Composition containing refrigerant, use of said composition, refrigerator having said composition, and method for operating said refrigerator

Information

  • Patent Grant
  • 11492527
  • Patent Number
    11,492,527
  • Date Filed
    Wednesday, October 17, 2018
    5 years ago
  • Date Issued
    Tuesday, November 8, 2022
    a year ago
Abstract
An object is to provide a mixed refrigerant having three types of performance, i.e., a refrigerating capacity (also referred to as refrigeration capacity and cooling capacity) and a coefficient of performance that are equivalent to those of R410A, and a sufficiently low GWP. Provided as a means for a solution is a composition comprising a refrigerant, the refrigerant comprising trans-1,2-difluoroethylene (HFO-1132(E)), trifluoroethylene (HFO-1123), and 2,3,3,3-tetrafluoro-1-propene (R1234yf), and R32.
Description
TECHNICAL FIELD

The present disclosure relates to a composition comprising a refrigerant, use of the composition, a refrigerating machine having the composition, and a method for operating the refrigerating machine.


BACKGROUND ART

R410A is currently used as an air conditioning refrigerant for home air conditioners etc. R410A is a two-component mixed refrigerant of difluoromethane (CH2F2: HFC-32 or R32) and pentafluoroethane (C2HF5: HFC-125 or R125), and is a pseudo-azeotropic composition.


However, the global warming potential (GWP) of R410A is 2088. Due to growing concerns about global warming, R32, which has a GWP of 675, has been increasingly used.


For this reason, various low-GWP mixed refrigerants that can replace R410A have been proposed (PTL 1).


CITATION LIST
Patent Literature

PTL 1: WO2015/141678


SUMMARY OF INVENTION
Technical Problem

The present inventors performed independent examination, and conceived of the idea that no prior art had developed refrigerant compositions having three types of performance, i.e., a refrigerating capacity (also referred to as “cooling capacity” or “capacity”) and a coefficient of performance (COP) that are equivalent to those of R410A, and a sufficiently low GWP. An object of the present disclosure is to solve this unique problem.


Solution to Problem

Item 1 A composition comprising a refrigerant, the refrigerant comprising 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).


Item 2 A composition comprising a refrigerant, the refrigerant comprising 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).


Item 3 A composition comprising a refrigerant, the refrigerant comprising trans-1,2-difluoroethylene (HFO-1132(E)), trifluoroethylene (HFO-1123), 2,3,3,3-tetrafluoro-1-propene (R1234yf), and 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≤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, −0.0304a7+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).


Item 4 The composition according to any one of Items 1 to 3, for use as a working fluid for a refrigerating machine, wherein the composition further comprises a refrigerant oil.


Item 5 The composition according to any one of Items 1 to 4, for use as an alternative refrigerant for R410A.


Item 6 Use of the composition according to any one of Items 1 to 4 as an alternative refrigerant for R410A.


Item 7 A refrigerating machine comprising the composition according to any one of Items 1 to 4 as a working fluid.


Item 8 A method for operating a refrigerating machine, comprising the step of circulating the composition according to any one of Items 1 to 4 as a working fluid in a refrigerating machine.


Advantageous Effects of Invention

The refrigerant according to the present disclosure has three types of performance, i.e., a refrigerating capacity and a coefficient of performance that are equivalent to those of R410A, and a sufficiently low GWP.





BRIEF DESCRIPTION OF DRAWINGS


FIG. 1 is a schematic view of an apparatus used in a flammability test.



FIG. 2 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. 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 92.9 mass % (the content of R32 is 7.1 mass %).



FIG. 4 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. 5 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. 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 81.8 mass % (the content of R32 is 18.2 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 78.1 mass % (the content of R32 is 21.9 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 73.3 mass % (the content of R32 is 26.7 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 70.7 mass % (the content of R32 is 29.3 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 63.3 mass % (the content of R32 is 36.7 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 55.9 mass % (the content of R32 is 44.1 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 52.2 mass % (the content of R32 is 47.8 mass %).





DESCRIPTION OF EMBODIMENTS

The present inventors conducted intensive study to solve the above problem, and consequently found that a mixed refrigerant comprising trans-1,2-difluoroethylene (HFO-1132(E)), 2,3,3,3-tetrafluoro-1-propene (R1234yf), trifluoroethylene (HFO-1123), and difluoromethane (R32) has the above properties.


The present disclosure has been completed as a result of further research based on this finding. The present disclosure includes the following embodiments.


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 be classified as “Class 2L.”


1. Refrigerant


1.1 Refrigerant Component


The refrigerant 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 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


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 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 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 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 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.


1.2. Use


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 R410A.


2. 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 %.


2.1. 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.


2.2. 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.


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 hydrochlorocarbon, a fluorocarbcn, 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 refrigerant composition according to the present disclosure may contain one or more tracers at a total concentration of about 10 parts per million by weight (ppm) to about 1000 ppm based on the entire refrigerant composition. The refrigerant composition according to the present disclosure may preferably contain one or more tracers at a total concentration of about 30 ppm to about 500 ppm, and more preferably about 50 ppm to about 300 ppm, based on the entire refrigerant composition.


2.3. 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.


2.4. 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.


2.5. 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.


3. 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.


3.1. Refrigeration Oil


The composition according to the present disclosure may comprise a single refrigeration oil, or two or more refrigeration oils.


