Dec 2015 A1
20160018135 Yuzawa et al. Jan 2016 A1
20160075927 Fukushima Mar 2016 A1
20160131378 Hinokuma et al. May 2016 A1
20160276886 Baba et al. Sep 2016 A1
20160333241 Fukushima et al. Nov 2016 A1
20160333243 Fukushima et al. Nov 2016 A1
20160340565 Tasaka et al. Nov 2016 A1
20160348933 Takeuchi et al. Dec 2016 A1
20160355719 Fukushima et al. Dec 2016 A1
20170002245 Fukushima Jan 2017 A1
20170058172 Fukushima et al. Mar 2017 A1
20170058173 Fukushima Mar 2017 A1
20170058174 Fukushima et al. Mar 2017 A1
20170121581 Horiike et al. May 2017 A1
20170138642 Ueno May 2017 A1
20170166831 Matsumoto Jun 2017 A1
20170248328 Eskew et al. Aug 2017 A1
20170328586 Maeyama Nov 2017 A1
20170336085 Yasuo et al. Nov 2017 A1
20170338707 Shono et al. Nov 2017 A1
20180051198 Okamoto Feb 2018 A1
20180094844 Suzuki Apr 2018 A1
20180138763 Nakamura et al. May 2018 A1
20180156217 Sakima et al. Jun 2018 A1
20180156511 Chikami et al. Jun 2018 A1
20180254676 Nigo et al. Sep 2018 A1
20180299175 Hayamizu et al. Oct 2018 A1
20180320942 Hayamizu et al. Nov 2018 A1
20180331436 Hayamizu et al. Nov 2018 A1
20180358861 Hayamizu et al. Dec 2018 A1
20190063773 Nagahashi et al. Feb 2019 A1
20190068015 Yabe et al. Feb 2019 A1
20190309963 Zaki et al. Oct 2019 A1
20200079985 Okamoto et al. Mar 2020 A1
20200321816 Watanabe Oct 2020 A1
20200325375 Kumakura et al. Oct 2020 A1
20200325376 Kumakura et al. Oct 2020 A1
20200325377 Kumakura et al. Oct 2020 A1
20200326100 Ukibune et al. Oct 2020 A1
20200326101 Itano et al. Oct 2020 A1
20200326102 Kumakura et al. Oct 2020 A1
20200326103 Kumakura et al. Oct 2020 A1
20200326105 Kumakura et al. Oct 2020 A1
20200326109 Kumakura et al. Oct 2020 A1
20200326110 Asano et al. Oct 2020 A1
20200332164 Itano et al. Oct 2020 A1
20200332166 Kumakura et al. Oct 2020 A1
20200333041 Itano et al. Oct 2020 A1
20200333054 Asano et al. Oct 2020 A1
20200347283 Itano et al. Nov 2020 A1
20200363085 Itano et al. Nov 2020 A1
20200363105 Kumakura et al. Nov 2020 A1
20200363106 Itano et al. Nov 2020 A1
20200363112 Ohtsuka et al. Nov 2020 A1
20200369934 Itano et al. Nov 2020 A1
20200385620 Itano et al. Dec 2020 A1
20200385621 Itano et al. Dec 2020 A1
20200385622 Itano et al. Dec 2020 A1
20200392387 Ohtsuka et al. Dec 2020 A1
20200392388 Itano et al. Dec 2020 A1
20200393178 Kumakura et al. Dec 2020 A1
20210018191 Itano et al. Jan 2021 A1
20210135520 Shimokawa et al. May 2021 A1
20210189209 Yotdumoto et al. Jun 2021 A1
20210222040 Fukushima et al. Jul 2021 A1
20210355359 Ohkubo et al. Nov 2021 A1
Foreign Referenced Citations (243)
Number Date Country
2001284508 Mar 2002 AU
1288132 Mar 2001 CN
1447491 Oct 2003 CN
1455855 Nov 2003 CN
1723373 Jan 2006 CN
1987264 Jun 2007 CN
101235815 Aug 2008 CN
101441012 May 2009 CN
102401519 Apr 2012 CN
