Composition containing mixture of fluorinated hydrocarbons, and use thereof

Information

  • Patent Grant
  • 10800958
  • Patent Number
    10,800,958
  • Date Filed
    Tuesday, November 15, 2016
    8 years ago
  • Date Issued
    Tuesday, October 13, 2020
    4 years ago
Abstract
The present invention provides a refrigerant composition that has a low GWP and ASHRAE non-flammability performance. Specifically, the present invention provides a composition comprising a mixture of fluorinated hydrocarbons, the mixture comprising difluoromethane (R32), pentafluoroethane (R125), 1,1,1,2-tetrafluoroethane (R134a), and 2,3,3,3-tetrafluoropropene (1234yf) at specific concentrations.
Description
TECHNICAL FIELD

The present invention relates to a composition comprising a mixture of fluorinated hydrocarbons that are used as, for example, a refrigerant; and use thereof. The present invention also includes a case in which the composition consists of the four basic components contained in the mixture, i.e., difluoromethane (R32), pentafluoroethane (R125), 2,3,3,3-tetrafluoropropene (1234yf), and 1,1,1,2-tetrafluoroethane (R134a).


BACKGROUND ART

Refrigerants recently used, for example, for air conditioners, refrigerating devices, and refrigerators, are mixtures of fluorinated hydrocarbons that contain no chlorine in their molecular structures, such as difluoromethane (CH2F2, R32, boiling point: −52° C.), pentafluoroethane (CF3CHF2, R125, boiling point: −48° C.), 1,1,1-trifluoroethane (CF3CH3, R143a, boiling point: −47° C.), 1,1,1,2-tetrafluoroethane (CF3CH2F, R134a, boiling point: −26° C.), 1,1-difluoroethane (CHF2CH3, R152a, boiling point: −24° C.), and 2,3,3,3-tetrafluoropropene (CF3CF═CH2, 1234yf, boiling point: −29° C.).


Among the above fluorinated hydrocarbons, a ternary mixed refrigerant of R32/R125/R134a in which the proportions thereof are 23/25/52 wt % (R407C), a ternary mixed refrigerant of R125/143a/R134a in which the proportions thereof are 44/52/4 wt % (R404A), etc., have been proposed, and R404A is currently widely used as a refrigerant for freezing and refrigerated storage (for example, Patent Literature 1 and 2).


However, the global warming potential (GWP) of R404A is as high as 3922, which is equal to that of CHClF2 (R22), which is a chlorine-containing fluorinated hydrocarbon. There is thus a desire to develop, as alternative refrigerants for R404A, refrigerants that have a refrigerating capacity equal to that of R404A, a lower GWP, and performance of non-flammable refrigerants (ASHRAE non-flammability (class 1 refrigerants defined in ANSI/ASHRAE 34-2013)), as with R404A.


There are still many refrigerating devices that use CHClF2 (R22) as chlorine-containing fluorinated hydrocarbons (HCFCs), which were used as refrigerants for freezing and refrigerated storage prior to the use of R404A; however, under the Montreal Protocol, HCFCs are required to be abolished by 2020 in developed countries, and to be phased out (first: 10%, second: 35%) in developing countries. For these refrigerating devices, there is also a desire to develop, as alternative refrigerants for R22, refrigerants that have a compressor outlet pressure equal to that of R22 used in a refrigeration cycle (“R22 retrofit refrigerants”), a lower GWP, and performance of non-flammable refrigerants (ASHRAE non-flammability (class 1 refrigerants defined in ANSI/ASHRAE 34-2013)), as with R22.


There are, for example, Patent Literature 3 and 4 as other prior art relating to the present invention.


CITATION LIST
Patent Literature

PTL 1: JP2869038B


PTL 2: U.S. Pat. No. 8,168,077


PTL 3: JP5689068B


PTL 4: JP2013-529703A


SUMMARY OF INVENTION
Technical Problem

Patent Literature 3 and 4 report, as alternative refrigerants for R404A, refrigerant compositions comprising difluoromethane (R32), pentafluoroethane (R125), 2,3,3,3-tetrafluoropropene (1234yf), and 1,1,1,2-tetrafluoroethane (R134a). However, no one has succeeded in developing a refrigerant composition that has a refrigerating capacity equal to that of R404A, a lower GWP, and ASHRAE non-flammability performance.


An object of the present invention is to provide a refrigerant composition that has a low GWP and ASHRAE non-flammability performance. Another object of the present invention is to provide, as preferable embodiments, a refrigerant composition that has a refrigerating capacity equal to that of currently widely used R404A, a lower GWP, and ASHRAE non-flammability performance, a refrigerant composition that has a compressor outlet pressure equal to that of R22, a lower GWP, and ASHRAE non-flammability performance, and the like.


Solution to Problem

The present inventors conducted extensive research to achieve the above object, and consequently found that the above object can be achieved by a composition comprising a mixture of fluorinated hydrocarbons, the mixture comprising difluoromethane (R32), pentafluoroethane (R125), 2,3,3,3-tetrafluoropropene (1234yf), and 1,1,1,2-tetrafluoroethane (R134a) at specific concentrations. Thus, the present invention has been accomplished.


Specifically, the present invention provides the following compositions and use thereof.


1. A composition comprising a mixture or mixtures of fluorinated hydrocarbons;


the composition comprising at least one member selected from the group consisting of the following mixtures 1 to 6, wherein the composition ratio of the fluorinated hydrocarbons contained in each mixture is indicated in a ternary composition diagram in which the sum of the concentrations of R125, 1234yf, and R134a is represented by (100−x) wt %, when the sum of the concentrations of R32, R125, 1234yf, and R134a is 100 wt %, and the concentration of R32 is x wt %:


mixture 1 having a composition ratio in which


(1)-1. 14.8 wt %>x≥10.8 wt %, and


(2)-1. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a pentagon having the following points as vertices:


point G (100−R32−1234yf−R134a/−0.5493x+45.325/−0.4243x+19.875),


point H (100−R32−1234yf-R134a/−0.9507x+60.575/−x+38.1),


point I (0/100−R32−1234yf−R134a/1.6974x+48.4),


point N (0/0/100−x), and


point D (0.375x+3.25/0/100−R32−R125−1234yf);


mixture 2 having a composition ratio in which


(1)-2. 18.1 wt %>x≥14.8 wt %, and


(2)-2. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a pentagon having the following points as vertices:


point G (100−R32−R125−1234yf/−0.5736x+45.669/−0.3945x+19.443),


point H (100−R32−1234yf−R134a/−0.9083x+59.936/−0.9723x+37.714),


point I (0/100−R32−1234yf−R134a/1.3625x+53.346),


point N (0/0/100−x), and


point D (0.3625x+3.4461/0/100−R32−R125−1234yf);


mixture 3 having a composition ratio in which


(1)-3. 20.0 wt %>x≥18.1 wt %, and


(2)-3. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a pentagon having the following points as vertices:


point G (100−R32−1234yf−R134a/−0.5258x+44.808/−0.4207x+19.907),


point H (100−R32−1234yf−R134a/−0.8948x+59.698/−1.0517x+39.117),


point I (0/100−R32−1234yf−R134a/1.0517x+58.983),


point N (0/0/100−x), and


point D (0.369x+3.31/0/100−R32−R125−1234yf);


mixture 4 having a composition ratio in which


(1)-4. 22.6 wt %>x≥20.0 wt %, and


(2)-4. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a quadrilateral having the following points as vertices:


point G (100−R32−1234yf−R134a/−0.5756x+45.817/−0.4244x+19.983),


point H (100−R32−1234yf−R134a/−0.9244x+60.283/−0.8488x+35.065),


point I (100−R32−1234yf−R134a/0/−2.0407x+120.8), and


point D (0.3430x+3.826/0/100−R32−R125−1234yf);


mixture 5 having a composition ratio in which


(1)-5. 24.5 wt %>x≥22.6 wt %, and


(2)-5. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a quadrilateral having the following points as vertices:


point G (100−R32−1234yf−R134a/−0.5283x+44.746/−0.4717x+21.054),


point H (100−R32−1234yf−R134a/−0.9435x+60.078/−0.8428x+34.949),


point I (100−R32−1234yf−R134a/0/−1.9435x+118.61), and


point D (0.3710x+3.2057/0/100−R32−R125−1234yf); and


mixture 6 having a composition ratio in which


(1)-6. 26.6 wt %≥x≥24.5 wt %, and


(2)-6. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a quadrilateral having the following points as vertices:


point G (100−R32−1234yf−R134a/−0.5710x+45.798/−0.4290x+20.002),


point H (100−R32−1234yf−R134a/−0.9517x+60.931/−0.7613x+32.965),


point I (100−R32−1234yf−R134a/0/−2.0000x+120.00), and


point D (0.3323x+4.1369/0/100−R32−R125−1234yf).


2. A composition comprising a mixture or mixtures of fluorinated hydrocarbons;


the composition comprising at least one member selected from the group consisting of the following mixtures 1 to 6, wherein the composition ratio of the fluorinated hydrocarbons contained in each mixture is indicated in a ternary composition diagram in which the sum of the concentrations of R125, 1234yf, and R134a is represented by (100−x) wt %, when the sum of the concentrations of R32, R125, 1234yf, and R134a is 100 wt %, and the concentration of R32 is x wt %:


mixture 1 having a composition ratio in which


(1)-1. 14.8 wt %>x≥10.8 wt %, and


(2)-1. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a pentagon having the following points as vertices:


point G′ (100−R32−1234yf−R134a/−0.5757x+45.025/−0.4243x+20.975),


point H′ (100−R32−1234yf−R134a/−0.9770x+59.575/−x+38.4),


point I′ (0/100−R32−1234yf−R134a/1.7007x+52.125),


point N (0/0/100−x), and


point D (0.375x+3.25/0/100−R32−R125−1234yf);


mixture 2 having a composition ratio in which


(1)-2. 18.1 wt %>x≥14.8 wt %, and


(2)-2. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a pentagon having the following points as vertices:


point G′ (100−R32−1234yf−R134a/−0.5458x+44.582/−0.4264x+21.031),


point H′ (100−R32−1234yf−R134a/−0.9083x+58.536/−0.9723x+38.014),


point I′ (0/100−R32−1234yf−R134a/1.3945x+56.657),


point N (0/0/100−x), and


point D (0.3625x+3.4461/0/100−R32−R125−1234yf);


mixture 3 having a composition ratio in which


(1)-3. 20.0 wt %>x≥18.1 wt %, and


(2)-3. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a quadrilateral having the following points as vertices:


point G′ (100−R32−1234yf−R134a/−0.5277x+44.277/−0.4207x+20.907),


point H′ (100−R32−1234yf−R134a/−0.8948x+58.298/−1.0517x+39.417),


point I′ (100−R32−1234yf−R134a/0/1.9483x+117.18), and


point D (0.369x+3.31/0/100−R32−R125−1234yf);


mixture 4 having a composition ratio in which


(1)-4. 22.6 wt %>x≥20.0 wt %, and


(2)-4. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a quadrilateral having the following points as vertices:


point G′ (100−R32−1234yf−R134a/−0.5349x+44.413/−0.4651x+21.787),


point H′ (100−R32−1234yf−R134a/−0.9244x+58.883/−0.8837x+36.078),


point I′ (100−R32−1234yf−R134a/0/−2.0756x+119.72), and


point D (0.343x+3.826/0/100−R32−R125−1234yf);


mixture 5 having a composition ratio in which


(1)-5. 24.5 wt %>x≥22.6 wt %, and


(2)-5. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a quadrilateral having the following points as vertices:


point G′ (100−R32−1234yf−R134a/−0.5848x+45.537/−0.4717x+21.954),


point H′ (100−R32−1234yf−R134a/−0.9435x+59.308/−0.8428x+35.149),


point I′ (100−R32−1234yf−R134a/0/−1.9435x+116.71), and


point D (0.3710x+3.2057/0/100−R32−R125−1234yf); and


mixture 6 having a composition ratio in which


(1)-6. 26.6 wt %≥x≥24.5 wt %, and


(2)-6. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a quadrilateral having the following points as vertices:


point G′ (100−R32−1234yf−R134a/−0.5242x+44.035/−0.4290x+20.902),


point H′ (100−R32−1234yf−R134a/−x+60.7/−0.7145x+32.001),


point I′ (100−R32−1234yf−R134a/0/−2.0468x+119.26), and


point D (0.3323x+4.1369/0/100−R32−R125−1234yf).


3. A composition comprising a mixture or mixtures of fluorinated hydrocarbons;


the composition comprising at least one member selected from the group consisting of the following mixtures 1 to 7, wherein the composition ratio of the fluorinated hydrocarbons contained in each mixture is indicated in a ternary composition diagram in which the sum of the concentrations of R125, 1234yf, and R134a is represented by (100−x) wt %, when the sum of the concentrations of R32, R125, 1234yf, and R134a is 100 wt %, and the concentration of R32 is x wt %:


mixture 1 having a composition ratio in which


(1)-1. 14.1 wt %>x≥10.8 wt %, and


(2)-1. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a quadrilateral having the following points as vertices:


point B (−2.6665x+62.786/0.7204x+31.027/100−R32−R125−1234yf),


point C (0.0914x2−4.2444x+69.184/0.1181x2−6.3648x+93.765/100−R32−R125−1234yf),


point F (0.0323x2−2.5621x+50.802/0.0346x2−3.9904x+67.56/100−R32−R125−1234yf), and


point E (0.0501x2−3.9756x+61.989/−0.0296x2+1.5133x+30.248/100−R32−R125−1234yf);


mixture 2 having a composition ratio in which


(1)-2. 16.1 wt %>x≥14.1 wt %, and


(2)-2. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a pentagon having the following points as vertices:


point B (−2.6456x+62.484/0.7929x+29.984/100−R32−R125−1234yf),


point C (0.0495x2−3.1434x+61.991/0.1723x2−8.1236x+107.78/100−R32−R125−1234yf),


point F (−1.5049x+42.339/−2.6349x+55.315/100−R32−R125−1234yf),


point E (0.2747x2−9.7967x+99.415/0.6366x2−25.375x+276.93/100−R32−R125−1234yf), and


when 14.8 wt %>x≥14.1 wt %,


point H′ (100−R32−1234yf−R134a/−0.9770x+59.575/−x+38.4), or


when 16.1 wt %>x≥14.8 wt %,


point H′ (100−R32−1234yf−R134a/−0.9083x+58.536/−0.9723x+38.014);


mixture 3 having a composition ratio in which


(1)-3. 16.8 wt %>x≥16.1 wt %, and


(2)-3. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a pentagon having the following points as vertices:


point B (−2.2857x+56.7/0.7747x+30.285/100−R32−R125−1234yf),


point C (−1.5714x+49.5/−2.8043x+66.812/100−R32−R125−1234yf),


point F (−1.2857x+38.8/−2.4954x+53.076/100−R32−R125−1234yf),


point E (−1.1429x+31.3/−5.3142x+118.96/100−R32−R125−1234yf), and


point H′ (100−R32−1234yf−R134a/−0.9083x+58.536/−0.9723x+38.014);


mixture 4 having a composition ratio in which


(1)-4. 18.1 wt %>x≥16.8 wt %, and


(2)-4. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a quadrilateral having the following points as vertices:


point B (−1.4615x+42.854/−5.931x+142.94/100−R32−1234yf−R134a),


point C (−1.3846x+46.362/−2.5156x+61.961/100−R32−R125−1234yf),


point F (−1.3846x+40.462/−2.5401x+53.827/100−R32−R125−1234yf), and


point E (−1.0769x+30.192/−4.9692x+113.16/100−R32−R125−1234yf);


mixture 5 having a composition ratio in which


(1)-5. 20.0 wt %>x≥18.1 wt %, and


(2)-5. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a quadrilateral having the following points as vertices:


point B (−1.0442x+35.27/0.2703x2−15.221x+222.52/100−R32−1234yf-R134a),


point C (−1.3145x+45.088/−2.4404x+60.615/100−R32−1234yf−R134a),


point F (−1.2138x+37.381/−0.1576x2+3.716x−7.7649/100−R32−1234yf−R134a), and


point E (−0.8869x+26.726/−4.3267x+101.52/100−R32−1234yf−R134a);


mixture 6 having a composition ratio in which


(1)-6. 21.6 wt %>x≥20.0 wt %, and


(2)-6. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a quadrilateral having the following points as vertices:


point B (−0.875x+31.9/−4.3372x+112.98/100−R32−1234yf−R134a),


point C (−1.25x+43.8/−2.375x+59.3/100−R32−1234yf−R134a),


point F (−1.125x+35.6/−2.1875x+47.25/100−R32−1234yf−R134a), and


point E (−0.75x+24/−3.8831x+92.657/100−R32−1234yf−R134a); and


mixture 7 having a composition ratio in which


(1)-7. 24.2 wt %>x≥21.6 wt, and


(2)-7. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a quadrilateral having the following points as vertices:


point B (−0.7267x+28.67/0.1603x2−10.987x+181.821/00−R32−1234yf−R134a),


point C (0.0529x2−3.5375x+68.536/0.0431x2−4.1038x+76.546/100−R32−1234yf−R134a),


point F (−1.9651x+53.771/0/100−R32−1234yf−R134a), and


point E (−0.6163x+21.118/0.0663x2−6.4133x+116.38/100−R32−1234yf−R134a).


4. A composition comprising a mixture or mixtures of fluorinated hydrocarbons,


the composition comprising at least one member selected from the group consisting of the following mixtures 1 to 9, wherein the composition ratio of the fluorinated hydrocarbons contained in each mixture is indicated in a ternary composition diagram in which the sum of the concentrations of R125, 1234yf, and R134a is represented by (100−x) wt %, when the sum of the concentrations of R32, R125, 1234yf, and R134a is 100 wt %, and the concentration of R32 is x wt %:


mixture 1 having a composition ratio in which


(1)-1. 14.2 wt %>x≥11.6 wt %, and


(2)-1. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a triangle having the following points as vertices:


point G′ (100−R32−1234yf−R134a/−0.5757x+45.025/−0.4243x+20.975),


point J (−3.5769x+75.492/1.2204x+24.143/100−R32−R125−1234yf), and


point K (−2.3846x+61.662/−4.0172x+84.9/100−R32−R125−1234yf);


mixture 2 having a composition ratio in which


(1)-2. 15.3 wt %>x≥14.2 wt %, and


(2)-2. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a triangle having the following points as vertices:


when 14.8 wt %>x≥14.2 wt %,


point G′ (100−R32−1234yf−R134a/−0.5757x+45.025/−0.4243x+20.975) or


when 15.3 wt %>x≥14.8 wt %,


point G′ (100−R32−1234yf−R134a/−0.5458x+44.582/−0.4264x+21.031), and


point J (−3.4381x+73.493/1.1236x+25.522/100−R32−R125−1234yf), and


point K (0.9091x2−29.091x+257.58/0.8579x2−29.085x+267.88/100−R32−R125−1234yf);


mixture 3 having a composition ratio in which


(1)-3. 16.2 wt %>x≥15.3 wt %, and


(2)-3. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a triangle having the following points as vertices:


point G′ (100−R32−1234yf−R134a/−0.5458x+44.582/−0.4264x+21.031),


point J (−3.5556x+75.3/1.2095x+24.209/100−R32−R125−1234yf), and


point K (−2x+55.9/−3.4439x+76.392/100−R32−R125−1234yf);


mixture 4 having a composition ratio in which


(1)-4. 17.5 wt %>x≥16.2 wt %, and


(2)-4. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a quadrilateral having the following points as vertices:


point G′ (100−R32−1234yf−R134a/−0.5458x+44.582/−0.4264x+21.031),


point H′ (100−R32−1234yf−R134a/−0.9083x+58.536/−0.9723x+38.014),


point J (−1.6163x+43.882/−6.3674x+146.95/100−R32−R125−1234yf), and


point K (−1.8488x+53.445/−3.1206x+71.153/100−R32−R125−1234yf);


mixture 5 having a composition ratio in which


(1)-5. 19.0 wt %>x≥17.5 wt %, and


(2)-5. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a pentagon having the following points as vertices:


when 18.1 wt %>x≥17.5 wt %,


point G′ (100−R32−1234yf−R134a/−0.5458x+44.582/−0.4264x+21.031), and


point H′ (100−R32−1234yf−R134a/−0.9083x+58.536/−0.9723x+38.014), or


when 19.0 wt %>x≥18.1 wt %,


point G′ (100−R32−1234yf−R134a/−0.5277x+44.277/−0.4207x+20.907), and


point H′ (100−R32−1234yf−R134a/−0.8948x+58.298/−1.0517x+39.417), and


point J (0.1273x2−6.1109x+83.553/0.1532x2−11.484x+189.57/100−R32−R125−1234yf),


point X (−0.1696x2+1.0575x+54.537/−0.2271x2+15.05x−177.28/100−R32−R125−1234yf), and


point R (−0.0401x2+3.0217x−19.198/−0.0297x2+2.7774x−22.544/100−R32−R125−1234yf);


mixture 6 having a composition ratio in which


(1)-6. 20.8 wt %>x≥19.0 wt %, and


(2)-6. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a quadrilateral having the following points as vertices:


when 20.0 wt %>x≥19.0 wt %,


point G′ (100−R32−1234yf−R134a/−0.5277x+44.277/−0.4207x+20.907), and


point H′ (100−R32−1234yf−R134a/−0.8948x+58.298/−1.0517x+39.417), or


when 20.8 wt %>x≥20.0 wt %,


point G′ (100−R32−1234yf−R134a/−0.5349x+44.413/−0.4651x+21.787), and


point H′ (100−R32−1234yf−R134a/−0.9244x+58.883/−0.8837x+36.078), and


point Q (−0.0198x2+27.157x−31.225/−0.0377x2+3.0486x−17.594/100−R32−R125−1234yf), and


point R (−0.0401x2+3.0217x−19.198/−0.0297x2+2.7774x−22.544/100−R32−R125−1234yf);


mixture 7 having a composition ratio in which


(1)-7. 23.2 wt %>x≥20.8 wt %, and


(2)-7. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a quadrilateral having the following points as vertices:


when 22.6 wt %>x≥20.8 wt %,


point G′ (100−R32−1234yf−R134a/−0.5349x+44.413/−0.4651x+21.787), and


point H′ (100−R32−1234yf−R134a/−0.9244x+58.883/−0.8837x+36.078), or


when 23.2 wt %>x≥22.6 wt %,


point G′ (100−R32−1234yf−R134a/−0.5848x+45.537/−0.4717x+21.954), and


point H′ (100−R32−1234yf−R134a/−0.9435x+59.308/−0.8428x+35.149), and


point Q (−0.0984x2+6.1633x−68.728/−0.0617x2+3.9141x−25.243/100−R32−R125−1234yf), and


point R (−0.0031x2+1.5234x−4.0783/−0.0503x2+3.6856x−32.627/100−R32−R125−1234yf);


mixture 8 having a composition ratio in which


(1)-8. 25.6 wt %>x≥23.2 wt %, and


(2)-8. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a quadrilateral having the following points as vertices:


when 24.5 wt %>x≥23.2 wt %,


point G′ (100−R32−1234yf−R134a/−0.5848x+45.537/−0.4717x+21.954), and


point H′ (100−R32−1234yf−R134a/−0.9435x+59.308/−0.8428x+35.149), or


when 25.6 wt %>x≥24.5 wt %,


point G′ (100−R32−1234yf−R134a/−0.5242x+44.035/−0.4290x+20.902), and


point H′ (100−R32−1234yf−R134a/−x+60.7/−0.7145x+32.001), and


point Q (−0.0115x2+2.3422x−26.868/−0.1077x2+6.4104x−58.357/100−R32−R125−1234yf), and


point R (−0.1398x2+8.0281x−81.391/−0.0932x2+5.7935x−58.514/100−R32−R125−1234yf); and


mixture 9 having a composition ratio in which


(1)-9. 26.6 wt %≥x≥25.6 wt %, and


(2)-9. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a triangle having the following points as vertices:


point G′ (100−R32−1234yf−R134a/−0.5242x+44.035/−0.4290x+20.902),


point Q (8.2x−184.32/−5x+163.1/100−R32−R125−1234yf), and


point R (1.2x+1.88/1.246x−3.0431/100−R32−R125−1234yf).


5. A composition comprising a mixture or mixtures of fluorinated hydrocarbons;


the composition comprising at least one member selected from the group consisting of the following mixtures 1 to 7, wherein the composition ratio of the fluorinated hydrocarbons contained in each mixture is indicated in a ternary composition diagram in which the sum of the concentrations of R125, 1234yf, and R134a is represented by (100−x) wt %, when the sum of the concentrations of R32, R125, 1234yf, and R134a is 100 wt %, and the concentration of R32 is x wt %:


mixture 1 having a composition ratio in which


(1)-1. 15.3 wt %>x≥14.2 wt %, and


(2)-1. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a triangle having the following points as vertices:


point T (100−R32−1234yf−R134a/0.0415x2+1.0547x+21.254/0.0863x2−3.628x+64.252),


point K (0.9091x2−29.091x+257.58/0.8579x2−29.085x+267.88/100−R32−R125−1234yf), and


point U (1.3896x2−47.266x+418.78/−2.8422x2+97.299x−780.65/100−R32−R125−1234yf);


mixture 2 having a composition ratio in which


(1)-2. 16.2 wt %>x≥15.3 wt %, and


(2)-2. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a quadrilateral having the following points as vertices:


point S (100−R32−1234yf−R134a/0.0508x2−2.3591x+66.946/−0.0008x2−0.6861x+31.798),


point T (100−R32−1234yf−R134a/−0.0415x2+1.0547x+21.254/0.0863x2−3.628x+64.252),


point K (−2x+55.9/−3.4439x+76.392/100−R32−R125−1234yf), and


point J (−3.5556x+75.3/1.2095x+24.209/100−R32−R125−1234yf);


mixture 3 having a composition ratio in which


(1)-3. 17.5 wt %>x≥16.2 wt %, and


(2)-3. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a pentagon having the following points as vertices:


when 17.0 wt %>x≥16.2 wt %,


point S (100−R32−1234yf−R134a/0.0508x2−2.3591x+66.946/−0.0008x2−0.6861x+31.798), and


point T (100−R32−1234yf−R134a/−0.0415x2+1.0547x+21.254/0.0863x2−3.628x+64.252), or


when 17.5 wt %>x≥17.0 wt %,


point S (100−R32−1234yf−R134a/0.1108x2−4.5904x+87.503/0.0939x2−4.1798x+63.826), and


point T (100−R32−1234yf−R134a/−0.0766x2+2.5779x+5.5242/0.2286x2−9.3441x+120.28), and


point K (−1.8488x+53.445/−3.1206x+71.153/100−R32−R125−1234yf),


point J (−1.6163x+43.882/−6.3674x+146.95/100−R32−R125−1234yf), and


point H′ (100−R32−1234yf−R134a/−0.9083x+58.536/−0.9723x+38.014);


mixture 4 having a composition ratio in which


(1)-4. 19.0 wt %>x≥17.5 wt %, and


(2)-4. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a hexagon having the following points as vertices:


point S (100−R32−1234yf−R134a/0.1108x2−4.5904x+87.503/0.0939x2−4.1798x+63.826),


point T (100−R32−1234yf−R134a/−0.0766x2+2.5779x+5.5242/0.2286x2−9.3441x+120.28),


point R (−0.0401x2+3.0217x−19.198/−0.0297x2+2.7774x−22.544/100−R32−R125−1234yf),


point X (−0.1696x2+1.0575x+54.537/−0.2271x2+15.05x−177.28/100−R32−R125−1234yf),


point J (0.1273x2−6.1109x+83.553/0.1532x2−11.484x+189.57/100−R32−R125−1234yf), and


when 18.1 wt %>x≥17.5 wt %,


point H′ (100−R32−1234yf−R134a/−0.9083x+58.536/−0.9723x+38.014), or


when 19.0 wt %>x≥18.1 wt %,


point H′ (100−R32−1234yf−R134a/−0.8948x+58.298/−1.0517x+39.417);


mixture 5 having a composition ratio in which


(1)-5. 20.8 wt %>x≥19.0 wt %, and


(2)-5. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a pentagon having the following points as vertices:


point S (100−R32−1234yf−R134a/0.1263x2−5.6749x+102.56/−0.029x2+0.4298x+20.594),


point T (100−R32−1234yf−R134a/0.1451x2−6.0744x+89.981/−0.2364x2+8.5372x−51.582),


point R (−0.0401x2+3.0217x−19.198/−0.0297x2+2.7774x−22.544/100−R32−R125−1234yf),


point Q (−0.0198x2+27.157x−31.225/−0.0377x2+3.0486x−17.594/100−R32−R125−1234yf), and


when 20.0 wt %>x≥19.0 wt %,


point H′ (100−R32−1234yf−R134a/−0.8948x+58.298/−1.0517x+39.417), or


when 20.8 wt %>x≥20.0 wt %,


point H′ (100−R32−1234yf−R134a/−0.9244x+58.883/−0.8837x+36.078);


mixture 6 having a composition ratio in which


(1)-6. 23.2 wt %>x≥20.8 wt %, and


(2)-6. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a pentagon having the following points as vertices:


point S (100−R32−1234yf−R134a/0.1017x2−5.1872x+102.99/0.0034x2−0.7313x+30.692),


point T (100−R32−1234yf−R134a/−0.0318x2+1.1657x+15.869/−0.123x2+4.4541x−15.735),


point R (−0.0031x+1.5234x−4.0783/−0.0503x2+3.6856x−32.627/100−R32−R125−1234yf),


point Q (−0.0984x2+6.1633x−68.728/−0.0617x2+3.9141x−25.243/100−R32−R125−1234yf), and


when 22.6 wt %>x≥20.8 wt %,


point H′ (100−R32−1234yf−R134a/−0.9244x+58.883/−0.8837x+36.078), or


when 23.2 wt %>x≥22.6 wt %,


point H′ (100−R32−1234yf−R134a/−0.9435x+59.308/−0.8428x+35.149); and


mixture 7 having a composition ratio in which


(1)-7. 25.4 wt %≥x≥23.2 wt %, and


(2)-7. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a triangle having the following points as vertices:


point S (100−R32−1234yf−R134a/−0.0317x2+0.4511x+43.979/0.075x2−4.1913x+72.494),


point α (0.0324x2−3.5746x+95.092/0.0193x2+3.2487x−59.944/100−R32−R125−1234yf), and


point Q (−0.0115x2+2.3422x−26.868/−0.1077x2+6.4104x−58.357/100−R32−R125−1234yf).