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.


3.2. 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.


4. Method for Operating Refrigerating Machine


The method for operating a refrigerating machine according to the present disclosure is a method for operating a refrigerating machine using the refrigerant according to the present disclosure.


Specifically, the method for operating a refrigerating machine according to the present disclosure comprises the step of circulating the refrigerant according to the present disclosure in a refrigerating machine.


Embodiments are described above; however, it will be understood that various changes in forms and details can be made without departing from the spirit and scope of the claims.


EXAMPLES

The present disclosure is described in more detail below with reference to Examples. However, the present disclosure 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 1 to 58.


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 PTL 1). 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 1 to 58 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 1








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





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


Item
Unit
Ex. 1
A
B
C
D′
G
I
J
K′

























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


HFO-1123
Mass %

0.0
58.7
67.1
75.4
28.0
0.0
52.9
5.9


R1234yf
Mass %

31.4
41.3
0.0
24.6
0.0
28.0
0.0
32.4


R32
Mass %

0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0


GWP

2088
2
2
1
2
1
2
1
2


COP ratio
% (relative
 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 2







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





Ex. 9
Ex. 10
Ex. 11
Ex. 12
Ex. 13
Ex. 14
Ex. 15
Ex. 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 3







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





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


Item
Unit
A
B
C = D′
G
I
J
K′























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


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


R1234yf
Mass %
40.5
46.6
0.0
0.0
33.1
0.0
41.4


R32
Mass %
11.1
11.1
11.1
11.1
11.1
11.1
11.1


GWP

77
77
76
76
77
76
77


COP ratio
% (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 4







Comp.
Comp.
Comp.
Comp.
Comp.





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




22
23
24
25
26
4


Item
Unit
A
B
G
I
J
K′






















HFO-
Mass %
42.8
0.0
52.1
52.1
34.3
36.5


1132(E)









HFO-
Mass %
0.0
37.8
33.4
0.0
51.2
5.6


1123









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
%
99.9
98.1
95.8
99.5
94.4
99.5


ratio
(relative









to









R410A)








Refrig-
%
85.0
85.0
109.1
89.6
111.1
85.3


erating
(relative








capacity
to








ratio
R410A)























TABLE 5







Comp.
Comp.
Comp.
Comp.
Comp.





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




27
28
29
30
31
5


Item
Unit
A
B
G
I
J
K′






















HFO-
Mass %
37.0
0.0
48.6
48.6
32.0
32.5


1132(E)









HFO-
Mass %
0.0
33.1
33.2
0.0
49.8
4.0


1123









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
%
100.0
98.6
95.9
99.4
94.7
99.8


ratio
(relative









to









R410A)








Refrig-
%
85.0
85.0
110.1
90.8
111.9
85.2


erating
(relative








capacity
to








ratio
R410A)























TABLE 6







Comp.
Comp.
Comp.
Comp.
Comp.





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




32
33
34
35
36
6


Item
Unit
A
B
G
I
J
K′






















HFO-
Mass %
31.5
0.0
45.4
45.4
30.3
28.8


1132(E)









HFO-
Mass %
0.0
28.5
32.7
0.0
47.8
2.4


1123









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
%
100.2
99.1
96.0
99.4
95.1
100.0


ratio
(relative









to









R410A)








Refrig-
%
85.0
85.0
111.0
92.1
112.6
85.1


erating
(relative








capacity
to








ratio
R410A)























TABLE 7







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




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




37
38
39
40
41
42


Item
Unit
A
B
G
I
J
K′






















HFO-
Mass %
24.8
0.0
41.8
41.8
29.1
24.8


1132(E)









HFO-
Mass %
0.0
22.9
31.5
0.0
44.2
0.0


1123









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
%
100.4
99.8
96.3
99.4
95.6
100.4


ratio
(relative









to









R410A)








Refrig-
%
85.0
85.0
111.9
93.8
113.2
85.0


erating
(relative








capacity
to








ratio
R410A)























TABLE 8







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




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




43
44
45
46
47
48


Item
Unit
A
B
G
I
J
K′






















HFO-
Mass %
21.3
0.0
40.0
40.0
28.8
24.3


1132(E)









HFO-
Mass %
0.0
19.9
30.7
0.0
41.9
0.0


1123









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
%
100.6
100.1
96.6
99.5
96.1
100.4


ratio
(relative









to









R410A)








Refrig-
%
85.0
85.0
112.4
94.8
113.6
86.7


erating
(relative








capacity
to








ratio
R410A)























TABLE 9







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




49
50
51
52
53
54


Item
Unit
A
B
G
I
J
K′






















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


HFO-1123
Mass %
0.0
11.7
27.6
0.0
34.0
0.0


R1234yf
Mass %
51.2
51.6
0.0
27.6
0.0
40.8


R32
Mass %
36.7
36.7
36.7
36.7
36.7
36.7


GWP

250
250
248
249
248
250


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



R410A)








Refrigerating
% (relative to
85.0
85.0
113.2
97.6
113.9
90.9


capacity ratio
R410A)





























TABLE 10







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




55
56
57
58
59
60


Item
Unit
A
B
G
I
J
K′






















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


HFO-1123
Mass %
0.0
3.9
23.9
0.0
26.5
0.0


R1234yf
Mass %
52.1
52.0
0.0
23.9
0.0
34.8


R32
Mass %
44.1
44.1
44.1
44.1
44.1
44.1


GWP

300
300
298
299
298
299


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



R410A)