103562338 Feb 2014 CN
203704143 Jul 2014 CN
103975204 Aug 2014 CN
104094069 Oct 2014 CN
104456760 Mar 2015 CN
104578493 Apr 2015 CN
204534884 Aug 2015 CN
104903661 Sep 2015 CN
104937350 Sep 2015 CN
204648544 Sep 2015 CN
105102905 Nov 2015 CN
204943959 Jan 2016 CN
205261858 May 2016 CN
106029821 Oct 2016 CN
106030222 Oct 2016 CN
106062159 Oct 2016 CN
106085363 Nov 2016 CN
106103992 Nov 2016 CN
106133110 Nov 2016 CN
106414653 Feb 2017 CN
106414654 Feb 2017 CN
106415152 Feb 2017 CN
106574802 Apr 2017 CN
106661477 May 2017 CN
106839496 Jun 2017 CN
107110570 Aug 2017 CN
107112830 Aug 2017 CN
107429957 Dec 2017 CN
107614980 Jan 2018 CN
107925285 Apr 2018 CN
108139112 Jun 2018 CN
108431414 Aug 2018 CN
108469126 Aug 2018 CN
1 231 255 Aug 2002 EP
1 246 348 Oct 2002 EP
1 326 057 Jul 2003 EP
1 632 732 Mar 2006 EP
1 953 388 Aug 2008 EP
2 423 609 Feb 2012 EP
2 620 736 Jul 2013 EP
2 711 405 Mar 2014 EP
2 789 933 Oct 2014 EP
2 840 335 Feb 2015 EP
2 853 826 Apr 2015 EP
2 918 953 Sep 2015 EP
2 952 828 Dec 2015 EP
2 980 508 Feb 2016 EP
3 012 555 Apr 2016 EP
3 012 557 Apr 2016 EP
3 070 417 Sep 2016 EP
3 101 082 Dec 2016 EP
3 109 302 Dec 2016 EP
3 115 716 Jan 2017 EP
3 121 242 Jan 2017 EP
3 128 259 Feb 2017 EP
3 147 595 Mar 2017 EP
3 153 559 Apr 2017 EP
3 153 561 Apr 2017 EP
3 170 881 May 2017 EP
3 222 934 Sep 2017 EP
3 249 309 Nov 2017 EP
3 299 731 Mar 2018 EP
3 358 272 Aug 2018 EP
3 358 278 Aug 2018 EP
3 399 189 Nov 2018 EP
2530915 Apr 2016 GB
51-90115 Jul 1976 JP
52-13025 Apr 1977 JP
57-198968 Dec 1982 JP
59-39790 Mar 1984 JP
62-69066 Mar 1987 JP
63-69066 Mar 1987 JP
2-4163 Jan 1990 JP
5-264070 Oct 1993 JP
5-272823 Oct 1993 JP
7-19627 Jan 1995 JP
7-190571 Jul 1995 JP
8-200273 Aug 1996 JP
10-46170 Feb 1998 JP
10-300292 Nov 1998 JP
10-309050 Nov 1998 JP
10-318564 Dec 1998 JP
11-206001 Jul 1999 JP
11-256358 Sep 1999 JP
2000-161805 Jun 2000 JP
2000-220877 Aug 2000 JP
2000-234767 Aug 2000 JP
2000-304302 Nov 2000 JP
2001-82755 Mar 2001 JP
2001-139972 May 2001 JP
2002-54888 Feb 2002 JP
2002-89978 Mar 2002 JP
2002-257366 Sep 2002 JP
2002-272043 Sep 2002 JP
2002-318028 Oct 2002 JP
2003-18776 Jan 2003 JP
2003-83614 Mar 2003 JP
2003-174794 Jun 2003 JP
2004-28035 Jan 2004 JP
2004-132647 Apr 2004 JP
2004-215406 Jul 2004 JP
2004-251535 Sep 2004 JP
2004-361036 Dec 2004 JP
2005-61711 Mar 2005 JP
2005-241045 Sep 2005 JP
2005-288502 Oct 2005 JP
2006-162197 Jun 2006 JP
2006-211824 Aug 2006 JP
2006-313027 Nov 2006 JP
2008-39305 Feb 2008 JP
2008-54488 Mar 2008 JP
2008-190377 Aug 2008 JP
2008-245384 Oct 2008 JP
2008-286422 Nov 2008 JP
2009-63216 Mar 2009 JP
2009-92274 Apr 2009 JP
2009-121654 Jun 2009 JP
2009-150620 Jul 2009 JP
2009-299975 Dec 2009 JP
2010-28985 Feb 2010 JP
2010-103346 May 2010 JP
2010-119190 May 2010 JP
2010-164222 Jul 2010 JP