6. A composition comprising a mixture of fluorinated hydrocarbons, the mixture comprising R32, R125, R134a, 1234yf, and at least one fluorinated hydrocarbon selected from the group consisting of HCFC-1122, HCFC-124, CFC-1113, and 3,3,3-trifluoropropyne.


7. A composition comprising a mixture of fluorinated hydrocarbons, the mixture comprising R32, R125, R134a, 1234yf, and at least one halogenated organic compound represented by formula (1): CmHnXp, wherein each X independently represents a fluorine atom, a chlorine atom, or a bromine atom, m is 1 or 2, 2m+2≥n+p, and p≥1.


8. A composition comprising a mixture of fluorinated hydrocarbons, the mixture comprising R32, R125, R134a, 1234yf, and at least one organic compound represented by formula (2): CmHnXp, wherein each X independently represents an atom that is not a halogen atom, m is 1 or 2, 2m+2≥n+p, and p≥1.


9. A composition comprising a mixture of fluorinated hydrocarbons, the mixture comprising R32, R125, R134a, 1234yf, and water.


10. The composition according to any one of items 1 to 9, comprising a refrigerant oil.


11. The composition according to item 10, wherein the refrigerant oil comprises at least one polymer selected from the group consisting of polyalkylene glycol (PAG), polyol ester (POE), and polyvinyl ether (PVE).


12. The composition according to any one of items 1, 2, and 4 to 11, wherein the composition is an alternative refrigerant for R404A (R125/R134a/R143a=44/4/52 wt %), which is a mixed refrigerant.


13. The composition according to any one of items 1 to 3 and 6 to 11, wherein the composition is an alternative refrigerant for R22, which is an HCFC refrigerant.


14. The composition according to any one of items 1 to 13, comprising at least one substance selected from the group consisting of tracers, compatibilizers, ultraviolet fluorescence dyes, stabilizers, and polymerization inhibitors.


15. The composition according to any one of items 1 to 14, wherein the composition consists of the mixture of fluorinated hydrocarbons.


16. A refrigeration method comprising the step of operating a refrigeration cycle using the composition according to any one of items 1 to 15.


17. A method for operating a refrigerating device, comprising operating a refrigeration cycle using the composition according to any one of items 1 to 15.


18. A refrigerating device comprising the composition according to any one of items 1 to 15.


19. The composition according to any one of items 1 to 15, which is used for at least one member selected from the group consisting of refrigerators, freezers, water coolers, ice machines, refrigerating showcases, freezing showcases, freezing and refrigerating units, refrigerating devices for freezing and refrigerating warehouses, chillers (chilling units), turbo refrigerators, and screw refrigerators.


Advantageous Effects of Invention

The composition of the present invention is a composition comprising a mixture of fluorinated hydrocarbons, the mixture comprising difluoromethane (R32), pentafluoroethane (R125), 2,3,3,3-tetrafluoropropene (1234yf), and 1,1,1,2-tetrafluoroethane (R134a) at specific concentrations, whereby the composition has a GWP of 1500 or less and ASHRAE non-flammability performance.





BRIEF DESCRIPTION OF DRAWINGS


FIG. 1 shows ASHRAE non-flammability limit compositions (six open circles) of a mixture of the four basic components: difluoromethane (R32), pentafluoroethane (R125), 2,3,3,3-tetrafluoropropene (1234yf), and 1,1,1,2-tetrafluoroethane (R134a), and regression lines connecting these points (a straight line connecting points G and H; and a straight line connecting points H and I), in a ternary composition diagram of R125, 1234yf, and R134a when the concentration of R32 is 22.6 wt %, determined from Experimental Example 1.



FIGS. 2 to 7 show the compositions of the above mixture (a pentagon surrounded by points G, H, I, N, and D; and a pentagon surrounded by points G′, H′, I′, N, and D) in a ternary composition diagram of R125, 1234yf, and R134a, when the concentration of R32 is 10.8, 12.4, 14.8, 16.1, 18.1, and 19.0 wt %. The 1234yf side from line segment AD shows a region with a GWP of 1500 or less, and the R125 side from line segments GHI (which mean line segment GH and line segment HI, which are collectively referred to as “line segments GHI”; hereinafter the same) shows a region showing ASHRAE non-flammability. The pentagon surrounded by points G, H, I, N, and D represents a region with a GWP of 1500 or less and showing ASHRAE non-flammability. The pentagon surrounded by points G′, H′, I′, N, and D represents a region with a GWP of 1500 or less and showing ASHRAE non-flammability in which safety ratio, described later, are taken into consideration for nonflammable refrigerants R134a and R125.



FIGS. 8 to 14 show the compositions of the above mixture (a quadrilateral surrounded by points G, H, I, and D; and a quadrilateral surrounded by points G′, H′, I′, and D) in a ternary composition diagram of R125, 1234yf, and R134a, when the concentration of R32 is 20.0, 21.6, 22.6, 23.2, 24.5, 25.6, and 26.6 wt %. The quadrilateral surrounded by points G, H, I, and D represents a region with a GWP of 1500 or less, and showing ASHRAE non-flammability. The quadrilateral surrounded by points G′, H′, I′, and D represents a region with a GWP of 1500 or less and showing ASHRAE non-flammability in which safety ratio, described later, are taken into consideration for nonflammable refrigerants R134a and R125.



FIG. 15 shows the compositions of the above mixture (a triangle surrounded by points B (B=C=G′), F, and E; and a quadrilateral surrounded by points B′, C′, F′, and E′) in a ternary composition diagram of R125, 1234yf, and R134a, when the concentration of R32 is 10.8 wt %. The triangle surrounded by points B, F, and E represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet pressure within ±2.5% of the pressure of R22. The quadrilateral surrounded by points B′, C′, F′, and E′ represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet pressure within ±1.25% of the pressure of R22.



FIGS. 16 and 17 show the compositions of the above mixture (a quadrilateral surrounded by points B, C, F, and E; and a quadrilateral surrounded by points B′, C′, F′, and E′) in a ternary composition diagram of R125, 1234yf, and R134a, when the concentration of R32 is 12.4 and 14.1 wt %. The quadrilateral surrounded by points B, C, F, and E represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet pressure within ±2.5% of the pressure of R22. The quadrilateral surrounded by points B′, C′, F′, and E′ represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet pressure within ±1.25% of the pressure of R22.



FIGS. 18 and 19 show the compositions of the above mixture (a pentagon surrounded by points B, C, F, E, and H′; and a quadrilateral surrounded by points B′, C′, F′, and E′) in a ternary composition diagram of R125, 1234yf, and R134a, when the concentration of R32 is 14.8 and 16.1 wt %. The pentagon surrounded by points B, C, F, E, and H′ represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet pressure within ±2.5% of the pressure of R22. The quadrilateral surrounded by points B′, C′, F′, and E′ represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet pressure within ±1.25% of the pressure of R22.



FIGS. 20 to 24 show the compositions of the above mixture (a quadrilateral surrounded by points B, C, F, and E; and a quadrilateral surrounded by points B′, C′, F′, and E′) in a ternary composition diagram of R125, 1234yf, and R134a, when the concentration of R32 is 16.8, 18.1, 18.7, 20.0, and 21.6 wt %. The quadrilateral surrounded by points B, C, F, and E represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet pressure within ±2.5% of the pressure of R22. The quadrilateral surrounded by points B′, C′, F′, and E′ represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet pressure within ±1.25% of the pressure of R22.



FIG. 25 shows the compositions of the above mixture (a pentagon surrounded by points B, C, D, F, and E; and a quadrilateral surrounded by points B′, C′, F′ (=D), and E′) in a ternary composition diagram of R125, 1234yf, and R134a, when the concentration of R32 is 22.6 wt %. The pentagon surrounded by points B, C, D, F, and E represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet pressure within ±2.5% of the pressure of R22. The quadrilateral surrounded by points B′, C′, F′, and E′ represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet pressure within ±1.25% of the pressure of R22.



FIG. 26 shows the compositions of the above mixture (a quadrilateral surrounded by points B, C, D, and F (F=E=I′); and a pentagon surrounded by points B′, C′, D, F′, and E′) in a ternary composition diagram of R125, 1234yf, and R134a, when the concentration of R32 is 24.2 wt %. The quadrilateral surrounded by points B, C, D, and F represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet pressure within ±2.5% of the pressure of R22. The pentagon surrounded by points B′, C′, D, F′, and E′ represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet pressure within ±1.25% of the pressure of R22.



FIG. 27 shows the compositions of the above mixture (a quadrilateral surrounded by points B, C, D, and I′; and a quadrilateral surrounded by points B′, C′ (=D), F′, and E′) in a ternary composition diagram of R125, 1234yf, and R134a, when the concentration of R32 is 24.5 wt %. The quadrilateral surrounded by points B, C, D, and I′ represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet pressure within ±2.5% of the pressure of R22. The quadrilateral surrounded by points B′, C′, F′, and E′ represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet pressure within ±1.25% of the pressure of R22.



FIG. 28 shows the compositions of the above mixture (a quadrilateral surrounded by points B, C, D, and I′; and a triangle surrounded by points B′, C′, and F′ (F′=E′=I′)) in a ternary composition diagram of R125, 1234yf, and R134a, when the concentration of R32 is 25.1 wt %. The quadrilateral surrounded by points B, C, D, and I′ represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet pressure within ±2.5% of the pressure of R22. The triangle surrounded by points B′, C′, and F′ represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet pressure within ±1.25% of the pressure of R22.



FIG. 29 shows the composition of the above mixture (represented by point J (J=K=G′)) in a ternary composition diagram of R125, 1234yf, and R134a, when the concentration of R32 is 11.6 wt %. The 1234yf side from line segment QR represents a region having a compressor outlet temperature of 115° C. or less, and the R134 side from line segment ST represents a region having a COP of 107.75% or more. Moreover, point J represents a point with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet temperature of 115° C. or less and a refrigerating capacity of 85% of that of R404A.



FIG. 30 shows the composition of the above mixture (a triangle surrounded by points G′, J, and K) in a ternary composition diagram of R125, 1234yf, and R134a, when the concentration of R32 is 14.2 wt %. The triangle surrounded by points G′, J, and K represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet temperature of 115° C. or less and a refrigerating capacity of 85% or more of that of R404A.



FIG. 31 shows the compositions of the above mixture (a triangle surrounded by points G′, J, and K; a triangle surrounded by points T, K, and U; and point L (L=M=G′)) in a ternary composition diagram of R125, 1234yf, and R134a, when the concentration of R32 is 14.5 wt %. The triangle surrounded by points G′, J, and K represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet temperature of 115° C. or less and a refrigerating capacity of 85% or more of that of R404A. The triangle surrounded by points T, K, and U represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet temperature of 115° C. or less, a COP of 107.75% or more of that of R404A, and a refrigerating capacity of 85% or more of that of R404A. Point L represents a point with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet temperature of 115° C. or less and a refrigerating capacity of 90% of that of R404A.



FIG. 32 shows the compositions of the above mixture (a triangle surrounded by points G′, J, and K; a triangle surrounded by points T, K, and U (U=J=S); and a triangle surrounded by points G′, L, and M) in a ternary composition diagram of R125, 1234yf, and R134a, when the concentration of R32 is 15.3 wt %. The triangle surrounded by points G′, J, and K represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet temperature of 115° C. or less and a refrigerating capacity of 85% or more of that of R404A. The triangle surrounded by points T, K, and U represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet temperature of 115° C. or less, a COP of 107.75% or more of that of R404A, and a refrigerating capacity of 85% or more of that of R404A. The triangle surrounded by points G′, L, and M represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet temperature of 115° C. or less and a refrigerating capacity of 90% or more of that of R404A.



FIG. 33 shows the compositions of the above mixture (a triangle surrounded by points G′, J (J=H′), and K; a quadrilateral surrounded by points S, T, K, and J (J=H′); and a triangle surrounded by points G′, L, and M) in a ternary composition diagram of R125, 1234yf, and R134a, when the concentration of R32 is 16.2 wt %. The triangle surrounded by points G′, J, and K represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet temperature of 115° C. or less and a refrigerating capacity of 85% or more of that of R404A. The quadrilateral surrounded by points S, T, K, and J represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet temperature of 115° C. or less, a COP of 107.75% or more of that of R404A, and a refrigerating capacity of 85% or more of that of R404A. The triangle surrounded by points G′, L, and M represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet temperature of 115° C. or less and a refrigerating capacity of 90% or more of that of R404A.



FIG. 34 shows the compositions of the above mixture (a quadrilateral surrounded by points G′, H′, J, and K; a pentagon surrounded by points S, T, K, J, and H′; and a triangle surrounded by points G′, L, and M (M=T)) in a ternary composition diagram of R125, 1234yf, and R134a, when the concentration of R32 is 17.0 wt %. The quadrilateral surrounded by points G′, H′, J, and K represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet temperature of 115° C. or less and a refrigerating capacity of 85% or more of that of R404A. The pentagon surrounded by points S, T, K, J, and H′ represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet temperature of 115° C. or less, a COP of 107.75% or more of that of R404A, and a refrigerating capacity of 85% or more of that of R404A. The triangle surrounded by points G′, L, and M represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet temperature of 115° C. or less and a refrigerating capacity of 90% or more of that of R404A.



FIG. 35 shows the compositions of the above mixture (a quadrilateral surrounded by points G′, H′, J, and K (K=R); a pentagon surrounded by points S, T, K (K=R), J, and H′; a triangle surrounded by points G′, L, and M; a triangle surrounded by points T, M, and V; and point O (O=P=G′)) in a ternary composition diagram of R125, 1234yf, and R134a, when the concentration of R32 is 17.5 wt %. The quadrilateral surrounded by points G′, H′, J and K represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet temperature of 115° C. or less and a refrigerating capacity of 85% or more of that of R404A. The pentagon surrounded by points S, T, K, J, and H′ represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet temperature of 115° C. or less, a COP of 107.75% or more of that of R404A, and a refrigerating capacity of 85% or more of that of R404A. The triangle surrounded by points G′, L, and M represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet temperature of 115° C. or less and a refrigerating capacity of 90% or more of that of R404A. The triangle surrounded by points T, M, and V represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet temperature of 115° C. or less, a COP of 107.75% or more of that of R404A, and a refrigerating capacity of 90% or more of that of R404A. Point O (O=P=G′) represents a point with a GWP of 1500, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a refrigerating capacity of 95% of that of R404A.



FIG. 36 shows the compositions of the above mixture (a quadrilateral surrounded by points G′, H′, J, and K; a hexagon surrounded by points S, T, R, X, J, and H′; a triangle surrounded by points G′, L (L=S), and M; a triangle surrounded by points T, M, and V (V=L=S); and a triangle surrounded by points G′, O, and P) in a ternary composition diagram of R125, 1234yf, and R134a, when the concentration of R32 is 18.0 wt %. The quadrilateral surrounded by points G′, H′, J, and K represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet temperature of 115° C. or less and a refrigerating capacity of 85% or more of that of R404A. The hexagon surrounded by points S, T, R, X, J, and H′ represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet temperature of 115° C. or less, a COP of 107.75% or more of that of R404A, and a refrigerating capacity of 85% or more of that of R404A. The triangle surrounded by points G′, L, and M represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet temperature of 115° C. or less and a refrigerating capacity of 90% or more of that of R404A. The triangle surrounded by points T, M, and V represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet temperature of 115° C. or less, a COP of 107.75% or more of that of R404A, and a refrigerating capacity of 90% or more of that of R404A. The triangle surrounded by points G′, O, and P represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a refrigerating capacity of 95% or more of that of R404A.



FIG. 37 shows the compositions of the above mixture (a pentagon surrounded by points G′, H′, J, X, and R; a hexagon surrounded by points S, T, R, X, J, and H′; a triangle surrounded by points G′, L (L=H′), and M; a quadrilateral surrounded by points S, T, M, and L (L=H′); and a triangle surrounded by points G′, O, and P) in a ternary composition diagram of R125, 1234yf, and R134a, when the concentration of R32 is 18.7 wt %. The pentagon surrounded by points G′, H′, J, X, and K represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet temperature of 115° C. or less and a refrigerating capacity of 85% or more of that of R404A. The hexagon surrounded by points S, T, R, X, J, and H′ represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet temperature of 115° C. or less, a COP of 107.75% or more of that of R404A, and a refrigerating capacity of 85% or more of that of R404A. The triangle surrounded by points G′, L, and M represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet temperature of 115° C. or less and a refrigerating capacity of 90% or more of that of R404A. The quadrilateral surrounded by points S, T, M, and L represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet temperature of 115° C. or less, a COP of 107.75% or more of that of R404A, and a refrigerating capacity of 90% or more of that of R404A. The triangle surrounded by points G′, O, and P represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a refrigerating capacity of 95% or more of that of R404A.



FIG. 38 shows the compositions of the above mixture (a quadrilateral surrounded by points G′, H′, Q (Q=J), and R; a pentagon surrounded by points S, T, R, Q (Q=J), and H′; a quadrilateral surrounded by points G′, H′, L, and M; a pentagon surrounded by points S, T, M, L, and H′; and a triangle surrounded by points G′, O, and P) in a ternary composition diagram of R125, 1234yf, and R134a, when the concentration of R32 is 19.0 wt %. The quadrilateral surrounded by points G′, H′, Q, and R represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet temperature of 115° C. or less and a refrigerating capacity of 85% or more of that of R404A. The pentagon surrounded by points S, T, R, Q, and H′ represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet temperature of 115° C. or less, a COP of 107.75% or more of that of R404A, and a refrigerating capacity of 85% or more of that of R404A. The quadrilateral surrounded by points G′, H′, L, and M represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet temperature of 115° C. or less and a refrigerating capacity of 90% or more of that of R404A. The pentagon surrounded by points S, T, M, L, and H′ represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet temperature of 115° C. or less, a COP of 107.75% or more of that of R404A, and a refrigerating capacity of 90% or more of that of R404A. The triangle surrounded by points G′, O, and P represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a refrigerating capacity of 95% or more of that of R404A.



FIG. 39 shows the compositions of the above mixture (a quadrilateral surrounded by points G′, H′, Q, and R; a pentagon surrounded by points S, T, R, Q, and H′; a quadrilateral surrounded by points G′, H′, L, and M (M=R); a pentagon surrounded by points S, T, M (M=R), L, and H′; and a triangle surrounded by points G′, O, and P) in a ternary composition diagram of R125, 1234yf, and R134a, when the concentration of R32 is 19.3 wt %. The quadrilateral surrounded by points G′, H′, Q, and R represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet temperature of 115° C. or less and a refrigerating capacity of 85% or more of that of R404A. The pentagon surrounded by points S, T, R, Q, and H′ represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet temperature of 115° C. or less, a COP of 107.75% or more of that of R404A, and a refrigerating capacity of 85% or more of that of R404A. The quadrilateral surrounded by points G′, H′, L, and M represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet temperature of 115° C. or less and a refrigerating capacity of 90% or more of that of R404A. The pentagon surrounded by points S, T, M, L, and H′ represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet temperature of 115° C. or less, a COP of 107.75% or more of that of R404A, and a refrigerating capacity of 90% or more of that of R404A. The triangle surrounded by points G′, O, and P represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a refrigerating capacity of 95% or more of that of R404A.



FIG. 40 shows the compositions of the above mixture (a quadrilateral surrounded by points G′, H′, Q, and R; a pentagon surrounded by points S, T, R, Q, and H′; a pentagon surrounded by points G′, H′, L, Y, and R; a hexagon surrounded by points S, T, R, Y, L, and H′; and a triangle surrounded by points G′, O, and P (P=T=W)) in a ternary composition diagram of R125, 1234yf, and R134a, when the concentration of R32 is 20.0 wt %. The quadrilateral surrounded by points G′, H′, Q, and R represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet temperature of 115° C. or less and a refrigerating capacity of 85% or more of that of R404A. The pentagon surrounded by points S, T, R, Q, and H′ represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet temperature of 115° C. or less, a COP of 107.75% or more of that of R404A, and a refrigerating capacity of 85% or more of that of R404A. The pentagon surrounded by points G′, H′, L, Y, and M represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet temperature of 115° C. or less and a refrigerating capacity of 90% or more of that of R404A. The hexagon surrounded by points S, T, R, Y, L, and H′ represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet temperature of 115° C. or less, a COP of 107.75% or more of that of R404A, and a refrigerating capacity of 90% or more of that of R404A. The triangle surrounded by points G′, O, and P represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a refrigerating capacity of 95% or more of that of R404A.



FIG. 41 shows the compositions of the above mixture (a quadrilateral surrounded by points G′, H′, Q, and R; a pentagon surrounded by points S, T, R, Q, and H′; a triangle surrounded by points G′, O (O=S=W), and P; and a triangle surrounded by points T, P, and W (W=S=O)) in a ternary composition diagram of R125, 1234yf, and R134a, when the concentration of R32 is 20.8 wt %. The quadrilateral surrounded by points G′, H′, Q, and R represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet temperature of 115° C. or less and a refrigerating capacity of 90% or more of that of R404A. The pentagon surrounded by points S, T, R, Q, and H′ represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet temperature of 115° C. or less, a COP of 107.75% or more of that of R404A, and a refrigerating capacity of 90% or more of that of R404A. The triangle surrounded by points G′, O, and P represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a refrigerating capacity of 95% or more of that of R404A. The triangle surrounded by points T, P, and W represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet temperature of 115° C. or less, a COP of 107.75% or more of that of R404A, and a refrigerating capacity of 95% or more of that of R404A.



FIG. 42 shows the compositions of the above mixture (a quadrilateral surrounded by points G′, H′, Q, and R; a pentagon surrounded by points S, T, R, Q, and H′; a triangle surrounded by points G′, O (O=H′), and P (P=R); and a quadrilateral surrounded by points S, T, P, and O (O=H′)) in a ternary composition diagram of R125, 1234yf, and R134a, when the concentration of R32 is 21.2 wt %. The quadrilateral surrounded by points G′, H′, Q, and R represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet temperature of 115° C. or less and a refrigerating capacity of 90% or more of that of R404A. The pentagon surrounded by points S, T, R, Q, and H′ represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet temperature of 115° C. or less, a COP of 107.75% or more of that of R404A, and a refrigerating capacity of 90% or more of that of R404A. The triangle surrounded by points G′, 0, and P represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a refrigerating capacity of 95% or more of that of R404A. The quadrilateral surrounded by points S, T, P, and O represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet temperature of 115° C. or less, a COP of 107.75% or more of that of R404A, and a refrigerating capacity of 95% or more of that of R404A.



FIG. 43 shows the compositions of the above mixture (a quadrilateral surrounded by points G′, H′, Q, and R; a pentagon surrounded by points S, T, R, Q, and H′; a quadrilateral surrounded by points G′, H′, O, and P; and a hexagon surrounded by points S, T, R, Z, O, and H′) in a ternary composition diagram of R125, 1234yf, and R134a, when the concentration of R32 is 21.6 wt %. The quadrilateral surrounded by points G′, H′, Q, and R represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet temperature of 115° C. or less and a refrigerating capacity of 90% or more of that of R404A. The pentagon surrounded by points S, T, R, Q, and H′ represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet temperature of 115° C. or less, a COP of 107.75% or more of that of R404A, and a refrigerating capacity of 90% or more of that of R404A. The quadrilateral surrounded by points G′, H′, O, and P represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a refrigerating capacity of 95% or more of that of R404A. The hexagon surrounded by points S, T, R, Z, O, and H′ represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, a compressor outlet temperature of 115° C. or less, a COP of 107.75% or more of that of R404A, and a refrigerating capacity of 95% or more of that of R404A.



FIG. 44 shows the compositions of the above mixture (a quadrilateral surrounded by points G′, H′, Q, and R; and a pentagon surrounded by points S, T, R, Q, and H′) in a ternary composition diagram of R125, 1234yf, and R134a, when the concentration of R32 is 22.6 wt %. The quadrilateral surrounded by points G′, H′, Q, and R represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet temperature of 115° C. or less and a refrigerating capacity of 95% or more of that of R404A. The pentagon surrounded by points S, T, R, Q, and H′ represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet temperature of 115° C. or less, a COP of 107.75% or more of that of R404A, and a refrigerating capacity of 95% or more of that of R404A.



FIG. 45 shows the compositions of the above mixture (a quadrilateral surrounded by points G′, H′, Q, and R; and a triangle surrounded by points S (S=H′), T (T=R), and Q) in a ternary composition diagram of R125, 1234yf, and R134a, when the concentration of R32 is 23.2 wt %. The quadrilateral surrounded by points G′, H′, Q, and R represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet temperature of 115° C. or less and a refrigerating capacity of 95% or more of that of R404A. The triangle surrounded by points S, T, and Q represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet temperature of 115° C. or less, a COP of 107.75% or more of that of R404A, and a refrigerating capacity of 95% or more of that of R404A.



FIG. 46 shows the compositions of the above mixture (a quadrilateral surrounded by points G′, H′, Q, and R; and a triangle surrounded by points S, a, and Q) in a ternary composition diagram of R125, 1234yf, and R134a, when the concentration of R32 is 24.7 wt %. The quadrilateral surrounded by points G′, H′, Q, and R represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet temperature of 115° C. or less and a refrigerating capacity of 95% or more of that of R404A. The triangle surrounded by points S, a, and Q represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet temperature of 115° C. or less, a COP of 107.75% or more of that of R404A, and a refrigerating capacity of 95% or more of that of R404A.



FIG. 47 shows the composition of the above mixture (a quadrilateral surrounded by points G′, H′, Q (Q=S), and R) in a ternary composition diagram of R125, 1234yf, and R134a, when the concentration of R32 is 25.4 wt %. The quadrilateral surrounded by points G′, H′, Q, and R represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet temperature of 115° C. or less and a refrigerating capacity of 95% or more of that of R404A.



FIG. 48 shows the composition of the above mixture (a triangle surrounded by points G′, Q (Q=H′), and R) in a ternary composition diagram of R125, 1234yf, and R134a, when the concentration of R32 is 25.6 wt %. The triangle surrounded by points G′, Q, and R represents a region with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet temperature of 115° C. or less and a refrigerating capacity of 95% or more of that of R404A.



FIG. 49 shows the composition of the above mixture (point Q (Q=R=G′)) in a ternary composition diagram of R125, 1234yf, and R134a, when the concentration of R32 is 26.6 wt %. Point Q represents a point with a GWP of 1500 or less, showing ASHRAE non-flammability in which safety ratio are taken into consideration, and having a compressor outlet temperature of 115° C. or less and a refrigerating capacity of 95% of that of R404A.





DESCRIPTION OF EMBODIMENTS

The present invention is roughly divided into a first embodiment to a fifth embodiment. Each embodiment is described in detail below. Hereinafter, “x2” in the explanation of each point and the explanation of approximate expressions represents “x2.”


First Embodiment

The first embodiment of the present invention is described in detail below.


Composition


The composition of the first embodiment of the present invention (hereinafter also referred to as “the composition of the present invention” in the section of the first embodiment) is a composition comprising a mixture of fluorinated hydrocarbons, the mixture comprising difluoromethane (R32), pentafluoroethane (R125), 2,3,3,3-tetrafluoropropene (1234yf), and 1,1,1,2-tetrafluoroethane (R134a) at specific concentrations.


The composition of the present invention has a GWP of 1500 or less and ASHRAE non-flammability performance.


Because the GWP is 1500 or less, the composition of the present invention can notably reduce the burden on the environment from a global warming perspective, compared with other general-purpose refrigerants. Moreover, since the composition of the present invention is non-flammable according to ASHRAE, it is safer than flammable refrigerants, and can be used in a wide range of applications.