Refrigerating
% (relative to
85.0
85.0
113.7
100.4
113.9
94.9


capacity ratio
R410A)






















TABLE 11







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


Item
Unit
A = B
G
I
J
K′





















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


HFO-1123
Mass %
0.0
21.8
0.0
23.3
0.0


R1234yf
Mass %
52.2
0.0
21.8
0.0
31.8


R32
Mass %
47.8
47.8
47.8
47.8
47.8


GWP

325
323
324
323
324


COP ratio
% (relative
102.1
98.2
100.0
982
100.6



to R410A)







Refrigerating
% (relative
850
113.8
101.8
113.9
96.8


capacity ratio
to R410A)






























TABLE 12





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
























HF0-1132 (E)
Mass %
5.0
10.0
15.0
20.0
25.0
30.0
35.0
40.0


HF0-1123
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 13





Item
Unit
Ex. 14
Ex. 15
Ex. 16
Ex. 17
Comp. Ex. 67
Ex. 18
Ex. 19
Ex. 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
100


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 14





Item
Unit
Ex. 21
Ex. 22
Ex. 23
Ex. 24
Ex. 25
Ex. 26
Ex. 27
Ex. 28
























HFO-1132 (E)
Mass %
25.0
30.0
35.0
40.0
45.0
50.0
55.0
60.0


HFO-1123
Mass %
57.9
52.9
47.9
42.9
37.9
32.9
27.9
22.9


R1234yf
Mass %
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0


R32
Mass %
7.1
7.1
7.1
7.1
7.1
7.1
7.1
7.1


GWP

49
49
49
49
49
49
49
49


COP ratio
% (relative
93.9
94.2
94.6
95.0
95.5
96.0
96.4
96.9



to R410A)










Refrigerating
% (relative
104.9
104.5
104.1
103.6
103.0
102.4
101.7
101.0


capacity ratio
to R410A)

































TABLE 15





Item
Unit
Comp. Ex. 68
Ex. 29
Ex. 30
Ex. 31
Ex. 32
Ex. 33
Ex. 34
Ex. 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 16





Item
Unit
Ex. 36
Ex. 37
Ex. 38
Ex. 39
Comp. Ex. 69
Ex. 40
Ex. 41
Ex. 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 17





Item
Unit
Ex. 43
Ex. 44
Ex. 45
Ex. 46
Ex. 47
Ex. 48
Ex. 49
Ex. 50
























HFO-1132 (E)
Mass %
25.0
30.0
35.0
40.0
45.0
50.0
55.0
60.0


HFO-1123
Mass %
47.9
42.9
37.9
32.9
27.9
22.9
17.9
12.9


R1234yf
Mass %
20.0
20.0
20.0
20.0
20.0
20.0
20.0
20.0


R32
Mass %
7.1
7.1
7.1
7.1
7.1
7.1
7.1
7.1


GWP

49
49
49
49
49
49
49
49


COP ratio
% (relative
95.0
95.3
95.7
96.2
96.6
97.1
97.6
98.1



to R410A)










Refrigerating
% (relative
99.2
98.8
98.3
97.8
97.2
96.6
95.9
95.2


capacity ratio
to R410A)

























TABLE 18





Item
Unit
Comp. Ex. 70
Ex. 51
Ex. 52
Ex. 53
Ex. 54
Ex. 55
Ex. 56
Ex. 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 19





Item
Unit
Ex. 58
Ex. 59
Ex. 60
Ex. 61
Comp. Ex. 71
Ex. 62
Ex. 63
Ex. 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 20





Item
Unit
Ex. 65
Ex. 66
Ex. 67
Ex. 68
Ex. 69
Ex. 70
Ex. 71
Ex 72
























HFO-1132 (E)
Mass %
25.0
30.0
35.0
40.0
45.0
50.0
55.0
60.0


HFO-1123
Mass %
37.9
32.9
27.9
22.9
17.9
12.9
7.9
2.9


R1234yf
Mass %
30.0
30.0
30.0
30.0
30.0
30.0
30.0
30.0


R32
Mass %
7.1
7.1
7.1
7.1
7.1
7.1
7.1
7.1


GWP

50
50
50
50
50
50
50
50


COP ratio
% (relative
96.2
96.6
97.0
97.4
97.9
98.3
98.8
99.3



to R410A)










Refrigerating
% (relative
93.3
92.9
92.4
91.8
91.2
90.5
89.8
89.1


capacity ratio
to R410A)

































TABLE 21





Item
Unit
Ex. 73
Ex. 74
Ex. 75
Ex. 76
Ex. 77
Ex. 78
Ex. 79
Ex. 80
























HFO-1132 (E)
Mass %
10.0
15.0
20.0
25.0
30.0
35.0
40.0
45.0


HFO-1123
Mass %
47.9
42.9
37.9
32.9
27.9
22.9
17.9
12.9


R1234yf
Mass %
35.0
35.0
35.0
35.0
35.0
35.0
35.0
35.0


R32
Mass %
7.1
7.1
7.1
7.1
7.1
7.1
7.1
7.1


GWP

50
50
50
50
50
50
50
50


COP ratio
% (relative
95.9
96.2
96.5
96.9
97.2
97.7
98.1
98.5



to R410A)