2010-230242 Oct 2010 JP
2011-4449 Jan 2011 JP
2011-43304 Mar 2011 JP
2011-52884 Mar 2011 JP
2011-94841 May 2011 JP
2011-135638 Jul 2011 JP
2011-202738 Oct 2011 JP
2011-252636 Dec 2011 JP
2012-42169 Mar 2012 JP
2012-112617 Jun 2012 JP
2012-132637 Jul 2012 JP
2012-151969 Aug 2012 JP
2013-124848 Jun 2013 JP
2013-126281 Jun 2013 JP
2013-139990 Jul 2013 JP
2013-155892 Aug 2013 JP
2013-155921 Aug 2013 JP
2013-172615 Sep 2013 JP
2013-200090 Oct 2013 JP
2013-221671 Oct 2013 JP
2014-70840 Apr 2014 JP
2014-75971 Apr 2014 JP
2014-89004 May 2014 JP
2014-129543 Jul 2014 JP
2014-152999 Aug 2014 JP
2014-167381 Sep 2014 JP
2015-23721 Feb 2015 JP
2015-55455 Mar 2015 JP
2015-78789 Apr 2015 JP
2015-82875 Apr 2015 JP
2015-111012 Jun 2015 JP
2015-114082 Jun 2015 JP
2015-145765 Aug 2015 JP
2015-158282 Sep 2015 JP
2015-218909 Dec 2015 JP
2015-218912 Dec 2015 JP
2015-229767 Dec 2015 JP
2016-1062 Jan 2016 JP
2016-11423 Jan 2016 JP
2016-56340 Apr 2016 JP
2016-125808 Jul 2016 JP
2016-133256 Jul 2016 JP
2016-172869 Sep 2016 JP
2016-174461 Sep 2016 JP
2017-36861 Feb 2017 JP
2017-46430 Mar 2017 JP
2017-53285 Mar 2017 JP
2017-67373 Apr 2017 JP
2017-67428 Apr 2017 JP
2017-122549 Jul 2017 JP
2017-145975 Aug 2017 JP
2017-192190 Oct 2017 JP
2018-25377 Feb 2018 JP
2001-0029975 Apr 2001 KR
2003-0028838 Apr 2003 KR
10-0939609 Oct 2003 KR
10-2004-0075737 Aug 2004 KR
10-2005-0044931 May 2005 KR
10-2017-0034887 Mar 2017 KR
2013 156 380 Jun 2015 RU
20030103482 Feb 2003 TW
0136571 May 2001 WO
0223100 Mar 2002 WO
2009069679 Jun 2009 WO
2009093345 Jul 2009 WO
2012157764 Nov 2012 WO
2012157765 Nov 2012 WO
WO-2012157765 Nov 2012 WO
2013084301 Jun 2013 WO
2013146103 Oct 2013 WO
2013146208 Oct 2013 WO
2013151043 Oct 2013 WO
2014045400 Mar 2014 WO
2014118945 Aug 2014 WO
2014119149 Aug 2014 WO
2014156190 Oct 2014 WO
2014203353 Dec 2014 WO
2014203354 Dec 2014 WO
2015071967 May 2015 WO
2015115252 Aug 2015 WO
2015125763 Aug 2015 WO
2015125884 Aug 2015 WO
2015136981 Sep 2015 WO
2015140827 Sep 2015 WO
2015141678 Sep 2015 WO
2015186557 Dec 2015 WO
2015186670 Dec 2015 WO
2016009884 Jan 2016 WO
2016017460 Feb 2016 WO
2016103711 Jun 2016 WO
2016104418 Jun 2016 WO
2016117443 Jul 2016 WO
2016157538 Oct 2016 WO
2016182030 Nov 2016 WO
2016190232 Dec 2016 WO
2017038489 Mar 2017 WO
2017056789 Apr 2017 WO
2017057004 Apr 2017 WO
2017115636 Jul 2017 WO
2017122517 Jul 2017 WO
2017195248 Nov 2017 WO
2019123782 Jun 2019 WO
2019123804 Jun 2019 WO
2019123805 Jun 2019 WO
2019123806 Jun 2019 WO
2019123807 Jun 2019 WO
2019124400 Jun 2019 WO
2019124401 Jun 2019 WO
2019124402 Jun 2019 WO
2019124403 Jun 2019 WO
2019124404 Jun 2019 WO
Non-Patent Literature Citations (74)
Entry
International Preliminary Report on Patentability dated Jun. 23, 2020 in International Application No. PCT/JP2018/045978.