The composition of the present invention preferably has refrigerating capacity equal to that of R404A. Specifically, the refrigerating capacity relative to that of R404A is preferably 85% or more, more preferably 90% or more, even more preferably 95% or more, and particularly preferably 100% or more. R404A is a refrigerant currently widely used as a refrigerant for freezing and refrigerated storage. The composition of the present invention can be an alternative refrigerant for R404A.


The compressor outlet temperature of the composition of the present invention in a refrigeration cycle is preferably 130° C. or less, more preferably 120° C. or less, and particularly preferably 115° C. or less, in terms of preventing deterioration of the refrigerant oil.


In the composition of the present invention, the ratio of refrigerating capacity to power consumed in a refrigeration cycle (coefficient of performance (COP)) is preferably high. Specifically, the COP is preferably 95 or more, more preferably 100 or more, and particularly preferably 107.75 or more.


In the composition of the present invention, the compressor outlet pressure in a refrigeration cycle is preferably equal to that of R22 (R22 retrofit). R22 was widely used as a refrigerant for freezing and refrigerated storage before the spread of R404A. Many refrigerating devices using R22 as a refrigerant still remain. However, R22 will be abolished in developed countries in 2020 due to the regulation of HCFC, and there is thus a strong demand for alternative refrigerants. It is essential for alternative refrigerants for refrigerating devices using R22 that the compressor outlet pressure, which is the maximum pressure in a refrigeration cycle, is equal to that of R22. The compressor outlet pressure is preferably within ±2.5%, and more preferably within ±1.25%, of that of R22.


In the composition of the present invention, the mixture may consist of the four basic components, i.e., difluoromethane (R32), pentafluoroethane (R125), 2,3,3,3-tetrafluoropropene (1234yf), and 1,1,1,2-tetrafluoroethane (R134a), or may comprise, in addition to the four basic components, components different from the four basic components (hereinafter referred to as “other components”). These are referred to as the “four basic components” and “other components” below. The details of the other components are described later. The composition of the present invention may consist of the above mixture, or may comprise any additives, such as refrigerant oil, described later, in addition to the mixture.


When the mixture comprises other components, the other components are preferably contained in amounts that do not inhibit the function of the four basic components. From this viewpoint, the content of other components in the mixture is preferably 0.5 wt % or less, more preferably 0.3 wt % or less, and particularly preferably 0.1 wt % or less.


Mixture of Fluorinated Hydrocarbons


The mixture of fluorinated hydrocarbons used in the present invention comprises difluoromethane (R32), pentafluoroethane (R125), 1,1,1,2-tetrafluoroethane (R134a), and 2,3,3,3-tetrafluoropropene (1234yf). The following explains Embodiment 1-1, Embodiment 1-2, Embodiment 1-3 (having Embodiment 1-3-A as a subordinate concept), Embodiment 1-4 (having Embodiments 1-4-A and 1-4-B as subordinate concepts), and Embodiment 1-5 (having Embodiments 1-5-A and 1-5-B as subordinate concepts), which are divided according to the difference in the concentrations of the four basic components.


Embodiment 1-1

In one embodiment (Embodiment 1-1) of the first embodiment, the mixture comprises at least one member selected from the group consisting of the following mixtures 1 to 6 each having a composition ratio indicated in a ternary composition diagram in which the sum of the concentrations of R125, 1234yf, and R134a is represented by (100−x) wt %, when the sum of the concentrations of R32, R125, 1234yf, and R134a is 100 wt %, and the concentration of R32 is x wt %:


mixture 1 having a composition ratio in which


(1)-1. 14.8 wt %>x≥10.8 wt %, and


(2)-1. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a pentagon having the following points as vertices:


point G (100−R32−1234yf−R134a/−0.5493x+45.325/−0.4243x+19.875),


point H (100−R32−1234yf−R134a/−0.9507x+60.575/−x+38.1),


point I (0/100−R32−1234yf−R134a/1.6974x+48.4),


point N (0/0/100−x), and


point D (0.375x+3.25/0/100−R32−R125−1234yf);


mixture 2 having a composition ratio in which


(1)-2. 18.1 wt %>x≥14.8 wt %, and


(2)-2. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a pentagon having the following points as vertices:


point G (100−R32−R125−1234yf/−0.5736x+45.669/−0.3945x+19.443),


point H (100−R32−1234yf−R134a/−0.9083x+59.936/−0.9723x+37.714),


point I (0/100−R32−1234yf−R134a/1.3625x+53.346),


point N (0/0/100−x), and


point D (0.3625x+3.4461/0/100−R32−R125−1234yf);


mixture 3 having a composition ratio in which


(1)-3. 20.0 wt %>x≥18.1 wt %, and


(2)-3. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a pentagon having the following points as vertices:


point G (100−R32−1234yf−R134a/−0.5258x+44.808/−0.4207x+19.907),


point H (100−R32−1234yf−R134a/−0.8948x+59.698/−1.0517x+39.117),


point I (0/100−R32−1234yf−R134a/1.0517x+58.983),


point N (0/0/100−x), and


point D (0.369x+3.31/0/100−R32−R125−1234yf);


mixture 4 having a composition ratio in which


(1)-4. 22.6 wt %>x≥20.0 wt %, and


(2)-4. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a quadrilateral having the following points as vertices:


point G (100−R32−1234yf−R134a/−0.5756x+45.817/−0.4244x+19.983),


point H (100−R32−1234yf−R134a/−0.9244x+60.283/−0.8488x+35.065),


point I (100−R32−1234yf−R134a/0/−2.0407x+120.8), and


point D (0.3430x+3.826/0/100−R32−R125−1234yf);


mixture 5 having a composition ratio in which


(1)-5. 24.5 wt %>x≥22.6 wt %, and


(2)-5. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a quadrilateral having the following points as vertices:


point G (100−R32−1234yf−R134a/−0.5283x+44.746/−0.4717x+21.054),


point H (100−R32−1234yf−R134a/−0.9435x+60.078/−0.8428x+34.949),


point I (100−R32−1234yf−R134a/0/−1.9435x+118.61), and


point D (0.3710x+3.2057/0/100−R32−R125−1234yf); and


mixture 6 having a composition ratio in which


(1)-6. 26.6 wt %≥x≥24.5 wt %, and


(2)-6. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a quadrilateral having the following points as vertices:


point G (100−R32−1234yf−R134a/−0.5710x+45.798/−0.4290x+20.002),


point H (100−R32−1234yf−R134a/−0.9517x+60.931/−0.7613x+32.965),


point I (100−R32−1234yf−R134a/0/−2.0000x+120.00), and


point D (0.3323x+4.1369/0/100−R32−R125−1234yf).


Such a mixture (at least one of mixtures 1 to 6) is preferable in terms of reducing GWP and ensuring ASHRAE non-flammability performance.


Embodiment 1-2

In one embodiment (Embodiment 1-2) of the first embodiment, the mixture comprises at least one member selected from the group consisting of the following mixtures 1 to 6 each having a composition ratio indicated in a ternary composition diagram in which the sum of the concentrations of R125, 1234yf, and R134a is represented by (100−x) wt %, when the sum of the concentrations of R32, R125, 1234yf, and R134a is 100 wt %, and the concentration of R32 is x wt %:


mixture 1 having a composition ratio in which


(1)-1. 14.8 wt %>x≥10.8 wt %, and


(2)-1. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a pentagon having the following points as vertices:


point G′ (100−R32−1234yf−R134a/−0.5757x+45.025/−0.4243x+20.975),


point H′ (100−R32−1234yf−R134a/−0.9770x+59.575/−x+38.4),


point I′ (0/100−R32−1234yf−R134a/1.7007x+52.125),


point N (0/0/100−x), and


point D (0.375x+3.25/0/100−R32−R125−1234yf);


mixture 2 having a composition ratio in which


(1)-2. 18.1 wt %>x≥14.8 wt %, and


(2)-2. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a pentagon having the following points as vertices:


point G′ (100−R32−1234yf−R134a/−0.5458x+44.582/−0.4264x+21.031),


point H′ (100−R32−1234yf−R134a/−0.9083x+58.536/−0.9723x+38.014),


point I′ (0/100−R32−1234yf−R134a/1.3945x+56.657),


point N (0/0/100−x), and


point D (0.3625x+3.4461/0/100−R32−R125−1234yf);


mixture 3 having a composition ratio in which


(1)-3. 20.0 wt %>x≥18.1 wt %, and


(2)-3. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a quadrilateral having the following points as vertices:


point G′ (100−R32−1234yf−R134a/−0.5277x+44.277/−0.4207x+20.907),


point H′ (100−R32−1234yf−R134a/−0.8948x+58.298/−1.0517x+39.417),


point I′ (100−R32−1234yf−R134a/0/1.9483x+117.18), and


point D (0.369x+3.31/0/100−R32−R125−1234yf);


mixture 4 having a composition ratio in which


(1)-4. 22.6 wt %>x≥20.0 wt %, and


(2)-4. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a quadrilateral having the following points as vertices:


point G′ (100−R32−1234yf−R134a/−0.5349x+44.413/−0.4651x+21.787),


point H′ (100−R32−1234yf−R134a/−0.9244x+58.883/−0.8837x+36.078),


point I′ (100−R32−1234yf−R134a/0/−2.0756x+119.72), and


point D (0.343x+3.826/0/100−R32−R125−1234yf);


mixture 5 having a composition ratio in which


(1)-5. 24.5 wt %>x≥22.6 wt %, and


(2)-5. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a quadrilateral having the following points as vertices:


point G′ (100−R32−1234yf−R134a/−0.5848x+45.537/−0.4717x+21.954),


point H′ (100−R32−1234yf−R134a/−0.9435x+59.308/−0.8428x+35.149),


point I′ (100−R32−1234yf−R134a/0/−1.9435x+116.71), and


point D (0.3710x+3.2057/0/100−R32−R125−1234yf); and


mixture 6 having a composition ratio in which


(1)-6. 26.6 wt %≥x≥24.5 wt %, and


(2)-6. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a quadrilateral having the following points as vertices:


point G′ (100−R32−1234yf−R134a/−0.5242x+44.035/−0.4290x+20.902),


point H′ (100−R32−1234yf−R134a/−x+60.7/−0.7145x+32.001),


point I′ (100−R32−1234yf−R134a/0/−2.0468x+119.26), and


point D (0.3323x+4.1369/0/100−R32−R125−1234yf).


Such a mixture (at least one of mixtures 1 to 6) is preferable in terms of reducing GWP and ensuring ASHRAE non-flammability performance (in which safety ratio are further taken into consideration).


Embodiment 1-3

In one embodiment (Embodiment 1-3) of the first embodiment, the mixture comprises at least one member selected from the group consisting of the following mixtures 1 to 7 each having a composition ratio indicated in a ternary composition diagram in which the sum of the concentrations of R125, 1234yf, and R134a is represented by (100−x) wt %, when the sum of the concentrations of R32, R125, 1234yf, and R134a is 100 wt %, and the concentration of R32 is x wt %:


mixture 1 having a composition ratio in which


(1)-1. 14.1 wt %>x≥10.8 wt %, and


(2)-1. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a quadrilateral having the following points as vertices:


point B (−2.6665x+62.786/0.7204x+31.027/100−R32−R125−1234yf),


point C (0.0914x2−4.2444x+69.184/0.1181x2−6.3648x+93.765/100−R32−R125−1234yf),


point F (0.0323x2−2.5621x+50.802/0.0346x2−3.9904x+67.56/100−R32−R125−1234yf), and


point E (0.0501x2−3.9756x+61.989/−0.0296x2+1.5133x+30.248/100−R32−R125−1234yf);


mixture 2 having a composition ratio in which


(1)-2. 16.1 wt %>x≥14.1 wt %, and


(2)-2. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a pentagon having the following points as vertices:


point B (−2.6456x+62.484/0.7929x+29.984/100−R32−R125−1234yf),


point C (0.0495x2−3.1434x+61.991/0.1723x2−8.1236x+107.78/100−R32−R125−1234yf),


point F (−1.5049x+42.339/−2.6349x+55.315/100−R32−R125−1234yf),


point E (0.2747x2−9.7967x+99.415/0.6366x2−25.375x+276.93/100−R32−R125−1234yf), and


when 14.8 wt %>x≥14.1 wt %,


point H′ (100−R32−1234yf−R134a/−0.9770x+59.575/−x+38.4), or


when 16.1 wt %>x≥14.8 wt %,


point H′ (100−R32−1234yf−R134a/−0.9083x+58.536/−0.9723x+38.014);


mixture 3 having a composition ratio in which


(1)-3. 16.8 wt %>x≥16.1 wt %, and


(2)-3. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a pentagon having the following points as vertices:


point B (−2.2857x+56.7/0.7747x+30.285/100−R32−R125−1234yf),


point C (−1.5714x+49.5/−2.8043x+66.812/100−R32−R125−1234yf),


point F (−1.2857x+38.8/−2.4954x+53.076/100−R32−R125−1234yf),


point E (−1.1429x+31.3/−5.3142x+118.96/100−R32−R125−1234yf), and


point H′ (100−R32−1234yf−R134a/−0.9083x+58.536/−0.9723x+38.014);


mixture 4 having a composition ratio in which


(1)-4. 18.1 wt %>x≥16.8 wt %, and


(2)-4. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a quadrilateral having the following points as vertices:


point B (−1.4615x+42.854/−5.931x+142.94/100−R32−1234yf−R134a),


point C (−1.3846x+46.362/−2.5156x+61.961/100−R32−R125−1234yf),


point F (−1.3846x+40.462/−2.5401x+53.827/100−R32−R125−1234yf), and


point E (−1.0769x+30.192/−4.9692x+113.16/100−R32−R125−1234yf);


mixture 5 having a composition ratio in which


(1)-5. 20.0 wt %>x≥18.1 wt %, and


(2)-5. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a quadrilateral having the following points as vertices:


point B (−1.0442x+35.27/0.2703x2−15.221x+222.52/100−R32−1234yf−R134a),


point C (−1.3145x+45.088/−2.4404x+60.615/100−R32−1234yf−R134a),


point F (−1.2138x+37.381/−0.1576x2+3.716x−7.7649/100−R32−1234yf−R134a), and


point E (−0.8869x+26.726/−4.3267x+101.52/100−R32−1234yf−R134a);


mixture 6 having a composition ratio in which


(1)-6. 21.6 wt %>x≥20.0 wt %, and


(2)-6. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a quadrilateral having the following points as vertices:


point B (−0.875x+31.9/−4.3372x+112.98/100−R32−1234yf−R134a),


point C (−1.25x+43.8/−2.375x+59.3/100−R32−1234yf−R134a),


point F (−1.125x+35.6/−2.1875x+47.25/100−R32−1234yf−R134a), and


point E (−0.75x+24/−3.8831x+92.657/100−R32−1234yf−R134a); and


mixture 7 having a composition ratio in which


(1)-7. 24.2 wt %>x≥21.6 wt %, and


(2)-7. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a quadrilateral having the following points as vertices:


point B (−0.7267x+28.67/0.1603x2−10.987x+181.821/00−R32−1234yf−R134a),


point C (0.0529x2−3.5375x+68.536/0.0431x2−4.1038x+76.546/100−R32−1234yf−R134a),


point F (−1.9651x+53.771/0/100−R32−1234yf−R134a), and


point E (−0.6163x+21.118/0.0663x2−6.4133x+116.38/100−R32−1234yf−R134a).


Such a mixture (at least one of mixtures 1 to 7) is preferable in terms of reducing GWP, ensuring ASHRAE non-flammability performance (in which safety ratio are further taken into consideration), and obtaining a compressor outlet pressure equal to that of R22 (R22 retrofit).


Embodiment 1-3-A

Moreover, in Embodiment 1-3-A, which is a subordinate concept of Embodiment 1-3, the mixture comprises at least one member selected from the group consisting of the following mixtures 1 to 7 each having a composition ratio indicated in a ternary composition diagram in which the sum of the concentrations of R125, 1234yf, and R134a is represented by (100−x) wt %, when the sum of the concentrations of R32, R125, 1234yf, and R134a is 100 wt %, and the concentration of R32 is x wt %:


mixture 1 having a composition ratio in which


(1)-1. 14.1 wt %>x≥10.8 wt %, and


(2)-1. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a quadrilateral having the following points as vertices:


point B′ (−2.6665x+62.786/0.7204x+31.027/100−R32−R125−1234yf),


point C′ (0.0902x2−4.1561x+66.56/0.117x2−6.2764x+90.341/100−R32−R125−1234yf),


point F′ (0.0702x2−3.5658x+59.024/0.0958x2−5.5978x+80.381/100−R32−R125−1234yf), and


point E′ (−2.7576x+56.987/0.784x+33.578/100−R32−R125−1234yf);


mixture 2 having a composition ratio in which


(1)-2. 14.8 wt %>x≥14.1 wt %, and


(2)-2. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a quadrilateral having the following points as vertices:


point B′ (−2.2857x+56.7/0.7747x+30.285/100−R32−R125−1234yf),


point C′ (−1.7143x+50.071/−2.8571x+65.386/100−R32−R125−1234yf),


point F′ (−1.5714x+44.857/−2.7143x+58.771/100−R32−R125−1234yf), and point E′ (−2.2857x+50.329/0.6717x+35.158/100−R32−R125−1234yf);


mixture 3 having a composition ratio in which


(1)-3. 16.1 wt %>x≥14.8 wt %, and


(2)-3. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a pentagon having the following points as vertices:


point B′ (−1.4615x+42.854/−5.931x+142.94/100−R32−R125−1234yf),


point C′ (−1.5385x+47.469/−2.7834x+64.295/100−R32−R125−1234yf),


point F′ (−1.5385x+44.369/−2.7889x+59.876/100−R32−R125−1234yf),


point E′ (−1.6154x+40.408/−6.3915x+139.69/100−R32−R125−1234yf), and


point H′ (100−R32−1234yf−R134a/−0.9083x+58.536/−0.9723x+38.014);


mixture 4 having a composition ratio in which


(1)-4. 18.1 wt %>x≥16.1 wt %, and


(2)-4. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a quadrilateral having the following points as vertices:


point B′ (−2.6456x+62.484/0.7929x+29.984/100−R32−R125−1234yf),


point C′ (−1.4515x+46.075/−2.5842x+61.058/100−R32−R125−1234yf),


point F′ (−1.3447x+41.226/0.0959x2−5.7176x+82.165/100−R32−R125−1234yf), and


point E′ (0.1044x2−4.7203x+63.337/0.3836x2−18.386x+233.37/100−R32−R125−1234yf);


mixture 5 having a composition ratio in which


(1)-5. 20.0 wt %>x≥18.1 wt %, and


(2)-5. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a quadrilateral having the following points as vertices:


point B′ (−1.0442x+33.87/0.2539x2−14.531x+212.38/100−R32−1234yf−R134a),


point C′ (−1.3145x+43.588/−2.4717x+59.031/100−R32−1234yf−R134a),


point F′ (−1.258x+39.651/0.0607x2−4.7348x+75.905/100−R32−1234yf−R134a), and


point E′ (−0.8869x+28.126/0.1994x2−11.991x+177.97/100−R32−1234yf−R134a);


mixture 6 having a composition ratio in which


(1)-6. 22.6 wt %>x≥20.0 wt %, and


(2)-6. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a quadrilateral having the following points as vertices:


point B′ (−0.7733x+28.448/0.0598x2−6.503x+129.46/100−R32−1234yf−R134a),


point C′ (−1.157x+40.426/−2.1919x+53.439/100−R32−1234yf−R134a),


point F′ (−1.1163x+36.822/0.0721x2−5.1875x+80.404/100−R32−1234yf−R134a), and


point E′ (−0.7733x+25.848/0.1578x2−10.613x+167.02/100−R32−1234yf−R134a); and


mixture 7 having a composition ratio in which


(1)-7. 25.1 wt %≥x≥22.6 wt %, and


(2)-7. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a quadrilateral having the following points as vertices:


point B′ (−0.6809x+26.385/0.1536x2−10.827x+179.27/100−R32−1234yf−R134a),


point C′ (−0.2417x2+10.247x−93.86/0.5728x2−28.884x+364.1/100−R32−1234yf−R134a),


point F′ (0.1528x2−9.0875x+138.94/0/100−R32−1234yf−R134a), and


point E′ (0.1167x2−6.085x+86.332/0.2787x2−16.413x+236.4/100−R32−1234yf−R134a).


Such a mixture (at least one of mixtures 1 to 7) is preferable in terms of reducing GWP, ensuring ASHRAE non-flammability performance (in which safety ratio are further taken into consideration), and obtaining a compressor outlet pressure equal to that of R22 (R22 retrofit).


Embodiment 1-4

In one embodiment (Embodiment 1-4) of the first embodiment, the mixture comprises at least one member selected from the group consisting of the following mixtures 1 to 9 each having a composition ratio indicated in a ternary composition diagram in which the sum of the concentrations of R125, 1234yf, and R134a is represented by (100−x) wt %, when the sum of the concentrations of R32, R125, 1234yf, and R134a is 100 wt %, and the concentration of R32 is x wt %:


mixture 1 having a composition ratio in which


(1)-1. 14.2 wt %>x≥11.6 wt %, and


(2)-1. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a triangle having the following points as vertices:


point G′ (100−R32−1234yf−R134a/−0.5757x+45.025/−0.4243x+20.975),


point J (−3.5769x+75.492/1.2204x+24.143/100−R32−R125−1234yf), and


point K (−2.3846x+61.662/−4.0172x+84.9/100−R32−R125−1234yf);


mixture 2 having a composition ratio in which


(1)-2. 15.3 wt %>x≥14.2 wt %, and


(2)-2. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a triangle having the following points as vertices:


when 14.8 wt %>x≥14.2 wt %,


point G′ (100−R32−1234yf−R134a/−0.5757x+45.025/−0.4243x+20.975) or


when 15.3 wt %>x≥14.8 wt %,


point G′ (100−R32−1234yf−R134a/−0.5458x+44.582/−0.4264x+21.031), and


point J (−3.4381x+73.493/1.1236x+25.522/100−R32−R125−1234yf), and


point K (0.9091x2−29.091x+257.58/0.8579x2−29.085x+267.88/100−R32−R125−1234yf);


mixture 3 having a composition ratio in which


(1)-3. 16.2 wt %>x≥15.3 wt %, and


(2)-3. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a triangle having the following points as vertices:


point G′ (100−R32−1234yf−R134a/−0.5458x+44.582/−0.4264x+21.031),


point J (−3.5556x+75.3/1.2095x+24.209/100−R32−R125−1234yf), and


point K (−2x+55.9/−3.4439x+76.392/100−R32−R125−1234yf);


mixture 4 having a composition ratio in which


(1)-4. 17.5 wt %>x≥16.2 wt %, and


(2)-4. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a quadrilateral having the following points as vertices:


point G′ (100−R32−1234yf−R134a/−0.5458x+44.582/−0.4264x+21.031),


point H′ (100−R32−1234yf−R134a/−0.9083x+58.536/−0.9723x+38.014),


point J (−1.6163x+43.882/−6.3674x+146.95/100−R32−R125−1234yf), and


point K (−1.8488x+53.445/−3.1206x+71.153/100−R32−R125−1234yf);


mixture 5 having a composition ratio in which


(1)-5. 19.0 wt %>x≥17.5 wt %, and


(2)-5. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a pentagon having the following points as vertices:


when 18.1 wt %>x≥17.5 wt %,


point G′ (100−R32−1234yf−R134a/−0.5458x+44.582/−0.4264x+21.031), and


point H′ (100−R32−1234yf−R134a/−0.9083x+58.536/−0.9723x+38.014), or


when 19.0 wt %>x≥18.1 wt %,


point G′ (100−R32−1234yf−R134a/−0.5277x+44.277/−0.4207x+20.907), and


point H′ (100−R32−1234yf−R134a/−0.8948x+58.298/−1.0517x+39.417), and


point J (0.1273x2−6.1109x+83.553/0.1532x2−11.484x+189.57/100−R32−R125−1234yf),


point X (−0.1696x2+1.0575x+54.537/−0.2271x2+15.05x−177.28/100−R32−R125−1234yf), and


point R (−0.0401x2+3.0217x−19.198/−0.0297x2+2.7774x−22.544/100−R32−R125−1234yf);


mixture 6 having a composition ratio in which


(1)-6. 20.8 wt %>x≥19.0 wt %, and


(2)-6. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a quadrilateral having the following points as vertices:


when 20.0 wt %>x≥19.0 wt %,


point G′ (100−R32−1234yf−R134a/−0.5277x+44.277/−0.4207x+20.907), and


point H′ (100−R32−1234yf−R134a/−0.8948x+58.298/−1.0517x+39.417), or


when 20.8 wt %>x≥20.0 wt %,


point G′ (100−R32−1234yf−R134a/−0.5349x+44.413/−0.4651x+21.787), and


point H′ (100−R32−1234yf−R134a/−0.9244x+58.883/−0.8837x+36.078), and


point Q (−0.0198x2+27.157x−31.225/−0.0377x2+3.0486x−17.594/100−R32−R125−1234yf), and


point R (−0.0401x2+3.0217x−19.198/−0.0297x2+2.7774x−22.544/100−R32−R125−1234yf);


mixture 7 having a composition ratio in which


(1)-7. 23.2 wt %>x≥20.8 wt %, and


(2)-7. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a quadrilateral having the following points as vertices:


when 22.6 wt %>x≥20.8 wt %,


point G′ (100−R32−1234yf−R134a/−0.5349x+44.413/−0.4651x+21.787), and


point H′ (100−R32−1234yf−R134a/−0.9244x+58.883/−0.8837x+36.078), or


when 23.2 wt %>x≥22.6 wt %,


point G′ (100−R32−1234yf−R134a/−0.5848x+45.537/−0.4717x+21.954), and


point H′ (100−R32−1234yf−R134a/−0.9435x+59.308/−0.8428x+35.149), and


point Q (−0.0984x2+6.1633x−68.728/−0.0617x2+3.9141x−25.243/100−R32−R125−1234yf), and


point R (−0.0031x2+1.5234x−4.0783/−0.0503x2+3.6856x−32.627/100−R32−R125−1234yf);


mixture 8 having a composition ratio in which


(1)-8. 25.6 wt %>x≥23.2 wt %, and


(2)-8. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a quadrilateral having the following points as vertices:


when 24.5 wt %>x≥23.2 wt %,


point G′ (100−R32−1234yf−R134a/−0.5848x+45.537/−0.4717x+21.954), and


point H′ (100−R32−1234yf−R134a/−0.9435x+59.308/−0.8428x+35.149), or


when 25.6 wt %>x≥24.5 wt %,


point G′ (100−R32−1234yf−R134a/−0.5242x+44.035/−0.4290x+20.902), and


point H′ (100−R32−1234yf−R134a/−x+60.7/−0.7145x+32.001), and


point Q (−0.0115x2+2.3422x−26.868/−0.1077x2+6.4104x−58.357/100−R32−R125−1234yf), and


point R (−0.1398x2+8.0281x−81.391/−0.0932x2+5.7935x−58.514/100−R32−R125−1234yf); and


mixture 9 having a composition ratio in which


(1)-9. 26.6 wt %≥x≥25.6 wt %, and


(2)-9. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a triangle having the following points as vertices:


point G′ (100−R32−1234yf−R134a/−0.5242x+44.035/−0.4290x+20.902),


point Q (8.2x−184.32/−5x+163.1/100−R32−R125−1234yf), and


point R (1.2x+1.88/1.246x−3.0431/100−R32−R125−1234yf).


Such a mixture (at least one of mixtures 1 to 9) is preferable in terms of reducing GWP, ensuring ASHRAE non-flammability performance (in which safety ratio are further taken into consideration), exhibiting refrigerating capacity equal to that of R404A, and reducing the compressor outlet temperature in a refrigeration cycle.