Refrigerating
% (relative
91.1
90.9
90.6
902
89.8
89.3
88.7
88.1


capacity ratio
to R410A)

































TABLE 22





Item
Unit
Ex. 81
Ex. 82
Ex. 83
Ex. 84
Ex. 85
Ex. 86
Ex. 87
Ex. 88
























HFO-1132 (E)
Mass %
50.0
55.0
10.0
15.0
20.0
25.0
30.0
35.0


HFO-1123
Mass %
7.9
2.9
42.9
37.9
32.9
27.9
22.9
17.9


R1234yf
Mass %
35.0
35.0
40.0
40.0
40.0
40.0
40.0
40.0


R32
Mass %
7.1
7.1
7.1
7.1
7.1
7.1
7.1
7.1


GWP

50
50
50
50
50
50
50
50


COP ratio
% (relative
99.0
99.4
96.6
96.9
97.2
97.6
98.0
98.4



to R410A)










Refrigerating
% (relative
87.4
86.7
88.0
87.8
87.5
87.1
86.6
86.1


capacity ratio
to R410A)

































TABLE 23







Comp.
Cornp.
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 to
98.8
99.2
99.6
97.4
97.7
98.0
98.3
98.7



R410A)










Refrigerating
% (relative to
85.5
84.9
84.2
84.9
84.6
84.3
83.9
83.5


capacity ratio
R410A)




























TABLE 24





Item
Unit
Comp. Ex. 80
Comp. Ex. 81
Comp. 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
% (relative
82.9
82.3
81.7


capacity ratio
to R410A)

























TABLE 25





Item
Unit
Ex. 89
Ex. 90
Ex. 91
Ex. 92
Ex. 93
Ex. 94
Ex. 95
Ex. 96
























HFO-1132(E)
Mass %
10.0
15.0
20.0
25.0
30.0
35.0
40.0
45.0


HFO-1123
Mass %
70.5
65.5
60.5
55.5
50.5
45.5
40.5
35.5


R1234yf
Mass %
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0


R32
Mass %
14.5
14.5
14.5
14.5
14.5
14.5
14.5
14.5


GWP

99
99
99
99
99
99
99
99


COP ratio
% (relative to R410A)
93.7
93.9
94.1
94.4
94.7
95.0
95.4
95.8


Refrigerating
% (relative to R410A)
110.2
110.0
109.7
109.3
108.9
108.4
107.9
107.3


capacity ratio

























TABLE 26





Item
Unit
Ex. 97
Comp. Ex 83
Ex. 98
Ex. 99
Ex. 100
Ex. 101
Ex. 102
Ex. 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 to R410A)
96.2
96.6
94.2
94.4
94.6
94.9
95.2
95.5


Refrigerating
% (relative to R410A)
106.6
106.0
107.5
107.3
107.0
106.6
106.1
105.6


capacity ratio

























TABLE 27





Item
Unit
Ex. 104
Ex. 105
Ex. 106
Comp. Ex. 84
Ex. 107
Ex. 108
Ex. 109
Ex. 110
























HFO-1132(E)
Mass %
40.0
45.0
50.0
55.0
100
150
200
250


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 28





Item
Unit
Ex. 111
Ex. 112
Ex. 113
Ex. 114
Ex. 115
Comp. Ex. 85
Ex. 116
Ex. 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 29





Item
Unit
Ex. 118
Ex. 119
Ex. 120
Ex. 121
Ex. 122
Ex. 123
Ex. 124
Comp. 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 30