International Search Report dated Mar. 19, 2019 in International Application No. PCT/JP2018/045978.
International Preliminary Report on Patentability dated Jun. 23, 2020 in International Application No. PCT/JP2018/046532.
International Search Report dated Feb. 12, 2019 in International Application No. PCT/JP2018/046532.
International Preliminary Report on Patentability dated Jun. 23, 2020 in International Application No. PCT/JP2018/042027.
International Search Report dated Feb. 12, 2019 in International Application No. PCT/JP2018/042027.
International Preliminary Report on Patentability dated Jun. 23, 2020 in International Application No. PCT/JP2018/042032.
International Search Report dated Feb. 19, 2019 in International Application No. PCT/JP2018/042032.
International Preliminary Report on Patentability dated Jun. 23, 2020 in International Application No. PCT/JP2018/046666.
International Search Report dated Apr. 2, 2019 in International Application No. PCT/JP2018/046666.
International Preliminary Report on Patentability dated Jun. 23, 2020 in International Application No. PCT/JP2018/045336.
International Search Report dated Feb. 19, 2019 in International Application No. PCT/JP2018/045336.
International Preliminary Report on Patentability dated Jun. 23, 2020 in International Application No. PCT/JP2018/045557.
International Search Report dated Mar. 12, 2019 in International Application No. PCT/JP2018/045557.
International Preliminary Report on Patentability dated Jun. 23, 2020 in International Application No. PCT/JP2018/046426.
International Search Report dated Feb. 19, 2019 in International Application No. PCT/JP2018/046426
International Preliminary Report on Patentability dated Jun. 23, 2020 in International Application No. PCT/JP2018/046427.
International Search Report dated Feb. 19, 2019 in International Application No. PCT/JP2018/046427.
International Preliminary Report on Patentability dated Jun. 23, 2020 in International Application No. PCT/JP2018/046428.
International Search Report dated Mar. 19, 2019 in International Application No. PCT/JP2018/046428.
International Preliminary Report on Patentability dated Jun. 23, 2020 in International Application No. PCT/JP2018/046581.
International Search Report dated Mar. 5, 2019 in International Application No. PCT/JP2018/046581.
International Preliminary Report on Patentability dated Jun. 23, 2020 in International Application No. PCT/JP2018/046630.
International Search Report dated Mar. 5, 2019 in International Application No. PCT/JP2018/046630.
International Preliminary Report on Patentability dated Jun. 23, 2020 in International Application No. PCT/JP2018/046582.
International Search Report dated Mar. 5, 2019 in International Application No. PCT/JP2018/046582.
International Preliminary Report on Patentability dated Jun. 23, 2020 in International Application No. PCT/JP2018/046631.
International Search Report dated Mar. 5, 2019 in International Application No. PCT/JP2018/046631.
International Preliminary Report on Patentability dated Jun. 23, 2020 in International Application No. PCT/JP2018/046627.
International Search Report dated Mar. 19, 2019 in International Application No. PCT/JP2018/046627.
International Preliminary Report on Patentability dated Jun. 23, 2020 in International Application No. PCT/JP2018/046628.
International Search Report dated Mar. 19, 2019 in International Application No. PCT/JP2018/046628.
International Preliminary Report on Patentability dated Jun. 23, 2020 in International Application No. PCT/JP2018/045979.
International Search Report dated Mar. 12, 2019 in International Application No. PCT/JP2018/045979
International Preliminary Report on Patentability dated Jun. 23, 2020 in International Application No. PCT/JP2018/046434.
International Search Report dated Feb. 19, 2019 in International Application No. PCT/JP2018/046434.
International Preliminary Report on Patentability dated Jun. 23, 2020 in International Application No. PCT/JP2018/045290.
International Search Report dated Jan. 22, 2019 in International Application No. PCT/JP2018/045290.