Embodiment 1-4-A

Moreover, in Embodiment 1-4-A, which is a subordinate concept of Embodiment 1-4, the mixture comprises at least one member selected from the group consisting of the following mixtures 1 to 8:


mixture 1 having a composition ratio in which


(1)-1. 17.0 wt %>x≥14.5 wt %, and


(2)-1. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a triangle having the following points as vertices:


when 14.8 wt %>x≥14.5 wt %,


point G′ (100−R32−1234yf−R134a/−0.5757x+45.025/−0.4243x+20.975), or


when 17.0 wt %>x≥14.8 wt %,


point G′ (100−R32−1234yf−R134a/−0.5458x+44.582/−0.4264x+21.031), and


point L (−3.3215x+82.089/1.1147x+20.535/100−R32−R125−1234yf), and


point M (−2.238x+66.348/−3.8006x+91.779/100−R32−R125−1234yf);


mixture 2 having a composition ratio in which


(1)-2. 18.0 wt %>x≥17.0 wt %, and


(2)-2. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a triangle having the following points as vertices:


point G′ (100−R32−1234yf−R134a/−0.5458x+44.582/−0.4264x+21.031),


point L (−3.4x+83.4/1.3x+17.378/100−R32−R125−1234yf), and


point M (−1.7x+57.217/−0.6939x2+21.203x−132.72/100−R32−R125−1234yf);


mixture 3 having a composition ratio in which


(1)-3. 18.7 wt %>x≥18.0 wt %, and


(2)-3. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a triangle having the following points as vertices:


when 18.1 wt %>x≥18.0 wt %,


point G′ (100−R32−1234yf−R134a/−0.5458x+44.582/−0.4264x+21.031), or


when 18.7 wt %>x≥18.1 wt %,


point G′ (100−R32−1234yf−R134a/−0.5277x+44.277/−0.4207x+20.907), and


point L (−3.1429x+78.771/1.1429x+20.229/100−R32−R125−1234yf), and


point M (−1.8571x+60.029/−3.1386x+80.613/100−R32−R125−1234yf);


mixture 4 having a composition ratio in which


(1)-4. 19.3 wt %>x≥18.7 wt %, and


(2)-4. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a quadrilateral having the following points as vertices:


point G′ (100−R32−1234yf−R134a/−0.5277x+44.277/−0.4207x+20.907),


point H′ (100−R32−1234yf−R134a/−0.8948x+58.298/−1.0517x+39.417),


point L (−1.6667x+51.167/−6.2835x+159.1/100−R32−R125−1234yf), and


point M (−1.8333x+59.567/−3.1952x+81.665/100−R32−R125−1234yf);


mixture 5 having a composition ratio in which


(1)-5. 20.8 wt %>x≥19.3 wt %, and


(2)-5. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a pentagon having the following points as vertices:


when 20.0 wt %>x≥19.3 wt %,


point G′ (100−R32−1234yf−R134a/−0.5277x+44.277/−0.4207x+20.907), and


point H′ (100−R32−1234yf−R134a/−0.8948x+58.298/−1.0517x+39.417), or


when 20.8 wt %>x≥20.0 wt %,


point G′ (100−R32−1234yf−R134a/−0.5349x+44.413/−0.4651x+21.787), and


point H′ (100−R32−1234yf−R134a/−0.9244x+58.883/−0.8837x+36.078), and


point L (−1.3994x+46.001/−5.5605x+145.15/100−R32−R125−1234yf),


point Y (−0.4421x2+12.862x−59.353/0.4405x2−11.34x+74.783/100−R32−R125−1234yf), and


point R (−0.0401x2+3.0217x−19.198/−0.0297x2+2.7774x−22.544/100−R32−R125−1234yf);


mixture 6 having a composition ratio in which


(1)-6. 23.2 wt %>x≥20.8 wt %, and


(2)-6. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a quadrilateral having the following points as vertices:


when 22.6 wt %>x≥20.8 wt %,


point G′ (100−R32−1234yf−R134a/−0.5349x+44.413/−0.4651x+21.787), and


point H′ (100−R32−1234yf−R134a/−0.9244x+58.883/−0.8837x+36.078), or


when 23.2 wt %>x≥22.6 wt %,


point G′ (100−R32−1234yf−R134a/−0.5848x+45.537/−0.4717x+21.954), and


point H′ (100−R32−1234yf−R134a/−0.9435x+59.308/−0.8428x+35.149), and


point Q (−0.0984x2+6.1633x−68.728/−0.0617x2+3.9141x−25.243/100−R32−R125−1234yf), and


point R (−0.0031x2+1.5234x−4.0783/−0.0503x2+3.6856x−32.627/100−R32−R125−1234yf);


mixture 7 having a composition ratio in which


(1)-7. 25.6 wt %>x≥23.2 wt %, and


(2)-7. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a quadrilateral having the following points as vertices:


when 24.5 wt %>x≥23.2 wt %,


point G′ (100−R32−1234yf−R134a/−0.5848x+45.537/−0.4717x+21.954), and


point H′ (100−R32−1234yf−R134a/−0.9435x+59.308/−0.8428x+35.149), or


when 25.6 wt %>x≥24.5 wt %,


point G′ (100−R32−1234yf−R134a/−0.5242x+44.035/−0.4290x+20.902), and


point H′ (100−R32−1234yf−R134a/−x+60.7/−0.7145x+32.001), and


point Q (−0.0115x2+2.3422x−26.868/−0.1077x2+6.4104x−58.357/100−R32−R125−1234yf), and


point R (−0.1398x2+8.0281x−81.391/−0.0932x2+5.7935x−58.514/100−R32−R125−1234yf); and


mixture 8 having a composition ratio in which


(1)-8. 26.6 wt %≥x≥25.6 wt %, and


(2)-8. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a triangle having the following points as vertices:


point G′ (100−32-1234yf−R134a/−0.5242x+44.035/−0.4290x+20.902),


point Q (8.2x−184.32/−5x+163.1/100−R32−R125−1234yf), and


point R (1.2x+1.88/1.246x−3.0431/100−R32−R125−1234yf).


Such a mixture (at least one of mixtures 1 to 8) is preferable in terms of reducing GWP, ensuring ASHRAE non-flammability performance (in which safety ratio are further taken into consideration), exhibiting refrigerating capacity equal to that of R404A (refrigerating capacity higher than that of Embodiment 1-4), and reducing the compressor outlet temperature in a refrigeration cycle.


Embodiment 1-4-B

Moreover, in Embodiment 1-4-B, which is a subordinate concept of Embodiment 1-4, the mixture comprises at least one member selected from the group consisting of the following mixtures 1 to 7:


mixture 1 having a composition ratio in which


(1)-1. 20.0 wt %>x≥17.5 wt %, and


(2)-1. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a triangle having the following points as vertices:


when 18.1 wt %>x≥17.5 wt %,


point G′ (100−R32−1234yf−R134a/−0.5458x+44.582/−0.4264x+21.031), or


when 20.0 wt %>x≥18.1 wt %,


point G′ (100−R32−1234yf−R134a/−0.5277x+44.277/−0.4207x+20.907), and


point O (−3.1554x+89.013/1.1108x+15.673/100−R32−R125−1234yf), and


point P (0.0698x2−4.6141x+93.254/0.1361x2−8.5106x+142.27/100−R32−R125−1234yf);


mixture 2 having a composition ratio in which


(1)-2. 20.8 wt %>x≥20.0 wt %, and


(2)-2. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a triangle having the following points as vertices:


point G′ (100−R32−1234yf−R134a/−0.5349x+44.413/−0.4651x+21.787),


point O (−3.5x+95.9/1.5661x+6.5807/100−R32−R125−1234yf), and


point P (−1.75x+63.9/−2.9691x+85.881/100−R32−R125−1234yf);


mixture 3 having a composition ratio in which


(1)-3. 21.2 wt %>x≥20.8 wt %, and


(2)-3. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a triangle having the following points as vertices:


point G′ (100−R32−1234yf−R134a/−0.5349x+44.413/−0.4651x+21.787),


point O (−2.25x+69.9/0.3629x+31.605/100−R32−R125−1234yf), and


point P (−1.75x+63.9/−3.0619x+87.812/100−R32−R125−1234yf);


mixture 4 having a composition ratio in which


(1)-4. 22.6 wt %>x≥21.2 wt %, and


(2)-4. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a pentagon having the following points as vertices:


point G′ (100−R32−1234yf−R134a/−0.5349x+44.413/−0.4651x+21.787),


point H′ (100−R32−1234yf−R134a/−0.9244x+58.883/−0.8837x+36.078),


point O (0.3214x2−15.507x+206.49/1.2477x2−60.003x+750.62/100−R32−R125−1234yf),


point Z (−0.0118x2−4.1976x+121.09/−0.0544x2+8.7425x−137.98/100−R32−R125−1234yf), and


point R (−0.0031x2+1.5234x−4.0783/−0.0503x2+3.6856x−32.627/100−R32−R125−1234yf);


mixture 5 having a composition ratio in which


(1)-5. 23.2 wt %>x≥22.6 wt %, and


(2)-5. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a quadrilateral having the following points as vertices:


point G′ (100−R32−1234yf−R134a/−0.5848x+45.537/−0.4717x+21.954),


point H′ (100−R32−1234yf−R134a/−0.9435x+59.308/−0.8428x+35.149),


point Q (−0.0984x2+6.1633x−68.728/−0.0617x2+3.9141x−25.243/100−R32−R125−1234yf), and


point R (−0.0031x2+1.5234x−4.0783/−0.0503x2+3.6856x−32.627/100−R32−R125−1234yf);


mixture 6 having a composition ratio in which


(1)-6. 25.6 wt %>x≥23.2 wt %, and


(2)-6. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a quadrilateral having the following points as vertices:


when 24.5 wt %>x≥23.2 wt %,


point G′ (100−R32−1234yf−R134a/−0.5848x+45.537/−0.4717x+21.954), and


point H′ (100−R32−1234yf−R134a/−0.9435x+59.308/−0.8428x+35.149), or


when 25.6 wt %>x≥24.5 wt %,


point G′ (100−R32−1234yf−R134a/−0.5242x+44.035/−0.4290x+20.902), and


point H′ (100−R32−1234yf−R134a/−x+60.7/−0.7145x+32.001), and


point Q (−0.0115x2+2.3422x−26.868/−0.1077x2+6.4104x−58.357/100−R32−R125−1234yf), and


point R (−0.1398x2+8.0281x−81.391/−0.0932x2+5.7935x−58.514/100−R32−R125−1234yf); and


mixture 7 having a composition ratio in which


(1)-7. 26.6 wt %≥x≥25.6 wt %, and


(2)-7. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a triangle having the following points as vertices:


point G′ (100−R32−1234yf−R134a/−0.5242x+44.035/−0.4290x+20.902),


point Q (8.2x−184.32/−5x+163.1/100−R32−R125−1234yf), and


point R (1.2x+1.88/1.246x−3.0431/100−R32−R125−1234yf).


Such a mixture (at least one of mixtures 1 to 7) is preferable in terms of reducing GWP, ensuring ASHRAE non-flammability performance (in which safety ratio are further taken into consideration), exhibiting refrigerating capacity equal to that of R404A (refrigerating capacity higher than that of Embodiment 1-4-A), and reducing the compressor outlet temperature in a refrigeration cycle.


Embodiment 1-5

In one embodiment (Embodiment 1-5) of the first embodiment, the mixture comprises at least one member selected from the group consisting of the following mixtures 1 to 7 each having a composition ratio indicated in a ternary composition diagram in which the sum of the concentrations of R125, 1234yf, and R134a is (100−x) wt %, when the sum of the concentrations of R32, R125, 1234yf, and R134a is 100 wt %, and the concentration of R32 is x wt %:


mixture 1 having a composition ratio in which


(1)-1. 15.3 wt %>x≥14.2 wt %, and


(2)-1. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a triangle having the following points as vertices:


point T (100−R32−1234yf−R134a/0.0415x2+1.0547x+21.254/0.0863x2−3.628x+64.252),


point K (0.9091x2−29.091x+257.58/0.8579x2−29.085x+267.88/100−R32−R125−1234yf), and


point U (1.3896x2−47.266x+418.78/−2.8422x2+97.299x−780.65/100−R32−R125−1234yf);


mixture 2 having a composition ratio in which


(1)-2. 16.2 wt %>x≥15.3 wt %, and


(2)-2. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a quadrilateral having the following points as vertices:


point S (100−R32−1234yf−R134a/0.0508x2−2.3591x+66.946/−0.0008x2−0.6861x+31.798),


point T (100−R32−1234yf−R134a/−0.0415x2+1.0547x+21.254/0.0863x2−3.628x+64.252),


point K (−2x+55.9/−3.4439x+76.392/100−R32−R125−1234yf), and


point J (−3.5556x+75.3/1.2095x+24.209/100−R32−R125−1234yf);


mixture 3 having a composition ratio in which


(1)-3. 17.5 wt %>x≥16.2 wt %, and


(2)-3. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a pentagon having the following points as vertices:


when 17.0 wt %>x≥16.2 wt %,


point S (100−R32−1234yf−R134a/0.0508x2−2.3591x+66.946/−0.0008x2−0.6861x+31.798), and


point T (100−R32−1234yf−R134a/−0.0415x2+1.0547x+21.254/0.0863x2−3.628x+64.252), or


when 17.5 wt %>x≥17.0 wt %,


point S (100−R32−1234yf−R134a/0.1108x2−4.5904x+87.503/0.0939x2−4.1798x+63.826), and


point T (100−R32−1234yf−R134a/−0.0766x2+2.5779x+5.5242/0.2286x2−9.3441x+120.28), and


point K (−1.8488x+53.445/−3.1206x+71.153/100−R32−R125−1234yf),


point J (−1.6163x+43.882/−6.3674x+146.95/100−R32−R125−1234yf), and


point H′ (100−R32−1234yf−R134a/−0.9083x+58.536/−0.9723x+38.014);


mixture 4 having a composition ratio in which


(1)-4. 19.0 wt %>x≥17.5 wt %, and


(2)-4. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a hexagon having the following points as vertices:


point S (100−R32−1234yf−R134a/0.1108x2−4.5904x+87.503/0.0939x2−4.1798x+63.826),


point T (100−R32−1234yf−R134a/−0.0766x2+2.5779x+5.5242/0.2286x2−9.3441x+120.28),


point R (−0.0401x2+3.0217x−19.198/−0.0297x2+2.7774x−22.544/100−R32−R125−1234yf),


point X (−0.1696x2+1.0575x+54.537/−0.2271x2+15.05x−177.28/100−R32−R125−1234yf),


point J (0.1273x2−6.1109x+83.553/0.1532x2−11.484x+189.57/100−R32−R125−1234yf), and


when 18.1 wt %>x≥17.5 wt %,


point H′ (100−R32−1234yf−R134a/−0.9083x+58.536/−0.9723x+38.014), or


when 19.0 wt %>x≥18.1 wt %,


point H′ (100−R32−1234yf−R134a/−0.8948x+58.298/−1.0517x+39.417);


mixture 5 having a composition ratio in which


(1)-5. 20.8 wt %>x≥19.0 wt %, and


(2)-5. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a pentagon having the following points as vertices:


point S (100−R32−1234yf−R134a/0.1263x2−5.6749x+102.56/−0.029x2+0.4298x+20.594),


point T (100−R32−1234yf−R134a/0.1451x2−6.0744x+89.981/−0.2364x2+8.5372x−51.582),


point R (−0.0401x2+3.0217x−19.198/−0.0297x2+2.7774x−22.544/100−R32−R125−1234yf),


point Q (−0.0198x2+27.157x−31.225/−0.0377x2+3.0486x−17.594/100−R32−R125−1234yf), and


when 20.0 wt %>x≥19.0 wt %,


point H′ (100−R32−1234yf−R134a/−0.8948x+58.298/−1.0517x+39.417), or


when 20.8 wt %>x≥20.0 wt %,


point H′ (100−R32−1234yf−R134a/−0.9244x+58.883/−0.8837x+36.078);


mixture 6 having a composition ratio in which


(1)-6. 23.2 wt %>x≥20.8 wt %, and


(2)-6. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a pentagon having the following points as vertices:


point S (100−R32−1234yf−R134a/0.1017x2−5.1872x+102.99/0.0034x2−0.7313x+30.692),


point T (100−R32−1234yf−R134a/−0.0318x2+1.1657x+15.869/−0.123x2+4.4541x−15.735),


point R (−0.0031x2+1.5234x−4.0783/−0.0503x2+3.6856x−32.627/100−R32−R125−1234yf),


point Q (−0.0984x2+6.1633x−68.728/−0.0617x2+3.9141x−25.243/100−R32−R125−1234yf), and


when 22.6 wt %>x≥20.8 wt %,


point H′ (100−R32−1234yf−R134a/−0.9244x+58.883/−0.8837x+36.078), or


when 23.2 wt %>x≥22.6 wt %,


point H′ (100−R32−1234yf−R134a/−0.9435x+59.308/−0.8428x+35.149); and


mixture 7 having a composition ratio in which


(1)-7. 25.4 wt %≥x≥23.2 wt %, and


(2)-7. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a triangle having the following points as vertices:


point S (100−R32−1234yf−R134a/−0.0317x2+0.4511x+43.979/0.075x2−4.1913x+72.494),


point α (0.0324x2−3.5746x+95.092/0.0193x2+3.2487x−59.944/100−R32−R125−1234yf), and


point Q (−0.0115x2+2.3422x−26.868/−0.1077x2+6.4104x−58.357/100−R32−R125−1234yf).


Such a mixture (at least one of mixtures 1 to 7) is preferable in terms of reducing GWP, ensuring ASHRAE non-flammability performance (in which safety ratio are further taken into consideration), exhibiting refrigerating capacity equal to that of R404A, reducing the compressor outlet temperature in a refrigeration cycle, and improving the coefficient of performance (COP).


Embodiment 1-5-A

Moreover, in Embodiment 1-5-A, which is a subordinate concept of Embodiment 1-5, the mixture comprises at least one member selected from the group consisting of the following mixtures 1 to 6:


mixture 1 having a composition ratio in which


(1)-1. 18.0 wt %>x≥17.0 wt %, and


(2)-1. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a triangle having the following points as vertices:


point T (100−R32−1234yf−R134a/−0.0766x2+2.5779x+5.5242/0.2286x2−9.3441x+120.28),


point M (−1.7x+57.217/−0.6939x2+21.203x−132.72/100−R32−R125−1234yf), and


point V (−1.3362x2+40.667x−276.87/2.2412x2−64.842x+481.81/100−R32−R125−1234yf);


mixture 2 having a composition ratio in which


(1)-2. 18.7 wt %>x≥18.0 wt %, and


(2)-2. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a quadrilateral having the following points as vertices:


point S (100−R32−1234yf−R134a/0.1108x2−4.5904x+87.503/0.0939x2−4.1798x+63.826),


point T (100−R32−1234yf−R134a/−0.0766x2+2.5779x+5.5242/0.2286x2−9.3441x+120.28),


point M (−1.8571x+60.029/−3.1386x+80.613/100−R32−R125−1234yf), and


point L (−3.1429x+78.771/1.1429x+20.229/100−R32−R125−1234yf);


mixture 3 having a composition ratio in which


(1)-3. 19.3 wt %>x≥18.7 wt %, and


(2)-3. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a pentagon having the following points as vertices:


when 19.0 wt %>x≥18.7 wt %,


point S (100−R32−1234yf−R134a/0.1108x2−4.5904x+87.503/0.0939x2−4.1798x+63.826), and


point T (100−R32−1234yf−R134a/−0.0766x2+2.5779x+5.5242/0.2286x2−9.3441x+120.28), or


when 19.3 wt %>x≥19.0 wt %,


point S (100−R32−1234yf−R134a/0.1263x2−5.6749x+102.56/−0.029x2+0.4298x+20.594), and


point T (100−R32−1234yf−R134a/0.1451x2−6.0744x+89.981/−0.2364x2+8.5372x−51.582), and


point M (−1.8333x+59.567/−3.1952x+81.665/100−R32−R125−1234yf),


point L (−1.6667x+51.167/−6.2835x+159.1/100−R32−R125−1234yf), and


point H′ (100−R32−1234yf−R134a/−0.8948x+58.298/−1.0517x+39.417);


mixture 4 having a composition ratio in which


(1)-4. 20.8 wt %>x≥19.3 wt %, and


(2)-4. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a hexagon having the following points as vertices:


point S (100−R32−1234yf−R134a/0.1017x2−5.1872x+102.99/0.0034x2−0.7313x+30.692),


point T (100−R32−1234yf−R134a/0.1451x2−6.0744x+89.981/−0.2364x2+8.5372x−51.582),


point R (−0.0401x2+3.0217x−19.198/−0.0297x2+2.7774x−22.544/100−R32−R125−1234yf),


point Y (−0.4421x2+12.862x−59.353/0.4405x2−11.34x+74.783/100−R32−R125−1234yf),


point L (−1.3994x+46.001/−5.5605x+145.15/100−R32−R125−1234yf), and


when 20.0 wt %>x≥19.3 wt %,


point H′ (100−R32−1234yf−R134a/−0.8948x+58.298/−1.0517x+39.417), or


when 20.8 wt %>x≥20.0 wt %,


point H′ (100−R32−1234yf−R134a/−0.9244x+58.883/−0.8837x+36.078);


mixture 5 having a composition ratio in which


(1)-5. 23.2 wt %>x≥20.8 wt %, and


(2)-5. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a pentagon having the following points as vertices:


point S (100−R32−1234yf−R134a/0.1017x2−5.1872x+102.99/0.0034x2−0.7313x+30.692),


point T (100−R32−1234yf−R134a/−0.0318x2+1.1657x+15.869/−0.123x2+4.4541x−15.735),


point R (−0.0031x2+1.5234x−4.0783/−0.0503x2+3.6856x−32.627/100−R32−R125−1234yf),


point Q (−0.0984x2+6.1633x−68.728/−0.0617x2+3.9141x−25.243/100−R32−R125−1234yf), and


when 22.6 wt %>x≥20.8 wt %,


point H′ (100−R32−1234yf−R134a/−0.9244x+58.883/−0.8837x+36.078), or


when 23.2 wt %>x≥22.6 wt %,


point H′ (100−R32−1234yf−R134a/−0.9435x+59.308/−0.8428x+35.149); and


mixture 6 having a composition ratio in which


(1)-6. 25.4 wt %≥x≥23.2 wt %, and


(2)-6. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a triangle having the following points as vertices:


point S (100−R32−1234yf−R134a/−0.0317x2+0.4511x+43.979/0.075x2−4.1913x+72.494),


point α (0.0324x2−3.5746x+95.092/0.0193x2+3.2487x−59.944/100−R32−R125−1234yf), and


point Q (−0.0115x2+2.3422x−26.868/−0.1077x2+6.4104x−58.357/100−R32−R125−1234yf).


Such a mixture (at least one of mixtures 1 to 6) is preferable in terms of reducing GWP, ensuring ASHRAE non-flammability performance (in which safety ratio are further taken into consideration), exhibiting refrigerating capacity equal to that of R404A (refrigerating capacity higher than that of Embodiment 1-5), reducing the compressor outlet temperature in a refrigeration cycle, and improving the coefficient of performance (COP).


Embodiment 1-5-B

Moreover, in Embodiment 1-5-B, which is a subordinate concept of Embodiment 1-5, the mixture comprises at least one member selected from the group consisting of the following mixtures 1 to 5:


mixture 1 having a composition ratio in which


(1)-1. 20.8 wt %>x≥20 wt %, and


(2)-1. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a triangle having the following points as vertices:


point T (100−R32−1234yf−R134a/0.1451x2−6.0744x+89.981/−0.2364x2+8.5372x−51.582),


point P (−1.75x+63.9/−2.9691x+85.881/100−R32−R125−1234yf), and


point W (−1.4439x2+51.537x−424.27/2.1733x2−72.785x+612.88/100−R32−R125−1234yf);


mixture 2 having a composition ratio in which


(1)-2. 21.2 wt %>x≥20.8 wt %, and


(2)-2. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a quadrilateral having the following points as vertices:


point S (100−R32−1234yf−R134a/0.1017x2−5.1872x+102.99/0.0034x2−0.7313x+30.692),


point T (100−R32−1234yf−R134a/−0.0318x2+1.1657x+15.869/−0.123x2+4.4541x−15.735),


point P (−1.75x+63.9/−3.0619x+87.812/100−R32−R125−1234yf), and


point O (−2.25x+69.9/0.3629x+31.605/100−R32−R125−1234yf);


mixture 3 having a composition ratio in which


(1)-3. 22.6 wt %>x≥21.2 wt %, and


(2)-3. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a hexagon having the following points as vertices:


point S (100−R32−1234yf−R134a/0.1017x2−5.1872x+102.99/0.0034x2−0.7313x+30.692),


point T (100−R32−1234yf−R134a/−0.0318x2+1.1657x+15.869/−0.123x2+4.4541x−15.735),


point R (−0.0031x2+1.5234x−4.0783/−0.0503x2+3.6856x−32.627/100−R32−R125−1234yf),


point Z (−0.0118x2−4.1976x+121.09/−0.0544x2+8.7425x−137.98/100−R32−R125−1234yf),


point O (0.3214x2−15.507x+206.49/1.2477x2−60.003x+750.62/100−R32−R125−1234yf), and


point H′ (100−R32−1234yf−R134a/−0.9244x+58.883/−0.8837x+36.078);


mixture 4 having a composition ratio in which


(1)-4. 23.2 wt %>x≥22.6 wt %, and


(2)-4. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a pentagon having the following points as vertices:


point S (100−R32−1234yf−R134a/0.1017x2−5.1872x+102.99/0.0034x2−0.7313x+30.692),


point T (100−R32−1234yf−R134a/−0.0318x2+1.1657x+15.869/−0.123x2+4.4541x−15.735),


point R (−0.0031x2+1.5234x−4.0783/−0.0503x2+3.6856x−32.627/100−R32−R125−1234yf),


point Q (−0.0984x2+6.1633x−68.728/−0.0617x2+3.9141x−25.243/100−R32−R125−1234yf), and


point H′ (100−R32−1234yf−R134a/−0.9435x+59.308/−0.8428x+35.149); and


mixture 5 having a composition ratio in which


(1)-5. 25.4 wt %>x≥23.2 wt %, and


(2)-5. the concentrations of R125, 1234yf, and 134a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) fall within a triangle having the following points as vertices:


point S (100−R32−1234yf−R134a/−0.0317x2+0.4511x+43.979/0.075x2−4.1913x+72.494),


point α (0.0324x2−3.5746x+95.092/0.0193x2+3.2487x−59.944/100−R32−R125−1234yf), and


point Q (−0.0115x2+2.3422x−26.868/−0.1077x2+6.4104x−58.357/100−R32−R125−1234yf).


Such a mixture (at least one of mixtures 1 to 5) is preferable in terms of reducing GWP, ensuring ASHRAE non-flammability performance (in which safety ratio are further taken into consideration), exhibiting refrigerating capacity equal to that of R404A (refrigerating capacity higher than that of Embodiment 1-5-A), reducing the compressor outlet temperature in a refrigeration cycle, and improving the coefficient of performance (COP).


The ASHRAE flammability classification of refrigerants is now described.


The ASHRAE flammability classification of refrigerants is performed based on ANSI/ASHRAE Standard 34-2013. Refrigerants classified as Class 1 are non-flammable refrigerants. That is, the composition of the present invention being non-flammable according to ASHRAE means that the mixture of fluorinated hydrocarbons used in the present invention (in particular, the four basic components) is classified as Class 1 in flammability classification.


More specifically, a leak test during storage, shipping, and use is performed based on ANSI/ASHRAE 34-2013 to specify the worst case of fractionation for flammability (WCFF). When the WCFF composition can be identified as being non-flammable in a test based on ASTM E681-2009 (a standard test method for concentration limits of flammability of chemicals (vapors and gases)), it is classified as Class 1.


The following shows a case in which the sum of the concentrations of R32, R125, 1234yf, and R134a is 100 wt %, and the concentration of R32 is 22.6 wt %, and explains a method for specifying ASHRAE non-flammability limits in a ternary composition diagram in which the sum of the concentrations of R125, 1234yf, and R134a is 77.4 wt %.


To specify ASHRAE non-flammability limits in the ternary composition diagram, it is first necessary to determine the non-flammability limits of a binary mixed refrigerant of a flammable refrigerant (R32 or 1234yf) and a non-flammable refrigerant (R134a or R125). The non-flammability limits of the binary mixed refrigerant were determined in Experimental Example 1.


Experimental Example 1 (Non-Flammability Limits of Binary Mixed Refrigerant of Flammable Refrigerant (R32 or 1234yf) and Non-Flammable Refrigerant (R134a or R125))

The non-flammability limits of the binary mixed refrigerant were determined based on the measuring apparatus and measuring method of a flammability test according to ASTM E681-2009.


Specifically, a 12-L spherical glass flask was used so that the combustion state could be visually observed and photographically recorded. When excessive pressure was generated by combustion in the glass flask, gas was allowed to escape from the upper lid. Ignition was achieved by electric discharge from electrodes disposed at one-third the distance from the bottom. The test conditions are as follows.


Test Conditions


Test vessel: 280 mm p spherical (internal volume: 12 liters)


Test temperature: 60° C.±3° C.


Pressure: 101.3 kPa±0.7 kPa


Water: 0.0088 g±0.0005 g per gram of dry air


Mixing ratio of binary refrigerant composition/air: 1 vol. % increments±0.2 vol. %


Binary refrigerant composition mixture: ±0.1 wt %


Ignition method: AC discharge, voltage: 15 kV, electric current: 30 mA, neon transformer


Electrode spacing: 6.4 mm (¼ inch)


Spark: 0.4 seconds±0.05 seconds


Evaluation Criteria:


When the flame propagation extended at an angle of 900 or more from the ignition point, it was evaluated as flammable (propagation).


When the flame propagation extended at an angle of less than 900 from the ignition point, it was evaluated as non-flammable (no flame propagation).


As a result, in the mixed refrigerant of flammable refrigerant R32 and non-flammable refrigerant R134a, no flame propagation was observed from R32=43.0 wt % and R134a=57.0 wt %. These compositions were regarded as non-flammability limits. Moreover, in the case of flammable refrigerant R32 and non-flammable refrigerant R125, no flame propagation was observed from R32=63.0 wt % and R125=37.0 wt %; in the case of flammable refrigerant 1234yf and non-flammable refrigerant R134a, no flame propagation was observed from 1234yf=62.0 wt % and R134a=38.0 wt %; and in the case of flammable refrigerant 1234yf and non-flammable refrigerant R125, no flame propagation was observed from 1234yf=79.0 wt % and R125=21.0 wt %. These compositions were regarded as non-flammability limits. The results are summarized in Table 1.