Item
Unit
Ex. 125
Ex. 126
Ex. 127
Ex. 128
Ex. 129
Ex. 130
Ex. 131
Ex. 132
























HFO-1132(E)
Mass %
10.0
15.0
20.0
25.0
30.0
35.0
40.0
45.0


HFO-1123
Mass %
50.5
45.5
40.5
35.5
30.5
25.5
20.5
15.5


R1234yf
Mass %
25.0
25.0
25.0
25.0
25.0
25.0
25.0
25.0


R32
Mass %
14.5
14.5
14.5
14.5
14.5
14.5
14.5
14.5


GWP

99
99
99
99
99
99
99
99


COP ratio
% (relative to R410A)
95.6
95.9
96.1
96.4
96.7
97.1
97.5
97.9


Refrigerating
% (relative to R410A)
98.9
98.6
98.3
97.9
97.4
96.9
96.3
95.7


capacity ratio

























TABLE 31





Item
Unit
Ex. 133
Comp. Ex 87
Ex. 134
Ex. 135
Ex. 136
Ex. 137
Ex. 138
Ex. 139
























HFO-1132(E)
Mass %
50.0
55.0
10.0
15.0
20.0
25.0
30.0
35.0


HFO-1123
Mass %
10.5
5.5
45.5
40.5
35.5
30.5
25.5
20.5


R1234yf
Mass %
25.0
25.0
30.0
30.0
30.0
30.0
30.0
30.0


R32
Mass %
14.5
14.5
14.5
14.5
14.5
14.5
14.5
14.5


GWP

99
99
100
100
100
100
100
100


COP ratio
% (relative to R410A)
98.3
98.7
96.2
96.4
96.7
97.0
97.3
97.7


Refrigerating
% (relative to R410A)
95.0
94.3
95.8
95.6
95.2
94.8
94.4
93.8


capacity ratio

























TABLE 32





Item
Unit
Ex. 140
Ex. 141
Ex. 142
Ex. 143
Ex. 144
Ex. 145
Ex. 146
Ex. 147
























HFO-1132(E)
Mass %
40.0
45.0
50.0
10.0
15.0
20.0
25.0
30.0


HFO-1123
Mass %
15.5
10.5
5.5
40.5
35.5
30.5
25.5
20.5


R1234yf
Mass %
30.0
30.0
30.0
35.0
35.0
35.0
35.0
35.0


R32
Mass %
14.5
14.5
14.5
14.5
14.5
14.5
14.5
14.5


GWP

100
100
100
100
100
100
100
100


COP ratio
% (relative to R410A)
98.1
98.5
98.9
96.8
97.0
97.3
97.6
97.9


Refrigerating
% (relative to R4104)
93.3
92.6
92.0
92.8
92.5
92.2
91.8
91.3


capacity ratio

























TABLE 33





Item
Unit
Ex. 148
Ex. 149
Ex. 150
Ex. 151
Ex. 152
Ex. 153
Ex. 154
Ex. 155
























HFO-1132(E)
Mass %
35.0
40.0
45.0
10.0
15.0
20.0
25.0
30.0


HFO-1123
Mass %
15.5
10.5
5.5
35.5
30.5
25.5
20.5
15.5


R1234yf
Mass %
35.0
35.0
35.0
40.0
40.0
40.0
40.0
40.0


R32
Mass %
14.5
14.5
14.5
14.5
14.5
14.5
14.5
14.5


GWP

100
100
100
100
100
100
100
100


COP ratio
% (relative to R410A)
98.3
98.7
99.1
97.4
97.7
98.0
98.3
98.6


Refrigerating
% (relative to R410A)
90.8
90.2
89.6
89.6
89.4
89.0
88.6
88.2


capacity ratio

























TABLE 34







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 35





Item
Unit
Comp. Ex. 91
Comp. Ex. 92
Comp. Ex. 93
Comp. Ex. 94
Comp. 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 to R410A)
98.9
99.1
99.4
99.7
100.0


Refrigerating
% (relative to R410A)
83.3
83.0
82.7
82.2
81.8


capacity ratio

























TABLE 36





Item
Unit
Ex. 161
Ex. 162
Ex. 163
Ex. 164
Ex. 165
Ex. 166
Ex. 167
Ex. 168
























HFO-1132(E)
Mass %
10.0
15.0
20.0
25.0
30.0
35.0
40.0
45.0


HFO-1123
Mass %
63.1
58.1
53.1
48.1
43.1
38.1
33.1
28.1


R1234yf
Mass %
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0


R32
Mass %
21.9
21.9
21.9
21.9
21.9
21.9
21.9
21.9


GWP

149
149
149
149
149
149
149
149


COP ratio
% (relative to R410A)
94.8
95.0
95.2
95.4
95.7
95.9
96.2
96.6


Refrigerating
% (relative to R410A)
111.5
111.2
110.9
110.5
110.0
109.5
108.9
108.3


capacity ratio

























TABLE 37





Item
Unit
Comp. Ex. 96
Ex. 169
Ex. 170
Ex. 171
Ex. 172
Ex. 173
Ex. 174
Ex. 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 38





Item
Unit
Ex. 176
Comp. Ex. 97
Ex. 177
Ex. 178
Ex. 179
Ex. 180
Ex. 181
Ex. 182
























HFO-1132(E)
Mass %
45.0
50.0
10.0
15.0
20.0
25.0
30.0
35.0


HFO-1123
Mass %
23.1
18.1
53.1
48.1
43.1
38.1
33.1
28.1


R1234yf
Mass %
10.0
10.0
15.0
15.0
15.0
15.0
15.0
15.0


R32
Mass %
21.9
21.9
21.9
21.9
21.9
21.9
21.9
21.9


GWP

149
149
149
149
149
149
149
149


COP ratio
% (relative to R410A)
97.0
97.4
95.7
95.9
96.1
96.3
96.6
96.9


Refrigerating
% (relative to R410A)
105.5
104.9
105.9
105.6
105.3
104.8
104.4
103.8


capacity ratio

























TABLE 39





Item
Unit
Ex. 183
Ex. 184
Comp. Ex. 98
Ex. 185
Ex. 186
Ex. 187
Ex. 188
Ex. 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
200


R32
Mass %
21.9
21.9
21.9
21.9
21.9
21.9
21.9
21.9


GWP

149
149
149
149
149
149
149
149


COP ratio
% (relative to R410A)
97.2
97.5
97.9
96.1
96.3
96.5
96.8
97.1


Refrigerating
% (relative to R410A)
103.3
102.6
102.0
103.0
102.7
102.3
101.9
101.4


capacity ratio

























TABLE 40










Comp.








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


Item
Unit
190
191
192
99
193
194
195
196
























HFO-1132 (E)
Mass %
35.0
40.0
45.0
50.0
10.0
15.0
20.0
25.0


HFO-1123
Mass %
23.1
18.1
13.1
8.1
43.1
38.1
33.1
28.1


R1234yf
Mass %
20.0
20.0
20.0
20.0
25.0
25.0
25.0
250


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
973



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 41











Comp.