International Preliminary Report on Patentability dated Jun. 23, 2020 in International Application No. PCT/JP2018/045288.
International Search Report dated Jan. 22, 2019 in International Application No. PCT/JP2018/045288.
International Preliminary Report on Patentability dated Jun. 23, 2020 in International Application No. PCT/JP2018/045289.
International Search Report dated Jan. 22, 2019 in International Application No. PCT/JP2018/045289.
International Preliminary Report on Patentability dated Jun. 23, 2020 in International Application No. PCT/JP2018/046639.
International Preliminary Report on Patentability dated Jun. 23, 2020 in International Application No. PCT/JP2018/046642.
International Preliminary Report on Patentability dated Jun. 23, 2020 in International Application No. PCT/JP2018/038746.
International Preliminary Report on Patentability dated Jun. 23, 2020 in International Application No. PCT/JP2018/046643.
International Preliminary Report on Patentability dated Jun. 23, 2020 in International Application No. PCT/JP2018/038748.
International Preliminary Report on Patentability dated Jun. 23, 2020 in International Application No. PCT/JP2018/046640.
International Preliminary Report on Patentability dated Jun. 23, 2020 in International Application No. PCT/JP2018/046644.
International Preliminary Report on Patentability dated Jun. 23, 2020 in International Application No. PCT/JP2018/038749.
International Preliminary Report on Patentability dated Jun. 23, 2020 in International Application No. PCT/JP2018/037483.
International Search Report dated Feb. 19, 2019 in International Application No. PCT/JP2018/045335
International Preliminary Report on Patentability dated Jun. 23, 2020 in International Application No. PCT/JP2018/045335.
International Search Report dated Feb. 19, 2019 in International Application No. PCT/JP2018/046435.
International Preliminary Report on Patentability dated Jun. 23, 2020 in International Application No. PCT/JP2018/046435.
International Search Report dated Mar. 19, 2019 in International (PCT) Application No. PCT/JP2018/046530.
International Preliminary Report on Patentability dated Jun. 23, 2020 in International Application No. PCT/JP2018/046530.
International Search Report dated Feb. 12, 2019 in International (PCT) Application No. PCT/JP2018/046533.
International Preliminary Report on Patentability dated Jun. 23, 2020 in International Application No. PCT/JP2018/046533.
Hirahara et al., “Latest trend of alternative refrigerant: LCCP-analogy for HFO-1234yf Air Conditioners using a Simulation with R134a Properties”, Refrigeration, Jan. 15, 2010, vol. 85, No. 987, pp. 15-20, with partial translation.
International Preliminary Report on Patentability dated Jun. 23, 2020 in International Application No. PCT/JP2018/038747.
International Search Report dated Mar. 12, 2019 in International (PCT) Application No. PCT/JP2018/046639.
International Search Report dated Mar. 12, 2019 in International (PCT) Application No. PCT/JP2018/046642.
International Search Report dated Dec. 18, 2018 in International (PCT) Application No. PCT/JP2018/038746.
International Search Report dated Mar. 19, 2019 in International (PCT) Application No. PCT/JP2018/046643.
International Search Report dated Dec. 18, 2018 in International (PCT) Application No. PCT/JP2018/038748.
International Search Report dated Mar. 12, 2019 in International (PCT) Application No. PCT/JP2018/046640.
International Search Report dated Mar. 19, 2019 in International (PCT) Application No. PCT/JP2018/046644.
International Search Report dated Dec. 18, 2018 in International (PCT) Application No. PCT/JP2018/038749.
International Search Report dated Dec. 18, 2018 in International (PCT) Application No. PCT/JP2018/037483
International Search Report dated Dec. 18, 2018 in International (PCT) Application No. PCT/JP2018/038747.
International Search Report dated Mar. 19, 2019 in International Application No. PCT/JP2018/046531.
International Preliminary Report on Patentability dated Jun. 23, 2020 in International Application No. PCT/JP2018/046531.
Summary, Collection of Papers of the 2nd Symposium on New Technologies of Refrigeration and Air Conditioning, 2nd Edition, Ding Guoliang, Ed., published by Shanghai Jiatong University Press, 2003, with Concise Explanation.
Related Publications (1)
Number Date Country
20200363085 A1 Nov 2020 US
Continuation in Parts (1)
Number Date Country
Parent 16954956 US
Child 16913506 US