TABLE 1









Non-




Flammable
flammable



Item
refrigerants
refrigerant









Binary mixed refrigerant
R32
R134a



combination



Non-flammability limit (wt %)
43.0
57.0



Binary mixed refrigerant
R32
R125



combination



Non-flammability limit (wt %)
63.0
37.0



Binary mixed refrigerant
1234yf
R134a



combination



Non-flammability limit (wt %)
62.0
38.0



Binary mixed refrigerant
1234yf
R125



combination



Non-flammability limit (wt %)
79.0
21.0










Next, based on the non-flammability limits of the binary mixed refrigerants determined in Experimental Example 1, ASHRAE non-flammability limits when R32=22.6% were determined in the following manner.


1) Case in which R32=22.6 wt % and 1234yf=0 wt %


When R125+R134a=77.4 wt %, WCFF compositions in mixture compositions close to the ASHRAE non-flammability limits were calculated by REFPROP 9.0. Table 2-1 shows the results. Moreover, whether the calculated WCFF composition was a non-flammability limit composition was examined in the following manner.


(1) Non-flammability limit R134a concentration (wt %) relative to 1234yf concentration of WCFF=1234yf of WCFF (wt %)×38/62=0


(2) Excess R134a concentration (wt %)=R134a concentration of WCFF (wt %)−(1)


(3) Non-flammability limit R32 concentration (wt %) relative to R125 concentration of WCFF=R125 concentration of WCFF composition (wt %)×63/37


(4) Non-flammability limit R134a concentration relative to R32 concentration of (R32 concentration of WCFF−(3))=(R32 concentration of WCFF−(3))×57/43


The composition that satisfied (2)-(4)>0 was regarded as a calculation ASHRAE non-flammability limit.

















TABLE 2-1






R32
R125
1234yf
R134a






Item
(wt %)
(wt %)
(wt %)
(wt %)
(2)
(4)
(2) − (4)
Calculation WCFF























Composition
22.6
2.6
0
74.8



Storage (storage


WCFF
45.6
4.8
0
49.6
49.60
49.61
−0.01
condition)/


Composition
22.6
2.7
0
74.7



shipping (shipping


WCFF
45.6
4.9
0
49.5
49.50
49.39
0.11
condition)


Composition
22.6
2.8
0
74.6



Boiling point + 10° C.


WCFF
45.6
5.1
0
49.3
49.30
48.94
0.36
Vapor phase initial










leak










2) Case in which R32=22.6 wt % and R134a=50.0 wt % (R32/R125≤1.70)


When R125+1234yf=27.4 wt %, WCFF compositions in mixture compositions close to the ASHRAE non-flammability limits were calculated by REFPROP 9.0. Table 2-2 shows the results. Moreover, whether the calculated WCFF composition was a non-flammability limit composition was examined in the following manner.


(1) Non-flammability limit R134a concentration (wt %) relative to 1234yf concentration of WCFF=1234yf of WCFF (wt %)×38/62


(2) Excess R134a concentration (wt %)=R134a concentration of WCFF (wt %)−(1)


(3) Non-flammability limit R32 concentration (wt %) relative to R125 concentration of WCFF=R125 concentration of WCFF composition (wt %)×63/37


(4) Non-flammability limit R134a concentration relative to R32 concentration of (R32 concentration of WCFF−(3))=(R32 concentration of WCFF−(3))×57/43


The composition that satisfied (2)-(4)>0 was regarded as a calculation ASHRAE non-flammability limit.

















TABLE 2-2






R32
R125
1234yf
R134a






Item
(wt %)
(wt %)
(wt %)
(wt %)
(2)
(4)
(2) − (4)
Calculation WCFF























Composition
22.6
10.8
16.6
50.0



Storage (storage


WCFF
41.7
16.1
14.5
27.7
18.81
18.94
−0.12
condition)/


Composition
22.6
10.9
16.5
50.0



shipping (shipping


WCFF
41.7
16.2
14.4
27.7
18.87
18.71
0.16
condition)


Composition
22.6
11.0
16.4
50.0



Boiling point + 10° C.


WCFF
41.6
16.4
14.3
27.7
18.94
18.13
0.81
Vapor phase initial










leak










3) Case in which R32=22.6 wt % and R134a=20.0 wt % (R32/R125≤1.70)


When R125+1234yf=57.4 wt %, WCFF compositions in mixture compositions close to the ASHRAE non-flammability limits were calculated by REFPROP 9.0. Table 2-3 shows the results. Moreover, whether the calculated WCFF composition was a non-flammability limit composition was examined in the following manner.


(1) Non-flammability limit R134a concentration (wt %) relative to 1234yf concentration of WCFF=1234yf of WCFF (wt %)×38/62


(2) Excess R134a concentration (wt %)=R134a concentration of WCFF (wt %)−(1)


(3) Non-flammability limit R32 concentration (wt %) relative to R125 concentration of WCFF=R125 concentration of WCFF composition (wt %)×63/37


(4) Non-flammability limit R134a concentration relative to R32 concentration of (R32 concentration of WCFF−(3))=(R32 concentration of WCFF−(3))×57/43


The composition that satisfied (2)-(4)>0 was regarded as a calculation ASHRAE non-flammability limit.

















TABLE 2-3






R32
R125
1234yf
R134a






Item
(wt %)
(wt %)
(wt %)
(wt %)
(2)
(4)
(2) − (4)
Calculation WCFF























Composition
22.6
20.6
36.8
20.0



Storage (storage


WCFF
39.8
25.7
24.9
9.6
2.325
2.455
−0.130
condition)/


Composition
22.6
20.7
36.7
20.0



shipping (shipping


WCFF
39.7
25.8
24.9
9.6
2.484
2.455
0.029
condition)


Composition
22.6
20.8
36.6
20.0



Boiling point + 10° C.


WCFF
39.7
25.9
24.8
9.6
2.584
2.429
0.155
Vapor phase initial










leak










4) R32=22.6%, R134a=15.9% (Calculation WCFF Change Point)


When R125+R134a=61.5 wt %, WCFF compositions in mixture compositions close to the ASHRAE non-flammability limits were calculated by REFPROP 9.0. Table 2-4 shows the results. Moreover, whether the calculated WCFF composition was a non-flammability limit composition was examined in the following manner.


(1) R125 non-flammability limit concentration (wt %) relative to R32 concentration of WCFF=R32 of WCFF (wt %)×37/63


(2) Excess R125 concentration (wt %)=R125 concentration of WCFF (wt %)−(1)


(3) Non-flammability limit 1234yf concentration (wt %) relative to R134a of WCFF=134a concentration of WCFF composition (wt %)×62/38


(4) R125 non-flammability limit concentration relative to 1234yf concentration of (1234yf concentration of WCFF−(3))=(1234 concentration of WCFF−(3))×21/79


The composition that satisfied (2)-(4)>0 was regarded as a calculation ASHRAE non-flammability limit.

















TABLE 2-4






R32
R125
1234yf
R134a






Item
(wt %)
(wt %)
(wt %)
(wt %)
(2)
(4)
(2) − (4)
Calculation WCFF























Composition
22.6
22.0
39.5
15.9



Storage (storage


WCFF
39.6
26.9
26.0
7.5
3.64
3.66
−0.02
condition)/


Composition
22.6
22.1
39.4
15.9



shipping (shipping


WCFF
39.6
27.0
25.9
7.5
3.74
3.63
0.11
condition)


Composition
22.6
22.2
39.3
15.9



Boiling point + 10° C.


WCFF
39.6
27.1
25.8
7.5
3.84
3.61
0.24
Vapor phase initial










leak









The above calculation WCFF being a change point was confirmed by calculating the WCFF composition from the liquid phase side by REFPROP 9.0 when R134a=15.8, 15.9, and 16.0 wt %. Table 2-5 shows the results. Moreover, whether the determined WCFF composition was a non-flammability limit composition was examined in the following manner.


(1) R125 non-flammability limit concentration (wt %) relative to R32 concentration of WCFF=R32 of WCFF (wt %)×37/63


(2) Excess R125 concentration (wt %)=R125 concentration of WCFF (wt %)−(1)


(3) Non-flammability limit 1234yf concentration (wt %) relative to R134a of WCFF=134a concentration of WCFF composition (wt %)×62/38


(4) R125 non-flammability limit concentration relative to 1234yf concentration of (1234yf concentration of WCFF−(3))=(1234 concentration of WCFF−(3))×21/79


The composition that satisfied (2)-(4)>0 was regarded as a calculation ASHRAE non-flammability limit.

















TABLE 2-5






R32
R125
1234yf
R134a






Item
(wt %)
(wt %)
(wt %)
(wt %)
(2)
(4)
(2) − (4)
Calculation WCFF























Composition
22.6
22.1
39.5
15.8



Storage (storage


WCFF
0.8
4.5
64.7
30.0
4.03
4.19
−0.16
condition)/


Composition
22.6
22.1
39.4
15.9



shipping (shipping


WCFF
0.8
4.5
64.4
30.3
4.03
3.98
0.05
condition) 0° C.


Composition
22.6
22.1
39.3
16.0



Liquid phase 95%


WCFF
0.8
4.5
64.2
30.5
4.03
3.84
0.19
leak









The above results show that WCFF was vapor phase initial leak when R134a≥16.0 wt %, and liquid phase 95% leak when R134a≤15.8 wt %. Thus, R134a=15.9 wt % is a change point of the WCFF composition.


5) ASHRAE Non-Flammability Limit when R32=22.6 and R125=25.0%


When 1234yf+R134a=52.4 wt %, WCFF compositions in mixture compositions close to the ASHRAE non-flammability limit were calculated by REFPROP 9.0. Table 2-6 shows the results. WCFF was liquid phase 95% leak because R134a≤15.8 wt %. Moreover, whether the calculated WCFF composition was a non-flammability limit composition was examined in the following manner.


(1) R125 non-flammability limit concentration (wt %) relative to R32 concentration of WCFF=R32 of WCFF (wt %)×37/63


(2) Excess R125 concentration (wt %)=R125 concentration of WCFF (wt %)−(1)


(3) Non-flammability limit 1234yf concentration (wt %) relative to R134a of WCFF=134a concentration of WCFF composition (wt %)×62/38


(4) R125 non-flammability limit concentration relative to 1234yf concentration of (1234yf concentration of WCFF−(3))=(1234 concentration of WCFF−(3))×21/79


The composition that satisfied (2)-(4)>0 was regarded as a calculation ASHRAE non-flammability limit.

















TABLE 2-6






R32
R125
1234yf
R134a






Item
(wt %)
(wt %)
(wt %)
(wt %)
(2)
(4)
(2) − (4)
Calculation WCFF























Composition
22.6
25.0
38.1
14.3



Storage (storage


WCFF
0.5
4.5
65.2
29.8
4.21
4.41
−0.20
condition)/


Composition
22.6
25.0
38.0
14.4



shipping (shipping


WCFF
0.5
4.5
64.9
30.1
4.21
4.20
0.01
condition) −10° C.


Composition
22.6
25.0
37.9
14.5



Liquid phase 95%


WCFF
0.5
4.5
64.7
30.3
4.21
4.06
0.15
leak


Composition
22.6
24.9
45.4
7.1



Storage (storage


WCFF
39.4
29.1
28.2
3.3
5.96
6.06
−0.10
condition)/


Composition
22.6
25.0
45.3
7.1



shipping (shipping


WCFF
39.4
29.2
28.1
3.3
6.06
6.04
0.02
condition)


Composition
22.6
25.1
45.2
7.1



Boiling point + 10° C.


WCFF
39.4
29.3
28.0
3.3
6.16
6.01
0.15
Vapor phase initial










leak










6) ASHRAE Non-Flammability Limit when GWP=1500


The WCFF composition of a composition in which GWP was 1500 (22.6/34.2/32.8/10.4) (R32 concentration (wt %)/R125 concentration (wt %)/1234yf concentration (wt %)/R134a concentration (wt %)), and WCFF compositions in mixture compositions close to the ASHRAE non-flammability limits were calculated by REFPROP 9.0. Table 2-7 shows the results. Moreover, whether the calculated WCFF composition was a non-flammability limit composition was examined in the following manner.


(1) R125 non-flammability limit concentration (wt %) relative to R32 concentration of WCFF=R32 of WCFF (wt %)×37/63


(2) Excess R125 concentration (wt %)=R125 concentration of WCFF (wt %)−(1)


(3) Non-flammability limit 1234yf concentration (wt %) relative to R134a of WCFF=134a concentration of WCFF composition (wt %)×62/38


(4) R125 non-flammability limit concentration relative to 1234yf concentration of (1234yf concentration of WCFF−(3))=(1234 concentration of WCFF−(3))×21/79


The composition that satisfied (2)-(4)>0 was regarded as a calculation ASHRAE non-flammability limit.

















TABLE 2-7






R32
R125
1234yf
R134a






Item
(wt %)
(wt %)
(wt %)
(wt %)
(2)
(4)
(2) − (4)
Calculation WCFF























Composition
22.6
34.2
32.9
10.3



Storage (storage


WCFF
0.2
5.4
66.2
28.2
5.28
5.37
−0.08
condition)/


Composition
22.6
34.2
32.8
10.4



shipping (shipping


WCFF
0.2
5.4
65.8
28.6
5.28
5.09
0.20
condition) −32° C.


Composition
22.6
34.2
32.7
10.5



Liquid phase 95%


WCFF
0.2
5.4
65.5
28.9
5.28
4.88
0.41
leak









The results of examining the above calculation ASHRAE non-flammability limit compositions are shown in a ternary composition diagram. The results of determining regression lines connecting these points are a straight line connecting points G and H, and a straight line connecting points H and I shown in FIG. 1.


Experimental Example 2 (Examination of Calculation Non-Flammability Limits Obtained in Experimental Example 1 by Combustion Test)

A combustion test was carried out according to ASTM E681 shown in Experimental Example 1 using, as representative examples, the WCFF composition (41.7/16.2/14.4/27.7) of the composition (R32/R125/1234yf/R134a)=(22.6/10.9/16.5/50.0), and the WCFF composition (0.2/5.4/65.8/28.6) of the composition (R32/R125/1234yf/R134a)=(22.6/34.2/32.8/10.4). As a result, flame propagation was not observed in these WCFF compositions.


Therefore, the ASHRAE non-flammability limits determined by calculation in Experimental Example 1 based on the non-flammability limits of the binary compositions determined in Experimental Example 1 satisfy the requirements for ASHRAE non-flammability based on ANSI/ASHRAE Standard 34-2013.


Moreover, as shown in FIG. 1 (a ternary diagram when R32=22.6%), the ASHRAE non-flammability limit with a GWP of 1500 or less is represented by a straight line (line HI) connecting 1234yf=0 wt % (the point determined by method 1) above; point I in FIG. 1) and R32=30%, R134a=10.3% (calculation WCFF change point) (the point determined by method 4) above; point H in FIG. 1), and a straight line (line GH) connecting point H and GWP=1500 (the point determined by method 6) above; point G in FIG. 1).


Hereinafter, the ASHRAE non-flammability limits in the present specification are represented by regression lines (line HI and line GH) determined by methods 1), 4), and 6) above based on the non-flammability limits of the binary compositions determined in Experimental Example 1. Table 2-8 shows the R32 concentration, R125 concentration, 1234yf concentration, and R134a concentration of point G, point H, and point I when the R32 concentration is 10.8, 12.4, 14.8, 16.1, 18.1, 19.0, 20.0, 21.6, 22.6, 23.2, 24.5, 25.6, and 26.6 wt %.













TABLE 2-8









Point G
Point H
Point I
















R32
R125
1234yf
R134a
R125
1234yf
R134a
R125
1234yf
R134a


(wt %)
(wt %)
(wt %)
(wt %)
(wt %)
(wt %)
(wt %)
(wt %)
(wt %)
(wt %)



















10.8
34.5
39.4
15.3
11.6
50.3
27.3
0.0
22.5
66.7


12.4
34.5
38.5
14.6
13.1
48.8
25.7
0.0
18.2
69.4


14.8
34.4
37.2
13.6
15.4
46.5
23.3
0.0
11.7
73.5


16.1
34.4
36.4
13.1
16.5
45.3
22.1
0.0
8.6
75.3


18.1
34.3
35.3
12.3
18.3
43.5
20.1
0.0
3.9
78.0


19.0
34.3
34.8
11.9
19.2
42.7
19.1
0.0
2.0
79.0


20.0
34.2
34.3
11.5
20.1
41.8
18.1
0.0
0.0
80.0


21.6
34.2
33.4
10.8
21.4
40.3
16.7
1.7
0.0
76.7


22.6
34.2
32.8
10.4
22.1
39.4
15.9
2.7
0.0
74.7


23.2
34.2
32.5
10.1
22.6
38.8
15.4
3.3
0.0
73.5


24.5
34.2
31.8
9.5
23.6
37.6
14.3
4.5
0.0
71.0


25.6
34.2
31.2
9.0
24.3
36.6
13.5
5.6
0.0
68.8


26.6
34.2
30.6
8.6
25.1
25.6
12.7
6.6
0.0
66.8









In the ASHRAE non-flammability limits determined by calculation as described above, safety ratio are preferably further taken into consideration, in view of the purity of each refrigerant during production, error during mixing, etc. ASHRAE non-flammability limit line GH was moved in parallel so that the concentration of non-flammable refrigerant R134a was higher by 1 wt % (because ±1 wt % is often expected as the allowable concentration during production), by reducing the 1234yf concentration by 1.63 wt % (63/37) based on the non-flammability limit mixing ratio of R134a and 1234yf. Thus, line segment G′H′ in which safety ratio were taken into consideration was obtained. Moreover, ASHRAE non-flammability limit line HI was moved in parallel so that the concentration of non-flammable refrigerant R125 was higher by 1 wt % (because ±1 wt % is often expected as the allowable concentration during production), by reducing the 1234yf concentration by 3.76 wt % (79/21) based on the non-flammability limit mixing ratio of R134a and 1234yf. Thus, line segment H′I′ in which safety ratio were taken into consideration was obtained.


Regarding ASHRAE non-flammability lines G′H′I′ in which safety ratio are taken into consideration, for example, in the case of R32=22.6 wt %, when R125=y wt %, 1234yf=z wt %, and R134a=w wt %, line segment GH was represented by z=1.2w+42.92 in a ternary diagram in which y+z+w=100 wt %; thus, 1.63 was subtracted from 42.92, line segment G′H′ was represented by z=1.2w+41.29, and the intersection of line segment G′H′ and line segment AD was regarded as G′. Line segment HI was represented by z=2.0309y+17.116; thus, 3.76 was subtracted from 17.116, line segment H′I′ was represented by z=2.0309y+13.356, and the intersection of line segment H′I′ and line segment DI was regarded as I′. Moreover, H′ was determined as an intersection of line segment G′H′ represented by the formula z=1.2w+41.29, and line segment H′I′ represented by the formula z=2.0309y+13.356.


Table 2-9 shows ASHRAE non-flammability points G′, H′, and I′ in which safety ratio were taken into consideration in the above manner.













TABLE 2-9









Point G′
Point H′
Point I′
















R32
R125
1234yf
R134a
R125
1234yf
R134a
R125
1234yf
R134a


(wt %)
(wt %)
(wt %)
(wt %)
(wt %)
(wt %)
(wt %)
(wt %)
(wt %)
(wt %)



















10.8
34.0
38.8
16.4
12.6
49.0
27.6
0.0
18.7
70.5


12.4
34.0
37.9
15.7
14.1
47.5
26.0
0.0
14.4
73.2


14.8
34.0
36.5
14.7
16.5
45.1
23.6
0.0
7.9
77.3


16.1
33.9
35.8
14.2
17.6
43.9
22.4
0.0
4.8
79.1


18.1
33.9
34.7
13.3
19.4
42.1
20.4
0.0
0.0
81.9


19.0
33.8
34.3
12.9
20.3
41.3
19.3
0.8
0.0
80.2


20.0
33.8
33.7
12.5
21.2
40.4
18.4
1.8
0.0
78.2


21.6
33.8
32.9
11.7
22.5
38.9
17.0
3.5
0.0
74.9


22.6
33.8
32.3
11.3
23.3
38.0
16.1
4.6
0.0
72.8


23.2
33.8
32.0
11.0
23.8
37.4
15.6
5.2
0.0
71.6


24.5
33.9
31.4
32.0
24.8
36.2
14.5
6.4
0.0
69.1


25.6
33.9
30.6
9.9
25.6
35.1
13.7
7.5
0.0
66.9


26.6
33.8
30.1
9.5
26.3
34.1
13.0
8.6
0.0
64.8









The composition ratio of R32, R125, 1234yf, and R134a contained in the mixture can be represented by points in a ternary composition diagram of R125, 1234yf, and R134a under the restriction by the condition of R32 concentration.


Specifically, when the concentration of R32 is x wt %, the sum of the concentrations of R125, 1234yf, and R134a is (100−x) wt %; and the composition ratio of R32, R125, 1234yf, and R134a contained in the mixture can be represented by coordinate points in a ternary composition diagram in which the sum of the concentrations of R125, 1234yf, and R134a is (100−x). The following shows a specific method for determining the coordinate points.


Hereinafter, cases were classified according to the range of x. The meaning of each of points A, B, C, D, E, F, B′, C′, E′, F′, G, H, I, G′, H′, I′, J, K, L, M, N, O, P, Q, R, S, T, U, V, W, X, Y, Z, and α is as described below. The concentration of each point is determined in Example 1, described later, and the determined values are shown.


A: Composition ratio in which GWP=1500 and the concentration (wt %) of R134a is 0 wt %


D: Composition ratio in which GWP=1500 and the concentration (wt %) of 1234yf is 0 wt %


G: Composition ratio in which GWP=1500 and which shows an ASHRAE non-flammability limit (when the WCFF becomes a liquid phase composition after 95% leak under the storage/shipping conditions)


H: Composition ratio showing an ASHRAE non-flammability limit (when the WCFF becomes a liquid phase composition after 95% leak under the storage/shipping conditions, and becomes a vapor phase composition at the time of 0% leak)


I: Composition ratio showing an ASHRAE non-flammability limit, in which the concentration (wt %) of 1234yf is 0 wt % (the WCFF is a vapor phase composition at the time of 0% leak under the storage/shipping conditions)


G′: Composition ratio showing an intersection of a line segment in which GWP=1500 and a line segment obtained by adding 1 wt of non-flammable refrigerant R134a to line segment GH, which shows an ASHRAE non-flammability limit, in order to take into consideration safety ratio of non-flammability


H′: Composition ratio showing an intersection of a line segment obtained by adding 1 wt % of non-flammable refrigerant R134a to line segment GH, which shows an ASHRAE non-flammability limit, and a line segment obtained by adding 1 wt % of non-flammable refrigerant R125 to line segment HI


I′: Composition ratio on a line segment obtained by adding 1 wt % of non-flammable refrigerant R125 to line segment HI, which shows an ASHRAE non-flammability limit, in order to take into consideration safety ratio of non-flammability, in which the concentration (wt %) of 1234yf is 0 wt %


B: Composition ratio present on line segments G′H′I′, in which the compressor outlet pressure is 102.5% of the R22 pressure


C: Composition ratio in which GWP=1500 and the compressor outlet pressure is 102.5% of the R22 pressure


E: Composition ratio present on line segments G′H′I′, in which the compressor outlet pressure is 97.5% of the R22 pressure


F: Composition ratio in which GWP=1500 and the compressor outlet pressure is 97.5% of the R22 pressure


B′: Composition ratio present on line segments G′H′I′, in which the compressor outlet pressure is 101.25% of the R22 pressure


C′: Composition ratio in which GWP=1500 and the compressor outlet pressure is 101.25% of the R22 pressure


E′: Composition ratio present on line segments G′H′I′, in which the compressor outlet pressure is 98.75% of the R22 pressure


F′: Composition ratio in which GWP=1500 and the compressor outlet pressure is 98.75% of the R22 pressure


J: Composition ratio present on line segments G′H′I′, in which the refrigerating capacity relative to that of R404 is 85%


K: Composition ratio in which GWP=1500 and the refrigerating capacity relative to that of R404 is 85%


L: Composition ratio present on line segments G′H′I′, in which the refrigerating capacity relative to that of R404 is 90%


M: Composition ratio in which GWP=1500 and the refrigerating capacity relative to that of R404 is 90%


O: Composition ratio present on line segments G′H′I′, in which the refrigerating capacity relative to that of R404 is 95%


P: Composition ratio in which GWP=1500 and the refrigerating capacity relative to that of R404 is 95%


Q: Composition ratio present on line segments G′H′I′, in which the compressor outlet temperature is 115° C.


R: Composition ratio in which GWP=1500 and the compressor outlet temperature is 115° C.


S: Composition ratio present on line segments G′H′I′, in which COP is 107.75% of that of R404A


T: Composition ratio in which GWP=1500, and COP is 107.75% of that of R404A


U: Intersection of line segment ST and line segment JK


V: Intersection of line segment ST and line segment LM


W: Intersection of line segment ST and line segment OP


X: Intersection of line segment QR and line segment JK


Y: Intersection of line segment OR and line segment LM


Z: Intersection of line segment QR and line segment OP


α: Intersection of line segment ST and line segment QR


N: Point in which R125=0 and R134a=0 (0/0/100−x)


(1) Method for Determining Points a, D, G, H, I, G′, H′, and I′


(1-1) Point a


14.8 wt %≥x≥10.8 wt %


When the concentration of x=R32 is 10.8 wt %, point A in the ternary composition diagram in which the sum of the concentrations of R125, 1234yf, and 134a is (100−x) wt % is: (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %))=(40.7/40.5/0);


when the concentration of R32 is 12.4 wt %, point A in the ternary composition diagram in which the sum of the concentrations of R125, 1234yf, and 134a is (100−x) wt % is:

(R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %))=(40.4/47.2/0); and

when the concentration of R32 is 14.8 wt %, point A in the ternary composition diagram in which the sum of the concentrations of R125, 1234yf, and 134a is (100−x) wt % is:

(R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %))=(40.0/45.2/0).

Accordingly, in the case where the concentration of R125 is regarded as y wt % when the sum of the concentrations of R32, R125, 1234yf, and 134a is 100 wt %, a regression line determined from the above three points plotted in the x-y coordinate is represented by the formula:

y=−1.743x+42.575.

Moreover, since the R134a concentration of point A is 0 wt %, the 1234yf concentration of point A is represented by (100−R32 concentration (wt %)−R125 concentration (wt %).


In light of the above, point A in the ternary composition diagram in which the sum of the concentrations of R125, 1234yf, and R134a is (100−x) (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) is represented by (42.575−1.743x/100−R32 concentration-R125 concentration/0).


The same calculations were performed for the following ranges: 18.1 wt %≥x≥14.8 wt %, 20.0 wt %≥x≥18.1 wt %, 22.6 wt %≥x≥20.0 wt %, 24.5 wt %≥x≥22.6 wt %, and 26.6 wt %≥x≥24.5 wt %. Table 3-1 shows (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) for each concentration range, determined by the approximate expression of x when R32=x wt %.









TABLE 3-1







Point A










Item
14.8 ≥ x ≥ 10.8
18.1 ≥ x ≥ 14.8
20.0 ≥ x ≥ 18.1



















R32
10.8
12.4
14.8
14.8
16.1
18.1
18.1
19.0
20.0


R125
40.7
40.4
40.0
40.0
39.7
39.3
39.3
39.1
38.9


1234yf
48.5
47.2
45.2
45.2
44.2
42.6
42.6
41.9
41.1


R134a
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0










R32
x
x
x


R125
−0.1743x + 42.575
−0.2111x + 43.115
−0.2103x + 43.103


approximate


expression


1234yf
100-R32-R125-R134a
100-R32-R125-R134a
100-R32-R125-R134a


approximate


expression


R134a
0
0
0


approximate


expression










Point A










Item
22.6 ≥ x ≥ 20.0
24.5 ≥ x ≥ 22.6
26.6 ≥ x ≥ 24.5



















R32
20.0
21.6
22.6
22.6
23.2
24.5
24.5
25.6
26.6


R125
38.9
38.6
38.4
38.4
38.3
38.1
38.1
37.9
37.7


1234yf
41.1
39.8
39.0
39.0
38.5
37.4
37.4
36.5
35.7


R134a
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0










R32
x
x
x


R125
−0.1919x + 42.739
−0.1572x + 41.951
−0.1903x + 42.766


approximate


expression


1234yf
100-R32-R125-R134a
100-R32-R125-R134a
100-R32-R125-R134a


approximate


expression


R134a
0
0
0


approximate


expression










(1-2) Point D


For point D, the same calculations as those of point A were performed for the following ranges: 14.8 wt %≥x≥10.8 wt %, 18.1 wt %≥x≥14.8 wt %, 20.0 wt %≥x≥18.1 wt %, 22.6 wt %≥x≥20.0 wt %, 24.5 wt %≥x≥22.6 wt, and 26.6 wt %≥x≥24.5 wt %. Table 3-2 shows (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) for each concentration range, determined by the approximate expression of x when R32=x wt %.