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


Item
Unit
197
198
199
200
100
201
202
203
























HFO-1132 (E)
Mass %
30.0
35.0
40.0
45.0
50.0
10.0
15.0
20.0


HFO-1123
Mass %
23.1
18.1
13.1
8.1
3.1
38.1
33.1
28.1


R1234yf
Mass %
25.0
25.0
25.0
25.0
25.0
30.0
30.0
30.0


R32
Mass %
21.9
21.9
21.9
21.9
21.9
21.9
21.9
21.9


GWP

149
149
149
149
149
150
150
150


COP ratio
% (relative
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 42







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
97.2
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 43







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 44














Comp.




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


Item
Unit
220
221
222
223
224
225
226
101
























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


HFO-1123
Mass %
8.1
3.1
23.1
18.1
13.1
8.1
3.1
18.1


R1234yf
Mass %
40.0
40.0
45.0
45.0
45.0
45.0
45.0
50.0


R32
Mass %
21.9
21.9
21.9
21.9
21.9
21.9
21.9
21.9


GWP

150
150
150
150
150
150
150
150


COP ratio
% (relative
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 45









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 46














Comp.




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


Item
Unit
227
228
229
230
231
232
233
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 47














Comp.




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


Item
Unit
234
235
2.36
237
238
239
240
106
























HFO-1132 (E)
Mass %
10.0
15.0
20.0
25.0
30.0
35.0
40.0
45.0


HFO-1123
Mass %
50.7
45.7
40.1
35.7
30.3
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 R410A)










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


capacity ratio
to R410A)

























TABLE 48














Comp.




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


Item
Unit
241
242
243
244
245
246
247
107
























HFO-1132 (E)
Mass %
10.0
15.0
20.0
25.0
30.0
35.0
40.0
45.0


HFO-1123
Mass %
45.7
40.7
35.7
30.7
25.7
20.7
15.7
10.7


R1234yf
Mass %
15.0
15.0
15.0
15.0
15.0
15.0
15.0
15.0


R32
Mass %
29.3
29.3
29.3
29.3
29.3
29.3
29.3
29.3


GWP

199
199
199
199
199
199
199
199


COP ratio
% (relative
96.7
96.8
97.0
97.2
97.4
97.7
97.9
98.2



to R410A)










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


capacity ratio
to R410A)

























TABLE 49














Comp.




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


Item
Unit
241
242
243
244
245
246
247
107
























HFO-1132 (E)
Mass %
10.0
15.0
20.0
25.0
30.0
35.0
40.0
45.0


HFO-1123
Mass %
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 50







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 %
25.3
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 51







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 52







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











to R410A)
99.2
99.4
99.1
99.3
99.5
99.7
99.7
99.8


Refrigerating
% (relative










capacity ratio
to R410A)
93.6
93.2
91.5
91.3
90.9
90.6
88.4
88.1





















TABLE 53









Comp.
Comp.


Item
Unit
Ex. 279
Ex. 280
Ex 109
Ex. 110




















HFO-1132 (E)
Mass %
20.0
10.0
15.0
10.0


HFO-1123
Mass %
5.7
10.7
5.7
5.7


R1234yf
Mass %
45.0
50.0
50.0
55.0


R32
Mass %
29.3
29.3
29.3
29.3


GWP

200
200
200
200


COP ratio
% (relative
100.0
100.3
100.4
100.9



to R410A)






Refrigerating
% (relative
87.8
85.2
85.0
82.0


capacity ratio
to R410A)

























TABLE 54












Comp.






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


Item
Unit
281
282
283
224
285
111
286
287
























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


HFO-1123
Mass %
40.9
35.9
30.9
25.9
20.9
15.9
35.9
30.9


R1234yf
Mass %
5.0
5.0
5.0
5.0
5.0
5.0
10.0
10.0


R32
Mass %
44.1
94.1
44.1
94.1
44.3
44.1
94.1
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 55










Comp.








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


Item
Unit
288
289
290
112
291
292
293
294
























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


HFO-1123
Mass %
25.9
20.9
15.9
10.9
30.9
25.9
20.9
15.9


R1234yf
Mass %
10.0
10.0
10.0
10.0
15.0
15.0
15.0
15.0


R32
Mass %
44.1
44.1
44.1
44.1
44.1
41.1
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 56








Comp.










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


Item
Unit
295
113
296
297
298
299
300
301
























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


HFO-1123
Mass %
10.9
5.9
25.9
20.9
15.9
10.9
5.9
20.9


R1234yf
Mass %
15.0
15.0
20.0
20.0
20.0
20.0
20.0
25.0


R32
Mass %
44.1
44.1
44.1
44.1
44.1
44.1
44.1
44.1


GWP

299
299
299
299
299
299
299
299


COP ratio
% (relative
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 57





Item
Unit
Ex. 302
Ex. 303
Ex. 304
Ex. 305
Ex. 306
Ex. 307
Ex. 308
Ex. 309
























HFO-1132(E)
Mass %
15.0
20.0
25.0
10.0
15.0
20.0
10.0
15.0


HFO-1123
Mass %
15.9
10.9
5.9
15.9
10.9
5.9
10.9
5.9


R1234yf
Mass %
25.0
25.0
25.0
30.0
30.0
30.0
35.0
35.0


R32
Mass %
44.1
44.1
44.1
44.1
44.1
44.1
44.1
44.1


GWP

299
299
299
299
299
299
299
299


COP ratio
% (relative to R410A)
99.5
99.6
99.7
99.8
99.9
100.0
1003
100.4


Refrigerating capacity ratio
% (relative to R410A)
101.0
100.7
100.3
98.3
98.0
97.8
95.3
95.1




