TABLE 3-2







Point D










Item
14.8 ≥ x ≥ 10.8
18.1 ≥ x ≥ 14.8
20.0 ≥ x ≥ 18.1



















R32
10.8
12.4
14.8
14.8
16.1
18.1
18.1
19.0
20.0


R125
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.8
1.8


1234yf
18.7
14.4
7.9
7.9
4.8
0.0
0.0
0.0
0.0


R134a
70.5
73.2
77.3
77.3
79.1
81.9
81.9
80.2
78.2










R32
x
x
x


R125
0.375x + 3.25
0.3625x + 3.4461
0.369x + 3.31


approximate


expression


1234yf
0
0
0


approximate


expression


R134a
100-R32-R125-1234yf
100-R32-R125-1234yf
100-R32-R125-1234yf


approximate


expression










Point D










Item
22.6 ≥ x ≥ 20.0
24.5 ≥ x ≥ 22.6
26.6 ≥ x ≥ 24.5



















R32
20.0
21.6
22.6
22.6
23.2
24.5
24.5
25.6
26.6


R125
1.8
3.5
4.6
4.6
5.2
6.4
6.4
7.5
8.6


1234yf
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0


R134a
78.2
74.9
72.8
72.8
71.6
69.1
69.1
66.9
64.8










R32
x
x
x


R125
0.3430x + 3.826
0.3710x + 3.2057
0.3323x + 4.1369


approximate


expression


1234yf
0
0
0


approximate


expression


R134a
100-R32-R125-1234yf
100-R32-R125-1234yf
100-R32-R125-1234yf


approximate


expression










(1-3) Point G


For point G, the same calculations as those of point A were performed for the following ranges: 14.8 wt %≥x≥10.8 wt %, 18.1 wt %≥x≥14.8 wt %, 20.0 wt %≥x≥18.1 wt %, 22.6 wt %≥x≥20.0 wt %, 24.5 wt %≥x≥22.6 wt %, and 26.6 wt %≥x≥24.5 wt %. Table 3-3 shows (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) for each concentration range, determined by the approximate expression of x when R32=x wt %.









TABLE 3-3







Point G










Item
14.8 ≥ x ≥ 10.8
18.1 ≥ x ≥ 14.8
20.0 ≥ x ≥ 18.1



















R32
10.8
12.4
14.8
14.8
16.1
18.1
18.1
19.0
20.0


R125
34.5
34.5
34.4
34.4
34.4
34.3
34.3
34.3
34.2


1234yf
39.4
38.5
37.2
37.2
36.4
35.3
35.3
34.8
34.3


R134a
15.3
14.6
13.6
13.6
13.1
12.3
12.3
11.9
11.5










R32
x
x
x


R125
100-R32-1234yf-R134a
100-R32-1234yf-R134a
100-R32-1234yf-R134a


approximate


expression


1234yf
−0.5493x + 45.325
−0.5736x + 45.669
−0.5258x + 44.808


approximate


expression


R134a
−0.4243x + 19.875
−0.3945x + 19.443
−0.4207x + 19.907


approximate


expression










Point G










Item
22.6 ≥ x ≥ 20.0
24.5 ≥ x ≥ 22.6
26.6 ≥ x ≥ 24.5



















R32
20.0
21.6
22.6
22.6
23.2
24.5
24.5
25.6
26.6


R125
34.2
34.2
34.2
34.2
34.2
34.2
34.2
34.2
34.2


1234yf
34.3
33.4
32.8
32.8
32.5
31.8
31.8
31.2
30.6


R134a
11.5
10.8
10.4
10.4
10.1
9.5
9.5
9.0
8.6










R32
x
x
x


R125
100-R32-1234yf-R134a
100-R32-1234yf-R134a
100-R32-1234yf-R134a


approximate


expression


1234yf
−0.5756x + 45.817
−0.5283x + 44.746
−0.5710x + 45.798


approximate


expression


R134a
−0.4244x + 19.983
−0.4717x + 21.054
−0.4290x + 20.002


approximate


expression










(1-4) Point H


For point H, the same calculations as those of point A were performed for the following ranges: 14.8 wt %≥x≥10.8 wt %, 18.1 wt %≥x≥14.8 wt %, 20.0 wt %≥x≥18.1 wt %, 22.6 wt %≥x≥20.0 wt %, 24.5 wt %≥x≥22.6 wt %, and 26.6 wt %≥x≥24.5 wt %. Table 3-4 shows (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) for each concentration range, determined by the approximate expression of x when R32=x wt %.









TABLE 3-4







Point H










Item
14.8 ≥ x ≥ 10.8
18.1 ≥ x ≥ 14.8
20.0 ≥ x ≥ 18.1



















R32
10.8
12.4
14.8
14.8
16.1
18.1
18.1
19.0
20.0


R125
11.6
13.1
15.4
15.4
16.5
18.3
18.3
19.2
20.1


1234yf
50.3
48.8
46.5
46.5
45.3
43.5
43.5
42.7
41.8


R134a
27.3
25.7
23.3
23.3
22.1
20.1
20.1
19.1
18.1










R32
x
x
x


R125
100-R32-1234yf-R134a
100-R32-1234yf-R134a
100-R32-1234yf-R134a


approximate


expression


1234yf
−0.9507x + 60.575
−0.9083x + 59.936
−0.8948x + 59.698


approximate


expression


R134a
   −x + 38.1
−0.9723x + 37.714
−1.0517x + 39.117


approximate


expression










Point H










Item
22.6 ≥ x ≥ 20.0
24.5 ≥ x ≥ 22.6
26.6 ≥ x ≥ 24.5



















R32
20.0
21.6
22.6
22.6
23.2
24.5
24.5
25.6
26.6


R125
20.1
21.4
22.1
22.1
22.6
23.6
23.6
24.3
25.1


1234yf
41.8
40.3
39.4
39.4
38.8
37.6
37.6
36.6
25.6


R134a
18.1
16.7
15.9
15.9
15.4
14.3
14.3
13.5
12.8










R32
x
x
x


R125
100-R32-1234yf-R134a
100-R32-1234yf-R134a
100-R32-1234yf-R134a


approximate


expression


1234yf
−0.9244x + 60.283
−0.9435x + 60.078
−0.9517x + 60.931


approximate


expression


R134a
−0.8488x + 35.065
−0.8428x + 34.949
−0.7613x + 32.965


approximate


expression










(1-5) Point I


For point I, the same calculations as those of point A were performed for the following ranges: 14.8 wt %≥x≥10.8 wt %, 18.1 wt %≥x≥14.8 wt %, 20.0 wt %≥x≥18.1 wt %, 22.6 wt %≥x≥20.0 wt %, 24.5 wt %≥x≥22.6 wt %, and 26.6 wt %≥x≥24.5 wt %. Table 3-5 shows (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) for each concentration range, determined by the approximate expression of x when R32=x wt %.









TABLE 3-5







Point I










Item
14.8 ≥ x ≥ 10.8
18.1 ≥ x ≥ 14.8
20.0 ≥ x ≥ 18.1



















R32
10.8
12.4
14.8
14.8
16.1
18.1
18.1
19.0
20.0


R125
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0


1234yf
22.5
18.1
11.7
11.7
8.6
3.9
3.9
2.0
0.0


R134a
66.7
69.5
73.5
73.5
75.3
78.0
78.0
79.0
80.0










R32
x
x
x


R125
0
0
0


approximate


expression


1234yf
100-R32-1234yf-R134a
100-R32-1234yf-R134a
100-R32-1234yf-R134a


approximate


expression


R134a
1.6974x + 48.4
1.3625x + 53.346
1.0517x + 58.983


approximate


expression










Point I










Item
22.6 ≥ x ≥ 20.0
24.5 ≥ x ≥ 22.6
26.6 ≥ x ≥ 24.5



















R32
20.0
21.6
22.6
22.6
23.2
24.5
24.5
25.6
26.6


R125
0.0
1.7
2.7
2.7
3.3
4.5
4.5
5.7
6.6


1234yf
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0


R134a
80.0
76.7
74.7
74.7
73.5
71.0
71.0
68.7
66.8










R32
x
x
x


R125
100-R32-1234yf-R134a
100-R32-1234yf-R134a
100-R32-1234yf-R134a


approximate


expression


1234yf
0
0
0


approximate


expression


R134a
−2.0407x + 120.8
−1.9435x + 118.61
−2.0000x + 120.00


approximate


expression










(1-6) Point G′


For point G′, the same calculations as those of point A were performed for the following ranges: 14.8 wt %≥x≥10.8 wt %, 18.1 wt %≥x≥14.8 wt %, 20.0 wt %≥x≥18.1 wt %, 22.6 wt %≥x≥20.0 wt %, 24.5 wt %≥x≥22.6 wt %, and 26.6 wt %≥x≥24.5 wt %. Table 3-6 shows (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) for each concentration range, determined by the approximate expression of x when R32=x wt %.









TABLE 3-6







Point G′










Item
14.8 ≥ x ≥ 10.8
18.1 ≥ x ≥ 14.8
20.0 ≥ x ≥ 18.1



















R32
10.8
12.4
14.8
14.8
16.1
18.1
18.1
19.0
20.0


R125
34.0
34.0
34.0
34.0
33.9
33.9
33.9
33.8
33.8


1234yf
38.8
37.9
36.5
36.5
35.8
34.7
34.7
34.3
33.7


R134a
16.4
15.7
14.7
14.6
14.2
13.3
13.3
12.9
12.5










R32
x
x
x


R125
100-R32-1234yf-R134a
100-R32-1234yf-R134a
100-R32-1234yf-R134a


approximate


expression


1234yf
−0.5757x + 45.025
−0.5458x + 44.582
−0.5277x + 44.277


approximate


expression


R134a
−0.4243x + 20.975
−0.4264x + 21.031
−0.4207x + 20.907


approximate


expression










Point G′










Item
22.6 ≥ x ≥ 20.0
24.5 ≥ x ≥ 22.6
26.6 ≥ x ≥ 24.5



















R32
20.0
21.6
22.6
22.6
23.2
24.5
24.5
25.6
26.6


R125
33.8
33.8
33.8
33.8
33.8
33.9
33.9
33.9
33.8


1234yf
33.7
32.9
32.3
32.3
32.0
21 2
21.2
30.6
30.1


R134a
12.5
11.7
11.3
11.3
11.0
10.4
10.4
9.9
9.5










R32
x
x
x


R125
100-R32-1234yf-R134a
100-R32-1234yf-R134a
100-R32-1234yf-R134a


approximate


expression


1234yf
−0.5349x + 44.413
−0.5848x + 45.537
−0.5242x + 44.035


approximate


expression


R134a
−0.4651 x + 21.787
−0.4717x + 21.954
−0.4290x + 20.902


approximate


expression










(1-7) Point H′


For point H′, the same calculations as those of point A were performed for the following ranges: 14.8 wt %≥x≥10.8 wt. %, 18.1 wt %≥x≥14.8 wt %, 20.0 wt %≥x≥18.1 wt %, 22.6 wt %≥x≥20.0 wt %, 24.5 wt %≥x≥22.6 wt %, and 26.6 wt %≥x≥24.5 wt %. Table 3-7 shows (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) for each concentration range, determined by the approximate expression of x when R32=x wt %.









TABLE 3-7







Point H′










Item
14.8 ≥ x ≥ 10.8
18.1 ≥ x ≥ 14.8
20.0 ≥ x ≥ 18.1



















R32
10.8
12.4
14.8
14.8
16.1
18.1
18.1
19.0
20.0


R125
12.6
14.1
16.5
16.5
17.6
19.4
19.4
20.3
21.2


1234yf
49.0
47.5
45.1
45.1
43.9
42.1
42.1
41.3
40.4


R134a
27.6
26.0
23.6
23.6
22.4
20.4
20.4
19.3
18.4










R32
x
x
x


R125
100-R32-1234yf-R134a
100-R32-1234yf-R134a
100-R32-1234yf-R134a


approximate


expression


1234yf
−0.9770x + 59.575
−0.9083x + 58.536
−0.8948x + 58.298


approximate


expression


R134a
   −x + 38.4
−0.9723x + 38.014
−1.0517x + 39.417


approximate


expression










Point H′










Item
22.6 ≥ x ≥ 20.0
24.5 ≥ x ≥ 22.6
26.6 ≥ x ≥ 24.5



















R32
20.0
21.6
22.6
22.6
23.2
24.5
24.5
25.6
26.6


R125
21.2
22.5
23.3
23.3
23.8
24.8
24.8
25.6
26.3


1234yf
40.4
38.9
38.0
38.0
37.4
36.2
36.2
35.1
34.1


R134a
18.4
17.0
16.1
16.1
15.6
14.5
14.5
13.7
13.0










R32
x
x
x


R125
100-R32-1234yf-R134a
100-R32-1234yf-R134a
100-R32-1234yf-R134a


approximate


expression


1234yf
−0.9244x + 58.883
−0.9435x + 59.308
   −x + 60.7


approximate


expression


R134a
−0.8837x + 36.078
−0.8428x + 35.149
−0.7145x + 32.001


approximate


expression










(1-8) Point I′


For point I′, the same calculations as those of point A were performed for the following ranges: 14.8 wt %≥x≥10.8 wt %, 18.1 wt %≥x≥14.8 wt %, 20.0 wt %≥x≥18.1 wt %, 22.6 wt %≥x≥20.0 wt %, 24.5 wt %≥x≥22.6 wt %, and 26.6 wt %≥x≥24.5 wt %. Table 3-7 shows (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) for each concentration range, determined by the approximate expression of x when R32=x wt %.









TABLE 3-8







Point I′










Item
14.8 ≥ x ≥ 10.8
18.1 ≥ x ≥ 14.8
20.0 ≥ x ≥ 18.1



















R32
10.8
12.4
14.8
14.8
16.1
18.1
18.1
19.0
20.0


R125
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.8
1.8


1234yf
18.7
14.4
7.9
7.9
4.8
0.0
0.0
0.0
0.0


R134a
70.5
73.2
77.3
77.3
79.1
81.9
81.9
80.2
78.2










R32
x
x
x


R125
0
0
100-R32-1234yf-R134a


approximate


expression


1234yf
100-R32-1234yf-R134a
100-R32-1234yf-R134a
0


approximate


expression


R134a
1.7007x + 52.125
1.3945x + 56.657
1.9483x + 117.18


approximate


expression










Point I′










Item
22.6 ≥ x ≥ 20.0
24.5 ≥ x ≥ 22.6
26.6 ≥ x ≥ 24.5



















R32
20.0
21.6
22.6
22.6
23.2
24.5
24.5
25.6
26.6


R125
1.8
3.5
4.6
4.6
5.2
6.4
6.4
7.5
8.6


1234yf
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0


R134a
78.2
74.9
72.8
72.8
71.6
69.1
69.1
66.9
64.8










R32
x
x
x


R125
100-R32-1234yf-R134a
100-R32-1234yf-R134a
100-R32-1234yf-R134a


approximate


expression


1234yf
0
0
0


approximate


expression


R134a
−2.0756x + 119.72
−1.9435x + 116.71
−2.0468x + 119.26


approximate


expression










(2) Method for Determining Points B, C, E, F, B′, C′, E′, and F′


(2-1) Point B


For point B, the same calculations as those of point A were performed for the following ranges: 14.1 wt %≥x≥10.8 wt %, 16.1 wt %≥x≥14.1 wt %, 16.8 wt %≥x≥16.1 wt %, 18.1 wt %≥x≥16.8 wt %, 20.0 wt %≥x≥18.1 wt %, 21.6 wt %≥x≥20.0 wt %, and 24.2 wt %≥x≥21.6 wt %. Table 3-9 shows (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) for each concentration range, determined by the approximate expression of x when R32=x wt %.









TABLE 3-9







Point B











Item
14.1 ≥ x ≥ 10.8
16.1 ≥ x ≥ 14.1
16.8 ≥ x ≥ 16.1
18.1 ≥ x ≥ 16.8




















R32
10.8
12.4
14.1
14.1
14.8
16.1
16.1
16.8
16.8
18.1


R125
34.0
29.7
25.2
25.2
23.3
19.9
19.9
18.3
18.3
16.4


1234yf
38.8
40.0
41.2
41.2
41.8
42.8
42.8
43.3
43.3
35.6


R134a
16.4
17.9
19.5
19.5
20.1
21.2
21.2
21.6
21.6
29.9











R32
x
x
x
x


R125
−2.6665x + 62.786
−2.6456x + 62.484
−2.2857x + 56.7  
−1.4615x + 42.854


approximate


expression


1234yf
 0.7204x + 31.027
 0.7929x + 29.984
0.7747x + 30.285
 −5.931x + 142.94


approximate


expression


R134a
100-R32-R125-1234yf
100-R32-R125-1234yf
100-R32-R125-1234yf
100-R32-R125-1234yf


approximate


expression










Point B










Item
20 ≥ x ≥ 18.1
21.6 ≥ x ≥ 20.0
24.2 ≥ x ≥ 21.6


















R32
18.1
18.7
20.0
20.0
21.6
21.6
22.6
24.2


R125
16.4
15.7
14.4
14.4
13.0
13.0
12.2
11.1


1234yf
35.6
32.4
26.2
26.2
19.3
19.3
15.4
9.8


R134a
29.9
33.2
39.4
39.4
46.1
46.1
49.8
54.9










R32
x
x
x


R125
−1.0442x + 35.27
−0.875x + 31.9 
−0.7267x + 28.67


approximate


expression


1234yf
0.2703x2 − 15.221x + 222.52
−4.3372x + 112.98
0.1603x2 − 10.987x + 181.82


approximate


expression


R134a
100-R32-1234yf-R134a
100-R32-1234yf-R134a
100-R32-1234yf-R134a


approximate


expression










(2-2) Point C


For point C, the same calculations as those of point A were performed for the following ranges: 14.1 wt %≥x≥10.8 wt %, 16.1 wt %≥x≥14.1 wt %, 16.8 wt %≥x≥16.1 wt %, 18.1 wt %≥x≥16.8 wt %, 20.0 wt %≥x≥18.1 wt %, 21.6 wt %≥x≥20.0 wt %, and 24.2 wt %≥x≥21.6 wt %. Table 3-10 shows (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) for each concentration range, determined by the approximate expression of x when R32=x wt %.









TABLE 3-10







Posnt C











Item
14.1 ≥ x ≥ 10.8
16.1 ≥ x ≥ 14.1
16.8 ≥ x ≥ 16.1
18.1 ≥ x ≥ 16.8




















R32
10.8
12.4
14.1
14.1
14.8
16.1
16.1
16.8
16.8
18.1


R125
34.0
30.6
27.5
27.5
26.3
24.2
24.2
23.1
23.1
21.3


1234yf
38.8
33.0
27.5
27.5
25.3
21.7
21.7
19.7
19.7
16.4


R134a
16.4
24.0
30.9
30.9
33.6
38.0
38.0
40.4
40.4
44.2











R32
x
x
x
X


R125
0.0914x2 − 4.2444x + 69.184
0.0495x2 − 3.1434x + 61.991
−1.5714x + 49.5 
−1.3846x + 46.362


approximate


expression


1234yf
0.1181x2 − 6.3648x + 93.765
0.1723x2 − 8.1236x + 107.78
−2.8043x + 66.812
−2.5156x + 61.961


approximate


expression


R134a
100-R32-R125-1234yf
100-R32-R125-1234yf
100-R32-R125-1234yf
100-R32-R125-1234yf


approximate


expression










Point C










item
20 ≥ x ≥ 18.1
21.6 ≥ x ≥ 20
24.2 ≥ x ≥ 21.6


















R32
18.1
18.7
20.0
20.0
21.6
21.6
22.6
24.2


R125
21.3
20.5
18.8
18.8
16.8
16.8
15.6
13.9


1234yf
16.4
15.0
11.8
11.8
8.0
8.0
5.8
2.5


R134a
44.2
45.8
49.4
49.4
53.6
53.6
56.0
59.4










R32
x
x
x


R125
−1.3145x + 45.088
 −1.25x + 43.8
0.0529x2 − 3.5375x + 68.536


approximate


expression


1234yf
−2.4404x + 60.615
−2.375x + 59.3
0.0431x2 − 4.1038x + 76.546


approximate


expression


R134a
100-R32-1234yf-R134a
100-R32-1234yf-R134a
100-R32-1234yf-R134a


approximate


expression










(2-3) Point E


For point E, the same calculations as those of point A were performed for the following ranges: 14.1 wt %≥x≥10.8 wt %, 16.1 wt %≥x≥14.1 wt %, 16.8 wt %≥x≥16.1 wt %, 18.1 wt %≥x≥16.8 wt %, 20.0 wt %≥x≥18.1 wt %, 21.6 wt %≥x≥20.0 wt, and 24.2 wt %≥x≥21.6 wt %. Table 3-11 shows (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) for each concentration range, determined by the approximate expression of x when R32=x wt %.









TABLE 3-11







Point E











Item
14.1 ≥ x ≥ 10.8
16.1 ≥ x ≥14.1
16.8 ≥ x ≥ 16.1
18.1 ≥ x ≥ 16.8




















R32
10.8
12.4
14.1
14.1
14.8
16.1
16.1
16.8
16.8
18.1


R125
24.9
20.4
15.9
15.9
14.6
12.9
12.9
12.1
12.1
10.7


1234yf
43.1
44.5
45.7
45.7
40.8
33.4
33.4
29.7
29.7
23.2


R134a
21.2
22.7
24.3
24.3
29.8
37.6
37.6
41.4
41.4
48.0











R32
x
x
x
x


R125
0.0501x2 − 3.9756x + 61.989
0.2747x2 − 9.7967x + 99.415
−1.1429x + 31.3 
−1.0769x + 30.192


approximate


expression


1234yf
−0.0296x2 + 1.5133x + 30.248
0.6366x2 − 25.375x + 276.93
−5.3142x + 118.96
−4.9692x + 113.16


approximate


expression


R134a
100-R32-R125-1234yf
100-R32-R125-1234yf
100-R32-R125-1234yf
100-R32-R125-1234yf


approximate


expression










Point E










Item
20 ≥ x ≥ 18.1
21.6 ≥ x ≥ 20
24.2 ≥ x ≥ 21.6


















R32
18.1
18.7
20.0
20.0
21.6
21.6
22.6
24.2


R125
10.7
10.1
9.0
9.0
7.8
7.8
7.2
6.2


1234yf
23.2
20.5
15.0
15.0
8.8
8.8
5.3
0.0


R134a
48.0
50.7
56.0
56.0
61.8
61.8
64.9
69.6










R32
x
x
x


R125
−0.8869x + 26.726
−0.75x + 24  
−0.6163x + 21.118


approximate


expression


1234yf
−4.3267x + 101.52
−3.8831x + 92.657
0.0663x2 − 6.4133x + 116.38


approximate


expression


R134a
100-R32-1234yf-R134a
100-R32-1234yf-R134a
100-R32-1234yf-R134a


approximate


expression










(2-4) Point F


For point F, the same calculations as those of point A were performed for the following ranges: 14.1 wt %≥x≥10.8 wt %, 16.1 wt %≥x≥14.1 wt %, 16.8 wt %≥x≥16.1 wt %, 18.1 wt %≥x≥16.8 wt %, 20.0 wt %≥x≥18.1 wt, 21.6 wt %≥x≥20.0 wt %, and 24.2 wt %≥x≥21.6 wt %. Table 3-12 shows (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) for each concentration range, determined by the approximate expression of x when R32=x wt %.









TABLE 3-12







Point F











Item
14.1 ≥ x ≥ 10.8
16.1 ≥ x ≥ 14.1
16.8 ≥ x ≥ 16.1
18.1 ≥ x ≥ 16.8




















R32
10.8
12.4
14.1
14.1
14.8
16.1
16.1
16.8
16.8
18.1


R125
26.9
24.0
21.1
21.1
20.1
18.1
18.1
17.2
17.2
15.4


1234yf
28.5
23.4
18.2
18.2
16.4
12.9
12.9
11.2
11.2
7.9


R134a
33.8
40.2
46.6
46.6
48.7
52.9
52.9
54.8
54.8
58.6











R32
x
x
x
x


R125
0.0323x2 − 2.5621 x + 50.802
−1.5049x + 42.339
−1.2857x + 38.8
−1.3846x + 40.462


approximate


expression


1234yf
0.0346x2 − 3.9904x + 67.56
−2.6349x + 55.315
−2.4954x + 53.076
−2.5401x + 53.827


approximate


expression


R134a
100-R32-R125-1234yf
100-R32-R125-1234yf
100-R32-R125-1234yf
100-R32-R125-1234yf


approximate


expression










Point F










Item
20 ≥ x ≥ 18.1
21.6 ≥ x ≥ 20
24.2 ≥ x ≥ 21.6


















R32
18.1
18.7
20.0
20.0
21.6
21.6
22.6
24.2


R125
15.4
14.7
13.1
13.1
11.3
11.3
9.4
6.2


1234yf
7.9
6.6
3.5
3.5
0.0
0.0
0.0
0.0


R134a
58.6
60.0
63.4
63.4
67.1
67.1
68.0
69.6










R32
x
x
x


R125
−1.2138x + 37.381
−1.125x + 35.6
−1.9651x + 53.771


approximate


expression


1234yf
−0.1576x2 + 3.716x − 7.7649
−2.1875x + 47.25
0


approximate


expression


R134a
100-R32-1234yf-R134a
100-R32-1234yf-R134a
100-R32-1234yf-R134a


approximate


expression










(2-5) Point B′


For point B′, the same calculations as those of point A were performed for the following ranges: 14.1 wt %≥x≥10.8 wt %, 14.8 wt %≥x≥14.1 wt %, 16.1 wt %≥x≥14.8 wt %, 18.1 wt %≥x≥16.1 wt %, 20.0 wt %≥x≥18.1 wt %, 22.6 wt %≥x≥20.0 wt %, and 25.1 wt %≥x≥22.6 wt %. Table 3-13 shows (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) for each concentration range, determined by the approximate expression of x when R32=x wt %.









TABLE 3-13







Point B′











Item
14.1 ≥ x ≥ 10.8
14.8 ≥ x ≥ 14.1
16.1 ≥ x ≥ 14.8
18.1 ≥ x ≥ 16.1




















R32
10.8
12.4
14.1
14.1
14.8
14.8
16.1
16.1
16.8
18.1


R125
31.8
27.4
22.9
22.9
21.0
21.0
17.6
17.6
16.6
15.0


1234yf
39.9
41.1
42.3
42.3
42.9
42.9
43.9
43.9
39.6
32.6


R134a
17.5
19.1
20.7
20.7
21.3
21.3
22.4
22.4
27.0
34.3











R32
x
x
x
x


R125
−2.6665x + 62.786
−2.2857x + 56.7  
−1.4615x + 42.854
−2.6456x + 62.484


approximate


expression


1234yf
 0.7204x + 31.027
0.7747x + 30.285
 −5.931x + 142.94
 0.7929x + 29.984


approximate


expression


R134a
100-R32-R125-1234yf
100-R32-R125-1234yf
100-R32-R125-1234yf
100-R32-R125-1234yf


approximate


expression











Point B′












Item
20 ≥ x ≥ 18.1
22.6 ≥ x ≥ 20.0
25.1 ≥ x ≥ 22.6



















R32
18.1
18.7
20.0
20.0
21.6
22.6
22.6
24.2
25.1


R125
15.0
14.3
13.0
13.0
11.7
11.0
11.0
9.9
9.3


1234yf
32.6
29.4
23.3
23.3
16.9
13.0
13.0
7.2
4.3


R134a
34.3
37.6
43.7
43.7
49.8
53.4
53.4
58.7
61.3











R32
x
x
x



R125
−1.0442x + 33.87
−0.7733x + 28.448
−0.6809x + 26.385


approximate


expression


1234yf
0.2539x2 − 14.531x + 212.38
0.0598x2 − 6.503x + 129.46
0.1536x2 − 10.827x + 179.27


approximate


expression


R134a
100-R32-1234yf-R134a
100-R32-1234yf-R134a
100-R32-1234yf-R134a


approximate


expression










(2-6) Point C′


For point C′, the same calculations as those of point A were performed for the following ranges: 14.1 wt %≥x≥10.8 wt %, 14.8 wt %≥x≥14.1 wt %, 16.1 wt %≥x≥14.8 wt %, 18.1 wt %≥x≥16.1 wt %, 20.0 wt %≥x≥18.1 wt %, 22.6 wt. %≥x≥20.0 wt %, and 25.1 wt %≥x≥22.6 wt %. Table 3-14 shows (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) for each concentration range, determined by the approximate expression of x when R32=x wt %.









TABLE 3-14







Point C′











Item
14.1 ≥ x ≥ 10.8
14.8 ≥ x ≥ 14.1
16.1 ≥ x ≥ 14.8
18.1 ≥ x ≥ 16.1




















R32
10.8
12.4
14.1
14.1
14.8
14.8
16.1
16.1
16.8
18.1


R125
32.2
28.9
25.9
25.9
24.7
24.7
22.7
22.7
21.6
19.8


1234yf
36.2
30.5
25.1
25.1
23.1
23.1
19.5
19.5
17.6
14.3


R134a
20.8
28.2
34.9
34.9
37.4
37.4
41.7
41.7
44.0
47.8











R32
x
x
x
x


R125
0.0902x2 − 4.1561x + 66.56
−1.7143x + 50.071
−1.5385x + 47.469
−1.4515x + 46.075


approximate


expression


1234yf
 0.117x2 − 6.2764x + 90.341
−2.8571x + 65.386
−2.7834x + 64.295
−2.5842x + 61.058


approximate


expression


R134a
100-R32-R125-1234yf
100-R32-R125-1234yf
100-R32-R125-1234yf
100-R32-R125-1234yf


approximate


expression










Point C′










Item
20 ≥ x ≥ 18.1
22.6 ≥ x ≥ 20.0
25.1 ≥ x ≥ 22.6



















R32
18.1
18.7
20.0
20.0
21.6
22.6
22.6
24.2
25.1


R125
19.8
19.0
17.3
17.3
15.4
14.3
14.3
12.6
11.1


1234yf
14.3
12.8
9.6
9.6
6.0
3.9
3.9
0.6
0.0


R134a
47.8
49.5
53.1
53.1
57.0
59.2
59.2
62.6
63.8










R32
x
x
x


R125
−1.3145x + 43.588
 −1.157x + 40.426
−0.2417x2 + 10.247x − 93.86


approximate


expression


1234yf
−2.4717x + 59.031
−2.1919x + 53.439
 0.5728x2 − 28.884x + 364.1


approximate


expression


R134a
100-R32-1234yf-R134a
100-R32-1234yf-R134a
100-R32-1234yf-R134a


approximate


expression










(2-7) Point E′


For point E′, the same calculations as those of point A were performed for the following ranges: 14.1 wt %≥x≥10.8 wt %, 14.8 wt %≥x≥14.1 wt %, 16.1 wt %≥x≥14.8 wt %, 18.1 wt %≥x≥16.1 wt %, 20.0 wt %≥x≥18.1 wt %, 22.6 wt %≥x≥20.0 wt %, and 25.1 wt %≥x≥22.6 wt %. Table 3-15 shows (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) for each concentration range, determined by the approximate expression of x when R32=x wt.









TABLE 3-15







Point E′











Item
14.1 ≥ x ≥ 10.8
14.8 ≥ x ≥ 14.1
16.1 ≥ x ≥ 14.8
18.1 ≥ x ≥ 16.1




















R32
10.8
12.4
14.1
14.1
14.8
14.8
16.1
16.1
16.8
18.1


R125
27.2
22.8
18.1
18.1
16.5
16.5
14.4
14.4
13.5
12.1


1234yf
42.0
43.3
44.6
44.6
45.1
45.1
36.8
36.8
32.8
26.3


R134a
20.0
21.5
23.2
23.2
23.6
23.6
32.7
32.7
36.9
43.5











R32
x
x
x
x


R125
−2.7576x + 56.987
−2.2857x + 50.329
−1.6154x + 40.408
0.1044x2 − 4.7203x + 63.337

















approximate












expression











1234yf
 0.784x + 33.578
 0.6717x + 35.158
−6.3915x + 139.69
0.3836x2 − 18.386x + 233.37


approximate

















expression





















R134a
100-R32-R125-1234yf
100-R32-R125-1234yf
100-R32-R125-1234yf
100-R32-R125-1234yf


approximate


expression










Point E′










Item
20 ≥ x ≥ 18.1
22.6 ≥ x ≥ 20.0
25.1 ≥ x ≥ 22.6



















R32
18.1
18.7
20.0
20.0
21.6
22.6
22.6
24.2
25.1


R125
12.1
11.5
10.4
10.4
9.1
8.4
8.4
7.4
7.1


1234yf
26.3
23.5
17.9
17.9
11.4
7.7
7.7
2.4
0.0


R134a
43.5
46.3
51.7
51.7
57.9
61.3
61.3
66.0
67.8










R32
x
x
x


R125
−0.8869x + 28.126
−0.7733x + 25.848
0.1167x2 − 6.085x + 86.332


approximate


expression


1234yf
0.1994x2 − 11.991x + 177.97
0.1578x2 − 10.613x + 167.02
0.2787x2 − 16.413x + 236.4


approximate


expression


R134a
100-R32-1234yf-R134a
100-R32-1234yf-R134a
100-R32-1234yf-R134a


approximate


expression










(2-8) Point F′


For point F′, the same calculations as those of point A were performed for the following ranges: 14.1 wt %≥x≥10.8 wt %, 14.8 wt %≥x≥14.1 wt %, 16.1 wt %≥x≥14.8 wt %, 18.1 wt %≥x≥16.1 wt %, 20.0 wt %≥x≥18.1 wt %, 22.6 wt %≥x≥20.0 wt %, and 25.1 wt %≥x≥22.6 wt %. Table 3-16 shows (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) for each concentration range, determined by the approximate expression of x when R32=x wt %.









TABLE 3-16







Point F′











Item
14.1 ≥ x ≥ 10.8
14.8 ≥ x ≥ 14.1
16.1 ≥ x ≥ 14.8
18.1 ≥ x ≥ 16.1




















R32
10.8
12.4
14.1
14.1
14.8
14.8
16.1
16.1
16.8
18.1


R125
28.7
25.6
22.7
22.7
21.6
21.6
19.6
19.6
18.6
16.9


1234yf
31.1
25.7
20.5
20.5
18.6
18.6
15.0
15.0
13.2
10.1


R134a
29.4
36.3
42.7
42.7
45.0
45.0
49.3
49.3
51.4
54.9











R32
x
x
x
x


R125
0.0702x2 − 3.5658x4 − 59.024
−1.5714x + 44.857
−1.5385x + 44.369
−1.3447x + 41.226


approximate


expression


1234yf
0.0958x2 − 5.5978x4 − 80.381
−2.7143x + 58.771
−2.7889x + 59.876
0.0959x2 − 5.7176x + 82.165


approximate


expression


R134a
100-R32-R125-1234yf
100-R32-R125-1234yf
100-R32-R125-1234yf
100-R32-R125-1234yf


approximate


expression










Point F′










Item
20 ≥ x ≥ 18.1
22.6 ≥ x ≥ 20.0
25.1 ≥ x ≥ 22.6



















R32
18.1
18.7
20.0
20.0
21.6
22.6
22.6
24.2
25.1


R125
16.9
16.1
14.5
14.5
12.7
11.6
11.6
8.5
7.1


1234yf
10.1
8.6
5.5
5.5
2.0
0.0
0.0
0.0
0.0


R134a
54.9
56.6
60.0
60.0
63.7
65.8
65.8
67.3
67.8










R32
x
x
x


R125
−1.258x + 39.651
−1.1163x + 36.822
0.1528x2 − 9.0875x + 138.94


approximate


expression


1234yf
0.0607x2 − 4.7348x + 75.905
0.0721x2 − 5.1875x + 80.404
0


approximate


expression


R134a
100-R32-1234yf-R134a
100-R32-1234yf-R134a
100-R32-1234yf-R134a


approximate


expression










(3) Method for Determining Points J, K, L, M, O, P, Q, R, S, and T


(3-1) Point J


For point J, the same calculations as those of point A were performed for the following ranges: 14.2 wt %≥x≥11.6 wt %, 15.3 wt %≥x≥14.2 wt %, 16.2 wt %≥x≥15.3 wt %, 17.5 wt %≥x≥16.2 wt %, and 19.0 wt %≥x≥17.5 wt %. Table 3-17 shows (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) for each concentration range, determined by the approximate expression of x when R32=x wt %.









TABLE 3-17







Point J










Item
14.2 ≥ x ≥ 11.6
15.3 ≥ x ≥ 14.2
16.2 ≥ x ≥ 15.3

















R32
11.6
14.2
14.2
14.5
15.3
15.3
16.2


R125
34.0
24.7
24.7
23.6
20.9
20.9
17.7


1234yf
38.3
41.5
41.5
41.8
42.7
42.7
43.8


R134a
16.1
19.6
19.6
20.1
21.1
21.1
22.3










R32
x
x
x


R125
−3.5769x + 75.492
−3.4381x + 73.493
−3.5556x + 75.3


approximate


expression


1234yf
 1.2204x + 24.143
 1.1236x + 25.522
  1.2095x + 24.209


approximate


expression


R134a
100-R32-R125-1234yf
100-R32-R125-1234yf
100-R32-R125-1234yf


approximate


expression










Point J









Item
17.5 ≥ x ≥ 16.2
19.0 ≥ x ≥ 17.5

















R32
16.2
17.0
17.5
17.5
18.0
18.7
19.0


R125
17.7
16.4
15.6
15.6
14.8
13.8
13.4


1234yf
43.8
38.7
35.5
35.5
32.5
28.4
26.7


R134a
22.3
27.9
31.4
31.4
34.7
39.1
40.9









R32
x
x


R125
−1.6163x + 43.882
0.1273x2 − 6.1109x + 83.553


approximate


expression


1234yf
−6.3674x + 146.95
0.1532x2 − 11.484x + 189.57


approximate


expression


R134a
100-R32-R125-1234yf
100-R32-R125-1234yf


approximate


expression










(3-2) Point K


For point K, the same calculations as those of point A were performed for the following ranges: 14.2 wt %≥x≥11.6 wt. %, 15.3 wt %≥x≥14.2 wt %, 16.2 wt %≥x≥15.3 wt %, 17.5 wt %≥x≥16.2 wt %, and 19.0 wt %≥x≥17.5 wt %. Table 3-18 shows (R125 concentration (wt %%)/1234yf concentration (wt %)/134a concentration (wt %)) for each concentration range, determined by the approximate expression of x when R32=x wt %.









TABLE 3-18







Point K










Item
14.2 ≥ x ≥ 11.6
15.3 ≥ x ≥ 14.2
16.2 ≥ x ≥ 15.3

















R32
11.6
14.2
14.2
14.5
15.3
15.3
16.2


R125
34.0
27.8
27.8
26.9
25.3
25.3
23.5


1234yf
38.3
27.9
27.9
26.5
23.7
23.7
20.6


R134a
16.1
30.1
30.1
32.1
35.7
35.7
39.7










R32
x
x
x


R125
−2.3846x + 61.662
0.9091x2 − 29.091x + 257.58
  −2x + 55.9


approximate


expression


1234yf
−4.0172x + 84.9 
0.8579x2 − 29.085x + 267.88
−3.4439x + 76.392


approximate


expression


R134a
100-R32-R125-1234yf
100-R32-R125-1234yf
100-R32-R125-1234yf


approximate


expression










Point K









Item
17.5 ≥ x ≥ 16.2
19.0 ≥ x ≥ 17.5

















R32
16.2
17.0
17.5
17.5
18.0
18.7
19.0


R125
23.5
22.0
21.1
21.1
20.2
19.0
18.5


1234yf
20.6
18.1
16.5
16.5
14.9
12.8
11.9


R134a
39.7
42.9
44.9
44.8
46.9
49.5
50.5









R32
x
x


R125
−1.8488x + 53.445
0.0637x2 − 4.0554x + 72.576


approximate


expression


1234yf
−3.1206x + 71.153
0.2514x2 − 12.247x + 153.88


approximate


expression


R134a
100-R32-R125-1234yf
100-R32-R125-1234yf


approximate


expression










(3-3) Point L


For point L, the same calculations as those of point A were performed for the following ranges: 17.0 wt %≥x≥14.5 wt %, 18.0 wt %≥x≥17.0 wt %, 18.7 wt %≥x≥18.0 wt %, 19.3 wt %≥x≥18.7 wt %, and 20.8 wt %≥x≥19.3 wt %. Table 3-19 shows (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) for each concentration range, determined by the approximate expression of x when R32=x wt %.









TABLE 3-19







Point L










Item
17.0 ≥ x ≥ 14.5
18.0 ≥ x ≥ 17.0
18.7 ≥ x ≥ 18.0



















R32
14.5
15.3
16.2
17.0
17.0
17.5
18.0
18.0
18.7


R125
33.9
31.3
28.3
25.6
25.6
23.9
22.2
22.2
20.0


1234yf
36.7
37.6
38.6
39.5
39.5
40.1
40.8
40.8
41.6


R134a
14.9
15.9
16.9
17.9
17.9
18.5
19.0
19.0
19.7










R32
x
x
x


R125
−3.3215x + 82.089
−3.4x + 83.4  
−3.1429x + 78.771 


approximate


expression


1234yf
 1.1147x + 20.535
1.3x + 17.378
1.1429x + 20.229


approximate


expression


R134a
100-R32-R125-1234yf
100-R32-R125-1234yf
100-R32-R125-1234yf


approximate


expression










Point L









Item
19.3 ≥ x ≥ 18.7
20.8 ≥ x ≥ 19.3
















R32
18.7
19.0
19.3
19.3
20.0
20.8


R125
20.0
19.5
19.0
19.0
18.0
16.9


1234yf
41.6
39.7
37.8
37.8
33.9
29.5


R134a
19.7
21.8
23.9
23.9
28.0
32.8









R32
x
x


R125
−1.6667x + 51.167
−1.3994x + 46.001


approximate


expression


1234yf
−6.2835x + 159.1 
−5.5605x + 145.15


approximate


expression


R134a
100-R32-R125-1234yf
100-R32-R125-1234yf


approximate


expression










(3-4) Point M


For point M, the same calculations as those of point A were performed for the following ranges: 17.0 wt %≥x≥14.5 wt %, 18.0 wt %≥x≥17.0 wt %, 18.7 wt %≥x≥18.0 wt %, 19.3 wt %≥x≥18.7 wt %, and 20.8 wt %≥x≥19.3 wt %. Table 3-20 shows (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) for each concentration range, determined by the approximate expression of x when R32=x wt %.









TABLE 3-20







Point M










Item
17.0 ≥ x ≥ 14.5
18.0 ≥ x ≥ 17.0
18.7 ≥ x ≥ 18.0



















R32
14.5
15.3
16.2
17.0
17.0
17.5
18.0
18.0
18.7


R125
33.9
32.1
30.1
28.3
28.3
27.5
26.6
26.6
25.3


1234yf
36.7
33.6
30.2
27.2
27.2
25.8
24.1
24.1
21.9


R134a
14.9
19.0
23.5
27.5
27.5
29.2
31.3
31.3
34.1










R32
x
x
x


R125
−2.238x + 66.348
−1.7x + 57.217
−1.8571x + 60.029


approximate


expression


1234yf
−3.8006x + 91.779
−0.6939x2 + 21.203x − 132.72
−3.1386x + 80.613


approximate


expression


R134a
100-R32-R125-1234yf
100-R32-R125-1234yf
100-R32-R125-1234yf


approximate


expression










Point M









Item
19.3 ≥ x ≥ 18.7
20.8 ≥ x ≥ 19.3
















R32
18.7
19.0
19.3
19.3
20.0
20.8


R125
25.3
24.7
24.2
24.2
23.0
21.6


1234yf
21.9
21.0
20.0
20.0
17.9
15.5


R134a
34.1
35.3
36.5
36.5
39.1
42.1









R32
x
x


R125
−1.8333x + 59.567
−1.7337x + 57.666


approximate


expression


1234yf
−3.1952x + 81.665
−3.0037x + 77.984


approximate


expression


R134a
100-R32-R125-1234yf
100-R32-R125-1234yf


approximate


expression










(3-5) Point O


For point O, the same calculations as those of point A were performed for the following ranges: 20.0 wt %≥x≥17.5 wt %, 20.8 wt %≥x≥20.0 wt %, 21.2 wt %≥x≥20.8 wt %, and 22.6 wt %≥x≥21.2 wt %. Table 3-21 shows (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) for each concentration range, determined by the approximate expression of x when R32=x wt %.









TABLE 3-21







Point O









Item
20.0 ≥ x ≥ 17.5
20.8 ≥ x ≥ 20.0


















R32
17.5
18.0
18.7
19.0
19.3
20.0
20.0
20.8


R125
33.8
32.2
30.0
29.1
28.1
25.9
25.9
23.1


1234yf
35.1
35.7
36.4
36.8
37.1
37.9
37.9
39.2


R134a
13.6
14.1
14.9
15.1
15.5
16.2
16.2
16.9









R32
x
x


R125
−3.1554x + 89.013
−3.5x + 95.9


approximate


expression


1234yf
 1.1108x + 15.673
1.5661x + 6.5807


approximate


expression


R134a
100-R32-R125-1234yf
100-R32-R125-1234yf


approximate


expression










Point O









Item
21.2 ≥ x ≥ 20.8
22.6 ≥ x ≥ 21.2















R32
20.8
21.2
21.2
21.6
22.6


R125
23.1
22.2
22.2
21.5
20.2


1234yf
39.2
39.3
39.3
36.7
31.8


R134a
16.9
17.3
17.3
20.2
25.4









R32
x
x


R125
−2.25x + 69.9 
0.3214x2 − 15.507x + 206.49


approximate


expression


1234yf
0.3629x + 31.605
1.2477x2 − 60.003x + 750.62


approximate


expression


R134a
100-R32-R125-1234yf
100-R32-R125-1234yf


approximate


expression










(3-6) Point P


For point P, the same calculations as those of point A were performed for the following ranges: 20.0 wt %≥x≥17.5 wt %, 20.8 wt %≥x≥20.0 wt %, 21.2 wt %≥x≥20.8 wt %, and 22.6 wt %≥x≥21.2 wt. Table 3-22 shows (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) for each concentration range, determined by the approximate expression of x when R32=x wt %.









TABLE 3-22







Point P









Item
20.0 ≥ x ≥ 17.5
20.8 ≥ x ≥ 20.0


















R32
17.5
18.0
18.7
19.0
19.3
20.0
20.0
20.8


R125
33.9
32.8
31.4
30.8
30.2
28.9
28.9
27.5


1234yf
35.0
33.2
30.7
29.7
28.7
26.5
26.5
24.1


R134a
13.6
16.0
19.2
20.5
21.8
24.6
24.6
27.6









R32
x
x


R125
0.0698x2 − 4.6141x + 93.254
−1.75x + 63.9


approximate


expression


1234yf
0.1361x2 − 8.5106x + 142.27
−2.9691x + 85.881


approximate


expression


R134a
100-R32-R125-1234yf
100-R32-R125-1234yf


approximate


expression










Point P









Item
21.2 ≥ x ≥ 20.8
22.6 ≥ x ≥ 21.2















R32
20.8
21.2
21.2
21.6
22.6


R125
27.5
26.8
26.8
26.1
24.5


1234yf
24.1
22.9
22.9
21.6
18.7


R134a
27.6
29.1
29.1
30.7
34.2









R32
x
x


R125
−1.75x + 63.9
0.1071x2 − 6.3357x + 112.96


approximate


expression


1234yf
−3.0619x + 87.812
0.25x2 − 13.95x + 206.28


approximate


expression


R134a
100-R32-R125-1234yf
100-R32-R125-1234yf


approximate


expression










(3-7) Point Q


For point Q, the same calculations as those of point A were performed for the following ranges: 20.8 wt %≥x≥17.5 wt %, 23.2 wt %≥x≥20.8 wt %, 23.2 wt %≥x≥20.8 wt %, 25.6 wt %≥x≥23.2 wt %, and 26.6 wt %≥x≥25.6 wt %. Table 3-23 shows (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) for each concentration range, determined by the approximate expression of x when R32=x wt %.









TABLE 3-23







Point Q










Item
20.8 ≥ x ≥ 17.5




















R32
17.5
18.0
18.7
19.0
19.3
20.0
20.8



R125
10.4
11.4
12.8
13.4
14.0
15.4
16.9



1234yf
24.2
25.1
26.2
26.7
27.2
28.3
29.5



R134a
47.9
45.5
42.3
40.9
39.5
36.3
32.8










R32
x



R125
−0.0198x2 + 27.157x − 31.225



approximate



expression



1234yf
−0.0377x2 + 3.0486x − 17.594



approximate



expression



R134a
100-R32-R125-1234yf



approximate



expression











Point Q










Item
23.2 ≥ x ≥ 20.8
25.6 ≥ x ≥ 23.2
26.6 ≥ x ≥ 25.6





















R32
20.8
21.2
21.6
22.6
23.2
23.2
24.7
25.4
25.6
25.6
26.6


R125
16.9
17.7
18.5
20.3
21.3
21.3
24.0
25.2
25.6
25.6
33.8


1234yf
29.5
30.0
30.5
31.7
32.4
32.4
34.2
35.0
35.1
35.1
30.1


R134a
32.8
31.3
29.4
25.4
23.1
23.1
17.1
14.4
13.7
13.7
9.5










R32
x
x
x


R125
−0.0984x2 + 6.1633x − 68.728
−0.0115x2 + 2.3422x − 26.868
8.2x − 184.32


approximate


expression


1234yf
−0.0617x2 + 3.9141x − 25.243
−0.1077x2 + 6.4104x − 58.357
−5x + 163.1 


approximate


expression


R134a
100-R32-R125-1234yf
100-R32-R125-1234yf
100-R32-R125-1234yf


approximate


expression










(3-8) Point R


For point R, the same calculations as those of point A were performed for the following ranges: 20.8 wt %≥x≥17.5 wt %, 23.2 wt %≥x≥20.8 wt %, 23.2 wt %≥x≥20.8 wt %, 25.6 wt %≥x≥23.2 wt %, and 26.6 wt %≥x≥25.6 wt %. Table 3-24 shows (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) for each concentration range, determined by the approximate expression of x when R32=x wt %.









TABLE 3-24







Point R










Item
20.8 ≥ x ≥ 17.5




















R32
17.5
18.0
18.7
19.0
19.3
20.0
20.8



R125
21.4
22.2
23.3
23.7
24.2
25.2
26.3



1234yf
17.0
17.8
19.0
19.5
20.0
21.1
22.4



R134a
44.1
42.0
39.0
37.8
36.5
33.7
30.5










R32
x



R125
−0.0401x2 + 3.0217x − 19.198



approximate



expression



1234yf
−0.0297x2 + 2.7774x − 22.544



approximate



expression



R134a
100-R32-R125-1234yf



approximate



expression











Point R










Item
23.2 ≥ x ≥ 20.8
25.6 ≥ x ≥ 23.2
26.6 ≥ x ≥ 25.6





















R32
20.8
21.2
21.6
22.6
23.2
23.2
24.7
25.4
25.6
25.6
26.6


R125
26.3
26.8
27.4
28.8
29.6
29.6
31.6
32.3
32.5
32.6
33.8


1234yf
22.3
22.9
23.5
25.0
25.8
25.8
27.8
28.6
28.8
28.9
30.1


R134a
30.5
29.1
27.5
23.6
21.4
21.4
15.9
13.7
13.1
12.9
9.5










R32
x
x
x


R125
−0.0031x2 + 1.5234x − 4.0783
−0.1398x2 + 8.0281x − 81.391
1.2x + 1.88


approximate


expression


1234yf
−0.0503x2 + 3.6856x − 32.627
−0.0932x2 + 5.7935x − 58.514
1.246x − 3.0431


approximate


expression


R134a
100-R32-R125-1234yf
100-R32-R125-1234yf
100-R32-R125-1234yf


approximate


expression










(3-9) Point S


For point S, the same calculations as those of point A were performed for the following ranges: 17.0 wt %≥x≥14.2 wt %, 19.0 wt %≥x≥17.0 wt %, 20.8 wt %≥x≥19.0 wt %, 23.2 wt %≥x≥20.8 wt %, and 25.4 wt %≥x≥23.2 wt %. Table 3-25 shows (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) for each concentration range, determined by the approximate expression of x when R32=x wt %.









TABLE 3-25







Point S









Item
17.0 ≥ x ≥ 14.2
19.0 ≥ x ≥ 17.0




















R32
14.2
14.5
15.3
16.2
17.0
17.0
17.5
18.0
18.7
19.0


R125
20.2
20.4
20.9
21.2
21.6
21.6
22.0
22.2
22.4
22.4


1234yf
43.7
43.4
42.7
42.1
41.5
41.5
41.1
40.8
40.4
40.3


R134a
21.9
21.7
21.1
20.5
19.9
19.9
19.4
19.0
18.5
18.3









R32
x
x


R125
100-R32-1234yf-R134a
100-R32-1234yf-R134a


approximate


expression


1234yf
0.0508x2 − 2.3591x + 66.946
0.1108x2 − 4.5904x + 87.503


approximate


expression


R134a
−0.0008x2 − 0.6861x + 31.798
0.0939x2 − 4.1798x + 63.826


approximate


expression










Point S










Item
20.8 ≥ x ≥ 19.0
23.2 ≥ x ≥ 20.8
25.4 ≥ x ≥ 23.2






















R32
19.0
19.3
20.0
20.8
20.8
21.2
21.6
22.6
23.2
23.2
24.7
25.4


R125
22.4
22.5
22.8
23.0
23.1
23.4
23.4
23.8
23.8
23.8
24.8
25.2


1234yf
40.3
40.1
39.6
39.2
39.2
38.6
38.5
37.7
37.4
37.4
35.8
35.0


R134a
18.3
18.1
17.6
17.0
16.9
16.8
16.5
15.9
15.6
15.6
14.7
14.4










R32
x
x
x


R125
100-R32-1234yf-R134a
100-R32-1234yf-R134a
100-R32-1234yf-R134a


approximate


expression


1234yf
0.1263x2 − 5.6749x + 102.56
0.1017x2 − 5.1872x + 102.99
−0.0317x2 + 0.4511x + 43.979


approximate


expression


R134a
−0.029x2 + 0.4298x + 20.594
0.0034x2 − 0.7313x + 30.692
0.075x2 − 4.1913x + 72.494


approximate


expression










(3-10) Point T


For point T, the same calculations as those of point A were performed for the following ranges: 17.0 wt %≥x≥14.2 wt %, 19.0 wt %≥x≥17.0 wt %, 20.8 wt %≥x≥19.0 wt %, 23.2 wt %≥x≥20.8 wt %, and 25.4 wt %≥x≥23.2 wt %. Table 3-26 shows (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) for each concentration range, determined by the approximate expression of x when R32=x wt %.









TABLE 3-26







Point T









Item
17.0 ≥ x ≥ 14.2
19.0 ≥ x ≥17.0




















R32
14.2
14.5
15.3
16.2
17.0
17.0
17.5
18.0
18.7
19.0


R125
27.8
27.9
28.1
28.2
28.3
28.3
28.5
28.7
28.9
28.8


1234yf
27.9
27.8
27.7
27.4
27.2
27.2
27.2
27.1
26.9
26.9


R134a
30.1
29.8
28.9
28.2
27.5
27.5
26.8
26.2
25.5
25.3









R32
x
x


R125
100-R32-1234yf-R134a
100-R32-1234yf-R134a


approximate


expression


1234yf
−0.0415x2 + 1.0547x + 21.254
−0.0766x2 + 2.5779x + 5.5242


approximate


expression


R134a
0.0863x2 − 3.628x + 64.252
 0.2286x2 − 9.3441x + 120.28


approximate


expression










Point T










Item
20.8 ≥ x ≥ 19.0
23.2 ≥ x ≥ 20.8
25.4 ≥ x ≥ 23.2






















R32
19.0
19.3
20.0
20.8
20.8
21.2
21.6
22.6
23.2
23.2
24.7
25.4


R125
28.8
28.8
28.9
29.1
29.1
29.1
29.1
29.3
29.6
29.6
29.8
29.9


1234yf
26.9
26.8
26.5
26.4
26.4
26.3
26.2
26.0
25.8
21.4
20.3
19.6


R134a
25.3
25.1
24.6
23.7
23.7
23.4
23.1
22.1
21.4
25.8
25.2
25.1










R32
x
x
x


R125
100-R32-1234yf-R134a
100-R32-1234yf-R134a
100-R32-1234yf-R134a


approximate


expression


1234yf
0.1451x2 − 6.0744x + 89.981
−0.0318x2 + 1.1657x + 15.869
0.1142x2 − 5.8724x + 100.55


approximate


expression


R134a
−0.2364x2 + 8.5372x − 51.582
−0.123x2 + 4.4541x − 15.735
−0.1186x2 + 4.9464x − 29.535


approximate


expression










(4) Method for Determining Intersections U, V, W, X, Y, Z, and α


(4-1) Intersection U of Line Segment JK and Line Segment ST


In the case of x=R32=14.5 wt %, when y=R125 concentration (wt %) and z=R134a concentration (wt %), line segment JK is represented by z=−4.6376y+151.27, and line segment ST is represented by z=−2.0815y+85.873, as shown in Table 3-27. Intersection U of line segment JK and line segment ST is (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %))=(25.6/32.6/27.3), as shown in Table 3-27, obtained by solving these formulas. Moreover, the approximate expression of intersection U in the range of 15.3 wt %≥x≥14.2 wt % is calculated in the same manner as in point A. Table 3-27 shows intersection U (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) determined by the approximate expression of x when R32=x wt %.