TABLE 58







Item
Unit
Ex 400




















HFO-1132 (E)
Mass %
10.0



HFO-1123
Mass %
5.9



R1234yf
Mass %
40.0



R32
Mass %
44.1



GWP

299



COP ratio
% (relative to R410A)
100.7



Refrigerating capacity ratio
% (relative to R410A)
92.3










The above results indicate that the refrigerating capacity ratio relative to R410A is 85% or more in the following cases:


When the mass % of HFO-1132(E), HFO-1123, R1234yf, and R32 based on their sum is respectively represented by x, y, z, and a, in a ternary composition diagram in which the sum of HFO-1132(E), HFO-1123, and R1234yf is (100−a) mass %, a straight line connecting a point (0.0, 100.0−a, 0.0) and a point (0.0, 0.0, 100.0−a) is the base, and the point (0.0, 100.0−a, 0.0) is on the left side, if 0<a≤11.1, coordinates (x, y, z) in the ternary composition diagram are on, or on the left side of, a straight line AB that connects point A (0.0134a2−1.9681a+68.6, 0.0, −0.0134a2+0.9681a+31.4) and point B (0.0, 0.0144a2−1.6377a+58.7, −0.0144a2+0.6377a+41.3);


if 11.1<a≤18.2, coordinates (x,y,z) in the ternary composition diagram are on, or on the left side of, a straight line AB that connects point A (0.0112a2−1.9337a+68.484, 0.0, −0.0112a2+0.9337a+31.516) and point B (0.0, 0.0075a2−1.5156a+58.199, −0.0075a2+0.5156a+41.801);


if 18.2a<a≤26.7, coordinates (x,y,z) in the ternary composition diagram are on, or on the left side of, a straight line AB that connects point A (0.0107a2−1.9142a+68.305, 0.0, −0.0107a2+0.9142a+31.695) and point B (0.0, 0.009a2−1.6045a+59.318, −0.009a2+0.6045a+40.682);


if 26.7<a≤36.7, coordinates (x,y,z) in the ternary composition diagram are on, or on the left side of, a straight line AB that connects point A (0.0103a2−1.9225a+68.793, 0.0, −0.0103a2+0.9225a+31.207) and point B (0.0, 0.0046a2−1.41a+57.286, −0.0046a2+0.41a+42.714); and


if 36.7<a≤46.7, coordinates (x,y,z) in the ternary composition diagram are on, or on the left side of, a straight line AB that connects point A (0.0085a2−1.8102a+67.1, 0.0, −0.0085a2+0.8102a+32.9) and point B (0.0, 0.0012a2−1.1659a+52.95, −0.0012a2+0.1659a+47.05).


Actual points having a refrigerating capacity ratio of 85% or more form a curved line that connects point A and point B, 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. 2, the COP ratio of 92.5% ox more forms a


curved line CD. In FIG. 2, 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. 3, 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 PC.


The results are shown in Tables 59 to 66.















TABLE 59





Item
Comp. Ex. 6
Comp. Ex. 13
Comp. Ex. 19
Comp. Ex. 24
Comp. Ex. 29
Comp. 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 60





Item
Comp. Ex. 39
Comp. Ex. 45
Comp. Ex. 51
Comp. Ex. 57
Comp. 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 61





Item
Comp. Ex. 7
Comp. Ex. 14
Comp. Ex. 20
Comp. Ex. 25
Comp. Ex. 30
Comp. 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 62





Item
Comp. Ex. 40
Comp. Ex. 46
Comp. Ex. 52
Comp. Ex. 58
Comp. 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 63





Item
Comp. Ex. 8
Comp. Ex. 15
Comp. Ex. 21
Comp. Ex. 26
Comp. Ex. 31
Comp. Ex. 36























WCF
HFO-1132
Mass %
47.1
40.5
37.0
34.3
32.0
30.3



(E)










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
Storage/
Storage/
Storage/
Storage/
Storage/
Storage/


WCFF
Shipping
Shipping
Shipping
Shipping
Shipping
Shipping



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



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



liquid phase
liquid phase
liquid phase
liquid phase
liquid phase
liquid phase



side
side
side
side
side
side















WCFF
HFO-1132
Mass %
72.0
62.4
56.2
50.6
45.1
40.0



(E)










HFO-1123
Mass %
28.0
31.6
33.0
33.4
32.5
30.5



R1234yf
Mass %
0.0
0.0
0.0
20.4
0.0
0.0



R32
Mass %
0.0
50.9
10.8
16.0
22.4
29.5














Burning velocity
cm/s
8 or less
8 or less
8 or less
8 or less
8 or less
8 or less


(WCF)









Burning velocity
cm/s
10
10
10
10
10
10


(WCFF)




























TABLE 64





Item
Comp. Ex. 41
Comp. Ex. 47
Comp. Ex. 53
Comp. Ex. 59
Comp. 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/Shipping
Storage/Shipping
Storage/Shipping
Storage/Shipping
Storage/Shipping



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



92% release,
92% release,
92% release,
90% release,
86% release,



liquid phase side
liquid phase side
liquid phase side
gas phase side
gas 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 65





Item
Comp. Ex. 9
Comp. Ex. 16
Comp. Ex. 22
Comp. Ex. 27
Comp. Ex. 32
Comp. 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
Shipping
Shipping
Shipping
Shipping
Shipping



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



0% release,
0% release,
0% release,
92% release,
0% release,
0% release,


















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





side
side
side
side
side
side


WCFF
HFO-1132(E)
Mass %
72.0
56.2
50.4
46.0
42.4
39.1



HFO-1123
Mass %
10.5
12.6
11.4
10.1
7.4
4.4



R1234yf
Mass %
17.5
20.4
21.8
22.9
24.3
25.7



R32
Mass %
0.0
10.8
16.3
21.0
25.9
30.8














Burning velocity (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 66







Item
Comp. Ex. 42
Comp. Ex. 48
Comp. Ex. 54
Comp. Ex. 60
Comp. 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/Shipping
Storage/Shipping
Storage/Shipping
Storage/Shipping
Storage/Shipping

















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





0% release,
0% release
0% release,
0% release,
0% release,





gas phase side
gas phase side
gas phase side
gas phase side
gas 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 59 to 62 indicate that the refrigerant has a WCF lower flammability in the following cases:


When then 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 67) and point I (Table 68) were individually obtained in each of the following five ranges by calculation, and their approximate expressions were obtained.












TABLE 67







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 68







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 63 to 66 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′(0.034a2−2.1977a+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, −0.0183a+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) 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 69) and point K′ (Table 70) were individually obtained in each of the following five ranges by calculation, and their approximate expressions were obtained.












TABLE 69







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
46.7 ≥ 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 70







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. 2 to 12 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 71).












TABLE 71







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 72).












TABLE 72







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 73).












TABLE 73







Item
11.1 ≥ R32 > 0





















R32
0
7.1
11.1



HFO-1132 (E)
0
0
0



HFO-1123
75.4
83.4
88.9



R1234yf
24.6
9.5
0










R32
a



HFO-1132 (E)




Approximate
0



expression




HFO-1123
 0.0224a2 + 0.968a + 75.4



Approximate




expression




R1234yf
−0.0224a2 − 1.968a + 24.6



Approximate




expression










Point C is a point where the content of R1234yf is 0 mass %, and a COP ratio of 95.5% relative to that of R410A is achieved.


Three points corresponding to point C were obtained in each of the following by calculation, and their approximate expressions were obtained (Table 74).












TABLE 74







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




Approximate
0



expression










DESCRIPTION OF REFERENCE NUMERALS




  • 1: Sample cell


  • 2: High-speed camera


  • 3: Xenon lamp


  • 4: Collimating lens


  • 5: Collimating lens


  • 6: Ring filter


Claims
  • 1. A composition comprising a refrigerant, the refrigerant comprising trans-1,2-difluoroethylene (HFO-1132(E)), trifluoroethylene (HFO-1123), 2,3,3,3-tetrafluoro-1-propene (R1234yf), and difluoromethane (R32),
  • 2. A composition comprising a refrigerant, the refrigerant comprising trans-1,2-difluoroethylene (HFO-1132(E)), trifluoroethylene (HFO-1123), 2,3,3,3-tetrafluoro-1-propene (R1234yf), and difluoromethane (R32),
  • 3. The composition according to claim 1, for use as a working fluid for a refrigerating machine, wherein the composition further comprises a refrigerant oil.
  • 4. The composition according to claim 1, for use as an alternative refrigerant for R410A.
  • 5. A refrigerating machine designed for operation using R410A comprising the composition according to claim 1 as a working fluid.
  • 6. A method for operating a refrigerating machine designed for operation using R410A, comprising the step of circulating the composition according to claim 1 as a working fluid in the refrigerating machine.
  • 7. The composition according to claim 2, for use as a working fluid for a refrigerating machine, wherein the composition further comprises a refrigerant oil.
  • 8. The composition according to claim 2, for use as an alternative refrigerant for R410A.
  • 9. The composition according to claim 3, for use as an alternative refrigerant for R410A.
  • 10. The composition according to claim 7, for use as an alternative refrigerant for R410A.
  • 11. A refrigerating machine designed for operation using R410A comprising the composition according to claim 2 as a working fluid.
  • 12. A refrigerating machine designed for operation using R410A comprising the composition according to claim 3 as a working fluid.
  • 13. A refrigerating machine designed for operation using R410A comprising the composition according to claim 7 as a working fluid.
  • 14. A method for operating a refrigerating machine designed for operation using R410A, comprising the step of circulating the composition according to claim 2 as a working fluid in the refrigerating machine.
  • 15. A method for operating a refrigerating machine designed for operation using R410A, comprising the step of circulating the composition according to claim 3 as a working fluid in the refrigerating machine.
  • 16. A method for operating a refrigerating machine designed for operation using R410A, comprising the step of circulating the composition according to claim 7 as a working fluid in the refrigerating machine.
Priority Claims (1)
Number Date Country Kind
JP2017-242185 Dec 2017 JP national
PCT Information
Filing Document Filing Date Country Kind
PCT/JP2018/038749 10/17/2018 WO
Publishing Document Publishing Date Country Kind
WO2019/123807 6/27/2019 WO A
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Related Publications (1)
Number Date Country
20200385620 A1 Dec 2020 US