TABLE 3-27







R32 = 14.5% Line segment JK and line segment ST













Item
J
K
S
T







x = R32
14.5
14.5
14.5
14.5



y = R125
23.6
26.9
20.4
27.9



z = 1234yf
41.8
26.5
43.4
27.8



R134a
20.1
32.1
21.7
29.8













Line segment JK
z = −4.6376

y + 151.27




Line segment ST
z = −2.0815

y + 85.873











Intersection U









15.3 ≥ x ≥ 14.2












Item
U = K = T
Intersection U
U = J = S







x = R32
14.2
14.5
15.3



y = R125
27.8
25.6
20.9



z = 1234yf
27.9
32.6
42.7



R134a
30.1
27.3
21.1










R32
x



R125
1.3896 × 2 − 47.266x + 418.78



approximate



expression



1234yf
−2.8422 × 2 + 97.299x − 780.65



approximate



expression



R134a
100 − R32 − R125 − 1234yf



approximate



expression











(4-2) Intersection V of Line Segment LM and Line Segment ST Intersection V when x=R32=17.5 wt % was calculated from the formulas of line segments shown in Table 3-28 in the same manner as for intersection U. Moreover, the approximate expression of intersection V in the range of 18.0 wt %≥x≥17.0 wt % was calculated in the same manner as for point A. Table 3-28 shows intersection V (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) represented by the approximate expression of x when R32=x wt %.









TABLE 3-28







R32 = 17.5% Line segment LM and line segment ST













Item
L
M
S
T







x = R32
17.5
17.5
17.5
17.5



y = R125
23.9
27.5
22.0
28.5



z = 1234yf
40.1
25.8
41.1
27.2



R134a
18.5
29.2
19.4
26.8













Line segment LM
z = −3.9728

y + 135.08




Line segment ST
z = −2.1399

y + 88.187











Intersection V









18.0 ≥ x ≥ 17.0












Item
V = M = T
Intersection V
V = L = S







x = R32
17.0
17.5
18.0



y = R125
28.3
25.6
22.2



z = 1234yf
27.2
33.4
40.8



R134a
27.5
23.5
19.0










R32
x



R125
−1.3362 × 2 + 40.667x − 276.87



approximate



expression



1234yf
2.2412 × 2 − 64.842x + 481.81



approximate



expression



R134a
100 − R32 − R125 − 1234yf



approximate



expression











(4-3) Intersection W of Line Segment OP and Line Segment ST


Intersection W when x=R32=20.4 wt % was calculated from the formulas of line segments shown in Table 3-29 in the same manner as for intersection U. Moreover, the approximate expression of intersection W in the range of 20.8 wt %≥x≥20.0 wt % was calculated in the same manner as for point A. Table 3-29 shows intersection W (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) represented by the approximate expression of x when R32=x wt %.









TABLE 3-29







R32 = 20.4% Line segment OP and line segment ST













Item
O
P
S
T







x = R32
20.4
20.4
20.4
20.4



y = R125
24.5
28.2
23.0
29.0



z = 1234yf
38.5
25.3
39.4
26.4



R134a
16.6
26.1
17.3
24.2













Line segment OP
z = −3.5676

y + 125.91




Line segment ST
z = −2.1667

y + 89.233











Intersection W









20.8 ≥ x ≥ 20.0












Item
W = P = T
Intersection W
W = O = S







x = R32
20.0
20.4
20.8



y = R125
28.9
26.2
23.0



z = 1234yf
26.5
32.5
39.2



R134a
24.6
20.9
17.0










R32
x



R125
−1.4439 × 2 + 51.537x − 424.27



approximate



expression



1234yf
2.1733 × 2 − 72.785x + 612.88



approximate



expression



R134a
100 − R32 − R125 − 1234yf



approximate



expression











(4-4) Intersection X of Line Segment JK and Line Segment QR


Intersection X when x=R32=18.0 wt % was calculated from the formulas of line segments shown in Table 3-30 in the same manner as for intersection U. Moreover, the approximate expression of intersection X in the range of 19.0 wt %≥x≥17.5 wt % was calculated in the same manner as for point A. Table 3-30 shows intersection X (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) represented by the approximate expression of x when R32=x wt %.















TABLE 3-30









Item
J
K
Q
R







x = R32
18.0
18.0
18.0
18.0



y = R125
14.8
20.2
11.4
22.1



z = 1234yf
32.5
14.9
25.1
17.6



R134a
34.7
46.9
45.5
42.3













Line segment JK
z = −3.2639

y + 80.806




Line segment QR
z = −0.6949

y + 32.976











Intersection X









19.0 ≥ x ≥ 17.5












Item
X = K = R
Intersection X
X = J = Q







x = R32
17.5
18.0
19.0



y = R125
21.1
18.6
13.4



z = 1234yf
16.5
20.0
26.7



R134a
44.9
43.4
40.9










R32
x



R125
−0.1696 × 2 + 1.0575x + 54.537



approximate



expression



1234yf
−0.2271 × 2 + 15.05x − 177.28



approximate



expression



R134a
100 − R32 − R125 − 1234yf



approximate



expression











(4-5) Intersection Y of Line Segment LM and Line Segment QR


Intersection Y when x=R32=20.0 wt % was calculated from the formulas of line segments shown in Table 3-31 in the same manner as for intersection U. Moreover, the approximate expression of intersection Y in the range of 20.8 wt %≥x≥19.3 wt % was calculated in the same manner as for point A. Table 3-31 shows intersection Y (R125 concentration (wt %)/1234yf concentration (wt %%)/134a concentration (wt %)) represented by the approximate expression of x when R32=x wt %.









TABLE 3-31







R32 = 20.0% Line segment LM and line segment QR













Item
L
M
Q
R







x = R32
20.0
20.0
20.0
20.0



y = R125
18.0
23.0
15.4
25.2



z = 1234yf
33.9
17.9
28.3
21.1



R134a
28.1
39.1
36.3
33.7













Line segment LM
z = −3.195

y + 91.409




Line segment QR
z = −0.7337

y + 39.621











Intersection Y









20.8 ≥ x ≥ 19.3












Item
Y = M = R
Intersection Y
Y = L = Q







x = R32
19.3
20.0
20.8



y = R125
24.2
21.0
16.9



z = 1234yf
20.0
24.2
29.5



R134a
36.5
34.8
32.8










R32
x



R125
−0.4421 × 2 + 12.862x − 59.353



approximate



expression



1234yf
0.4405 × 2 − 11.34x + 74.783



approximate



expression



R134a
100 − R32 − R125 − 1234yf



approximate



expression











(4-6) Intersection Z of Line Segment OP and Line Segment QR


Intersection Z when x=R32=21.6 wt % was calculated from the formulas of line segments shown in Table 3-32 in the same manner as for intersection U. Moreover, the approximate expression of intersection Z in the range of 22.6 wt %≥x≥21.2 wt % was calculated in the same manner as for point A. Table 3-32 shows intersection Z (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) represented by the approximate expression of x when R32=x wt %.









TABLE 3-32







R32 = 21.6% Line segment OP and line segment QR













Item
O
P
Q
R







x = R32
21.6
21.6
21.6
21.6



y = R125
21.5
26.1
18.5
27.4



z = 1234yf
36.7
21.6
30.5
23.5



R134a
20.2
30.7
29.4
27.5













Line segment OP
z = −3.2736

y + 107.04




Line segment QR
z = −0.792

y + 45.201











Intersection Z









22.6 ≥ x ≥ 21.2












Item
Z = P = R
Intersection Z
Z = O = Q







x = R32
21.2
21.6
22.6



y = R125
26.8
24.9
20.2



z = 1234yf
22.9
25.5
31.8



R134a
29.1
28.0
25.4










R32
x



R125
−0.0118 × 2 − 4.1976x + 121.09



approximate



expression



1234yf
−0.0544 × 2 + 8.7425x − 137.98



approximate



expression



R134a
100 − R32 − R125 − 1234yf



approximate



expression











(4-7) Intersection a of Line Segment ST and Line Segment QR


Intersection a when x=R32=21.6 wt % was calculated from the formulas of line segments shown in Table 3-33 in the same manner as for intersection U. Moreover, the approximate expression of intersection a in the range of 25.4 wt %≥x≥23.2 wt % was calculated in the same manner as for point A. Table 3-33 shows intersection a (R125 concentration (wt %)/1234yf concentration (wt %)/134a concentration (wt %)) represented by the approximate expression of x when R32=x wt %.















TABLE 3-33









Item
S
T
Q
R







x = R32
24.7
24.7
24.7
24.7



y = R125
24.0
31.6
24.8
29.8



z = 1234yf
34.2
27.8
35.8
25.2



R134a
17.1
15.9
14.7
20.3













Line segment ST
z = −0.8459

y + 54.53




Line segment QR
z = −2.1205

y + 88.391











Intersection α









25.4 ≥ x ≥ 23.2












Item
α = T = R
Intersection α
α = S = Q







x = R32
23.2
24.7
25.4



y = R125
29.6
26.6
25.2



z = 1234yf
25.8
32.1
35.0



R134a
21.4
16.6
14.4










R32
x



R125
0.0324 × 2 − 3.5746x + 95.092



approximate



expression



1234yf
0.0193 × 2 + 3.2487x − 59.944



approximate



expression



R134a
100 − R32 − R125 − 1234yf



approximate



expression










The mixture (at least one of the mixtures described above) contained in the composition of the first embodiment of the present invention may further contain water as another component, in addition to the four basic components (R32, R125, R134a, and 1234yf).


The concentration of water contained in the mixture is preferably 200 weight ppm or less based on the 1234yf content of the mixture. The lower limit of the water concentration based on the 1234yf content of the mixture is not particularly limited, as long as the effect of improving the stability of the composition is exhibited. For example, the lower limit of the water concentration can be 0.1 weight ppm.


The presence of water in the mixture results in an unexpected effect such that the chemical stability of the composition comprising the mixture increases. The reason for this is considered as follows. Specifically, because the mixture contains water, the double bonds in the molecules of the unsaturated fluorinated hydrocarbons contained in the composition can be stably present, and oxidation of the unsaturated fluorinated hydrocarbons is less likely to occur, consequently improving the stability of the composition.


The mixture contained in the composition of the first embodiment of the present invention may contain other component(s) (fluorinated hydrocarbon(s) that are different from the four basic components) in addition to the four basic components (R32, R125, R134a, and 1234yf). The fluorinated hydrocarbon(s) as other component(s) are not particularly limited, and are, for example, at least one fluorinated hydrocarbon selected from the group consisting of HCFC-1122, HCFC-124, CFC-1113, and 3,3,3-trifluoropropyne.


The mixture contained in the composition of the first embodiment of the present invention may contain, in addition to the four basic components (R32, R125, R134a, and 1234yf), at least one halogenated organic compound represented by formula (1): CmHnXp, wherein each X independently represents a fluorine atom, a chlorine atom, or a bromine atom, m is 1 or 2, 2m+2≥n+p, and p≥1, as other component(s). The at least one halogenated organic compound as other component(s) is not particularly limited. Preferable examples include difluorochloromethane, chloromethane, 2-chloro-1,1,1,2,2-pentafluoroethane, 2-chloro-1,1,1,2-tetrafluoroethane, 2-chloro-1,1-difluoroethylene, trifluoroethylene, and the like.


The mixture contained in the composition of the first embodiment of the present invention may contain, in addition to the four basic components (R32, R125, R134a, and 1234yf), at least one organic compound represented by formula (2): CmHnXp, wherein each X independently represents an atom that is not a halogen atom, m is 1 or 2, 2m+2≥n+p, and p≥1, as other component(s). The at least one organic compound as other component(s) is not particularly limited. Preferable examples include propane, isobutane, and the like.


As described above, when the mixture contains other components, the content of other components in the mixture, whether other components are used singly or in a combination of two or more, is preferably 0.5 wt % or less, more preferably 0.3 wt % or less, and even more preferably 0.1 wt % or less, as the total content amount.


Second Embodiment to Fourth Embodiment

The composition of the second embodiment of the present invention is a composition comprising a mixture of fluorinated hydrocarbons, wherein the mixture comprises R32, R125, R134a, 1234yf, and at least one fluorinated hydrocarbon selected from the group consisting of HCFC-1122, HCFC-124, CFC-1113, and 3,3,3-trifluoropropyne. That is, in addition to the four basic components (R32, R125, R134a, and 1234yf), at least one member selected from the group consisting of HCFC-1122, HCFC-124, CFC-1113, and 3,3,3-trifluoropropyne is contained as other component(s) (fluorinated hydrocarbon(s) that are different from the four basic components).


Moreover, the composition of the third embodiment of the present invention is a composition comprising a mixture of fluorinated hydrocarbons, wherein the mixture comprises R32, R125, R134a, 1234yf, and at least one halogenated organic compound represented by formula (1): CmHnXp, wherein each X independently represents a fluorine atom, a chlorine atom, or a bromine atom, m is 1 or 2, 2m+2≥n+p, and p≥1. That is, in addition to the four basic components (R32, R125, R134a, and 1234yf), at least one halogenated organic compound represented by formula (1) is contained as other component(s).


Furthermore, the composition of the fourth embodiment of the present invention is a composition comprising a mixture of fluorinated hydrocarbons, wherein the mixture comprises R32, R125, R134a, 1234yf, and at least one organic compound represented by formula (2): CmHnXp, wherein each X independently represents an atom that is not a halogen atom, m is 1 or 2, 2m+2≥n+p, and p≥1. That is, in addition to the four basic components (R32 R125, R134a, and 1234yf), at least one organic compound represented by formula (2) is contained as other component(s).


The compositions of the second to fourth embodiments of the present invention can be the same as the composition of the first embodiment of the present invention, except that the composition ratio of R32, R125, R134a, and 1234yf contained in the mixture is not particularly limited. In the compositions of the second to fourth embodiments of the present invention, the content of other components in the mixture is preferably 0.5 wt % or less, more preferably 0.3 wt % or less, and particularly preferably 0.1 wt % or less, as in the first embodiment.


Fifth Embodiment

The composition of the fifth embodiment of the present invention is a composition comprising a mixture of fluorinated hydrocarbons, wherein the mixture comprises difluoromethane (R32), pentafluoroethane (R125), 1,1,1,2-tetrafluoroethane (R134a), 2,3,3,3-tetrafluoropropene (1234yf), and water. That is, in addition to the four basic components (R32 R125, R134a, and 1234yf), water is contained as another component. In the composition of the fifth embodiment of the present invention, the content of water as another component in the mixture is preferably 0.5 wt % or less, more preferably 0.3 wt % or less, and particularly preferably 0.1 wt % or less, as in the first embodiment.


The composition ratio of R32, R125, R134a, and 1234yf contained in the mixture contained in the composition of the fifth embodiment of the present invention is not particularly limited.


The concentration of water contained in the mixture is preferably 200 weight ppm or less based on the 1234yf content of the mixture. The lower limit of the water concentration based on the 1234yf content of the mixture is not particularly limited, as long as the effect of improving the stability of the composition is exhibited. For example, the lower limit of the water concentration can be 0.1 weight ppm.


The presence of water in the mixture results in an unexpected effect such that the chemical stability of the composition comprising the mixture increases. The reason for this is considered as follows. That is, because the mixture contains water, the double bonds in the molecules of the unsaturated fluorinated hydrocarbons contained in the composition can be stably present, and oxidation of the unsaturated fluorinated hydrocarbons is less likely to occur, consequently improving the stability of the composition.


The composition of the fifth embodiment of the present invention can be the same as the composition of the first embodiment of the present invention, except that the composition ratio of R32, R125, R134a, and 1234yf contained in the mixture is not particularly limited.


Optional Additives


The compositions of the first to fifth embodiments of the present invention may appropriately contain various additives in addition to the mixture of fluorinated hydrocarbons.


The compositions of the present invention may further contain a refrigerant oil. The refrigerant oil is not particularly limited and can be suitably selected from commonly used refrigerant oils. In this case, a refrigerant oil that is more excellent in terms of, for example, the effect of improving miscibility with the mixture, stability of the mixture, etc., may be appropriately selected, if necessary.


Although there is no particular limitation, the stability of the mixture can be evaluated by a commonly used method. Examples of such methods include an evaluation method using the amount of free fluorine ions as an index according to ASHRAE Standard 97-2007, and the like. There is, for example, another evaluation method using the total acid number as an index. This method can be performed, for example, according to ASTM D 974-06.


Preferred as the type of the refrigerant oil is, specifically, for example, at least one member selected from the group consisting of polyalkylene glycol (PAG), polyol ester (POE), and polyvinyl ether (PVE).


The refrigerant oil to be used may have, for example, a kinematic viscosity at 40° C. of 5 to 400 cSt. When the refrigerant oil has a kinematic viscosity within this range, it is preferable in terms of lubricity.


The concentration of the refrigerant oil is not particularly limited, and may be generally 10 to 50 wt %, relative to the entire composition.


The compositions of the first to fifth embodiments of the present invention may further contain one or more tracers. The one or more tracers are added to the compositions of the present invention at a detectable concentration so that, when the compositions of the present invention are diluted, contaminated, or undergo any other change, the change can be traced. There is no limitation on the tracers. Preferable examples include hydrofluorocarbons, deuterated hydrocarbons, deuterated hydrofluorocarbons, perfluorocarbons, fluoroethers, brominated compounds, iodinated compounds, alcohols, aldehydes, ketones, nitrous oxide (N2O), and the like. Particularly preferred are hydrofluorocarbons or fluoroethers.


The compositions of the first to fifth embodiments of the present invention may further contain a compatibilizer. The type of compatibilizer is not particularly limited. Preferable examples include polyoxyalkylene glycol ethers, amides, nitriles, ketones, chlorocarbons, esters, lactones, aryl ethers, fluoroethers, 1,1,1-trifluoroalkans, and the like. Particularly preferred are polyoxyalkylene glycol ethers.


The compositions of the first to fifth embodiments of the present invention may further contain one or more ultraviolet fluorescent dyes. There is no limitation on the ultraviolet fluorescent dyes. Preferable examples include naphthalimide, coumarin, anthracene, phenanthrene, xanthene, thioxanthene, naphthoxanthene, fluorescein, and derivatives thereof. Either naphthalimide or coumarin, or both, are particularly preferable.


The compositions of the first to fifth embodiments of the present invention may further contain a stabilizer, a polymerization inhibitor, etc., if necessary.


Examples of stabilizers include, but are not particularly limited to, (i) aliphatic nitro compounds, such as nitromethane and nitroethane; and aromatic nitro compounds, such as nitrobenzene and nitrostyrene; (ii) ethers, such as 1,4-dioxane; amines, such as 2,2,3,3,3-pentafluoropropylamine and diphenylamine; butylhydroxyxylene, benzotriazole, and the like. The stabilizers can be used singly or in a combination of two or more.


The concentration of the stabilizer varies depending on the type of stabilizer, but can be determined within a range in which the properties of the composition are not impaired. The concentration of the stabilizer is generally preferably about 0.01 to 5 parts by weight, and more preferably about 0.05 to 2 parts by weight, per 100 parts by weight of the mixture.


Examples of polymerization inhibitors include, but are not particularly limited to, 4-methoxy-1-naphthol, hydroquinone, hydroquinonemethyl ether, dimethyl-t-butylphenol, 2,6-di-tert-butyl-p-cresol, benzotriazole, and the like.


The concentration of the polymerization inhibitor is generally preferably 0.01 to 5 parts by weight, and more preferably about 0.05 to 2 parts by weight, per 100 parts by weight of the mixture.


An object can be refrigerated by a method comprising the step of operating a refrigeration cycle using the compositions of the first to fifth embodiments of the present invention. For example, the composition can be circulated via a compressor to form the refrigeration cycle.


It is also possible to obtain a device for forming a refrigeration cycle in which each of the above compositions is circulated via a compressor. In a refrigeration method using such a device, because the composition ratio of R32, R125, R134a, and 1234yf contained in the mixture is the above specific composition ratio, the outlet temperature of the compressor can, for example, be set to 110° C. or less. Because the outlet temperature of the compressor is set within this range, when the composition comprises a refrigerant oil, the deterioration of the refrigerant oil can be suppressed.


Examples of refrigerating devices that can use the compositions of the first to fifth embodiments of the present invention include, but are not limited to, refrigerators, freezers, water coolers, ice machines, refrigerating showcases, freezing showcases, freezing and refrigerating units, refrigerating devices used, for example, for freezing and refrigerating warehouses, chillers (chilling units), turbo refrigerators, screw refrigerators, and the like.


EXAMPLES

The present invention is described in detail below with reference to Examples and Comparative Examples. However, the present invention is not limited to the Examples.


Examples 1-1 to 3-139 and Comparative Examples 1-1 to 3-115

The GWP of each of R404A and compositions comprising a mixture of R32, R125, R134a, and 1234yf was evaluated based on the values described in the Fourth Assessment Report of the Intergovernmental Panel on Climate Change (IPCC). The refrigerating capacity of each of R404A and the compositions comprising a mixture of R32, R125, R134a, and 1234yf was determined by performing refrigeration cycle theoretical 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.


Evaporation temperature −40° C.


Condensation temperature 40° C.


Superheating temperature 20 K


Supercooling temperature 0 K


Compressor efficiency 70%


The flammability was determined based on the ASHRAE flammability classification.


Further, Tables 4-1 to 6-21 show the GWP, COP, compressor outlet pressure, compressor outlet temperature, and refrigerating capacity calculated based on these results. Table 5 shows the COP, refrigerating capacity, and compressor outlet pressure each relative to those of R22, and Table 6 shows the COP and refrigerating capacity each relative to those of R404A.


The coefficient of performance (COP) was calculated according to the following equation.

COP=(refrigerating capacity or heating capacity)/amount of electrical power consumed


In FIGS. 15 to 27, 30, 31, 33, 36, 44, and 45, open circles (◯) represent the compositions of the Examples other than the reference signs, and open triangles (Δ) represent the compositions of the Comparative Examples other than the reference signs.



















TABLE 4-1







Compar-












ative
Exam-
Exam-
Exam-
Exam-
Exam-
Exam-
Exam-
Exam-




Example
ple
ple
ple
ple
ple
ple
ple
ple




1-1
1-1
1-2
1-3
1-4
1-5
1-6
1-7
1-8


Item
Unit
A
D
G
H
I
G′
H′
I′
N


























Compo-
R32
mass %
10.8
10.8
10.8
10.8
10.8
10.8
10.8
10.8
10.8


sition
R125
mass %
40.7
7.3
34.5
11.6
0.0
34.0
12.6
0.0
0.0



1234yf
mass %
48.5
0.0
39.4
50.3
22.5
38.8
49.0
18.7
0.0



R134a
mass %
0.0
81.9
15.3
27.3
66.7
16.4
27.6
70.5
89.2

















GWP
Year
1500
1500
1500
871
1028
1500
911
1082
1348


ASHRAE

Flam-
Non-
Non-
Non-
Non-
Non-
Non-
Non-
Non-


non-flammability

mable
flam-
flam-
flam-
flam-
flam-
flam-
flam-
flam-





mable
mable
mable
mable
mable
mable
mable
mable


























TABLE 4-2







Compar-












ative
Exam-
Exam-
Exam-
Exam-
Exam-
Exam-
Exam-
Exam-




Example
ple
ple
ple
ple
ple
ple
ple
ple




1-2
1-9
1-10
1-11
1-12
1-13
1-14
1-15
1-16


Item
Unit
A
D
G
H
I
G′
H′
I′
N


























Compo-
R32
mass %
12.4
12.4
12.4
12.4
12.4
12.4
12.4
12.4
12.4


sition
R125
mass %
40.4
7.9
34.5
13.1
0.0
34.0
14.1
0.0
0.0



1234yf
mass %
47.2
0.0
38.5
48.8
18.1
37.9
47.5
14.3
0.0



R134a
mass %
0.0
79.7
14.6
25.7
69.5
15.7
26.0
73.3
87.6

















GWP
Year
1500
1500
1500
912
1078
1500
951
1132
1336


ASHRAE

Flam-
Non-
Non-
Non-
Non-
Non-
Non-
Non-
Non-


non-flammability

mable
flam-
flam-
flam-
flam-
flam-
flam-
flam-
flam-





mable
mable
mable
mable
mable
mable
mable
mable


























TABLE 4-3







Compar-












ative
Exam-
Exam-
Exam-
Exam-
Exam-
Exam-
Exam-
Exam-




Example
ple
ple
ple
ple
ple
ple
ple
ple




1-3
1-17
1-18
1-19
1-20
1-21
1-22
1-23
1-24


Item
Unit
A
D
G
H
I
G′
H′
I′
N


























Compo-
R32
mass %
14.8
14.8
14.8
14.8
14.8
14.8
14.8
14.8
14.8


sition
R125
mass %
40.0
8.8
34.4
15.4
0.0
34.0
16.5
0.0
0.0



1234yf
mass %
45.2
0.0
37.2
46.5
11.7
36.5
45.1
7.9
0.0



R134a
mass %
0.0
76.4
13.6
23.3
73.5
14.7
23.6
77.3
85.2

















GWP
Year
1500
1500
1500
974
1151
1500
1017
1206
1318


ASHRAE

Flam-
Non-
Non-
Non-
Non-
Non-
Non-
Non-
Non-


non-flammability

mable
flam-
flam-
flam-
flam-
flam-
flam-
flam-
flam-





mable
mable
mable
mable
mable
mable
mable
mable


























TABLE 4-4







Compar-












ative
Exam-
Exam-
Exam-
Exam-
Exam-
Exam-
Exam-
Exam-




Example
ple
ple
ple
ple
ple
ple
ple
ple




1-4
1-25
1-26
1-27
1-28
1-29
1-30
1-31
1-32


Item
Unit
A
D
G
H
I
G′
H′
I′
N


























Compo-
R32
mass %
16.1
16.1
16.1
16.1
16.1
16.1
16.1
16.1
16.1


sition
R125
mass %
39.7
9.3
34.4
16.5
0.0
33.9
17.6
0.0
0.0



1234yf
mass %
44.2
0.0
36.4
45.3
8.6
35.8
43.9
4.8
0.0



R134a
mass %
0.0
74.6
13.1
22.1
75.3
14.2
22.4
79.1
83.9

















GWP
Year
1500
1500
1500
1004
1186
1500
1047
1240
1308


ASHRAE

Flam-
Non-
Non-
Non-
Non-
Non-
Non-
Non-
Non-


non-flammability

mable
flam-
flam-
flam-
flam-
flam-
flam-
flam-
flam-





mable
mable
mable
mable
mable
mable
mable
mable

























TABLE 4-5







Compar-











ative
Exam-
Exam-
Exam-
Exam-
Exam-
Exam-
Exam-




Example
ple
ple
ple
ple
ple
ple
ple




1-5
1-33
1-34
1-35
1-36
1-37
1-38
1-39


Item
Unit
A
D
G
H
I
G′
H′
I′ = N

























Compo-
R32
mass %
18.1
18.1
18.1
18.1
18.1
18.1
18.1
18.1


sition
R125
mass %
39.3
10.0
34.3
18.3
0.0
33.9
19.4
0.0



1234yf
mass %
42.6
0.0
35.3
43.5
3.9
34.7
42.1
0.0



R134a
mass %
0.0
71.9
12.3
20.1
78.0
13.3
20.4
81.9
















GWP
Year
1500
1500
1500
1052
1238
1500
1095
1293


ASHRAE

Flam-
Non-
Non-
Non-
Non-
Non-
Non-
Non-


non-flammability

mable
flam-
flam-
flam-
flam-
flam-
flam-
flam-





mable
mable
mable
mable
mable
mable
mable


























TABLE 4-6







Compar-












ative
Exam-
Exam-
Exam-
Exam-
Exam-
Exam-
Exam-
Exam-




Example
ple
ple
ple
ple
ple
ple
ple
ple




1-6
1-40
1-41
1-42
1-43
1-44
1-45
1-46
1-47


Item
Unit
A
D
G
H
I
G′
H′
I′
N


























Compo-
R32
mass %
19.0
19.0
19.0
19.0
19.0
19.0
19.0
19.0
19.0


sition
R125
mass %
39.1
10.3
34.3
19.2
0.0
33.8
20.3
0.8
0.0



1234yf
mass %
41.9
0.0
34.8
42.7
2.0
34.3
41.3
0.0
0.0



R134a
mass %
0.0
70.7
11.9
19.1
79.0
12.9
19.4
80.2
81.0

















GWP
Year
1500
1500
1500
1075
1258
1500
1118
1303
1287


ASHRAE

Flam-
Non-
Non-
Non-
Non-
Non-
Non-
Non-
Non-


non-flammability

mable
flam-
flam-
flam-
flam-
flam-
flam-
flam-
flam-





mable
mable
mable
mable
mable
mable
mable
mable

























TABLE 4-7







Compar-











ative
Exam-
Exam-
Exam-
Exam-
Exam-
Exam-
Exam-




Example
ple
ple
ple
ple
ple
ple
ple




1-7
1-48
1-49
1-50
1-51
1-52
1-53
1-54


Item
Unit
A
D
G
H
I = N
G′
H′
I′

























Compo-
R32
mass %
20.0
20.0
20.0
20.0
20.0
20.0
20.0
20.0


sition
R125
mass %
38.9
10.7
34.2
20.1
0.0
33.8
21.2
1.8



1234yf
mass %
41.1
0.0
34.3
41.8
0.0
33.7
40.4
0.0



R134a
mass %
0.0
69.3
11.5
18.1
80.0
12.5
18.4
78.2
















GWP
Year
1500
1500
1500
1099
1279
1500
1142
1316


ASHRAE

Flam-
Non-
Non-
Non-
Non-
Non-
Non-
Non-


non-flammability

mable
flam-
flam-
flam-
flam-
flam-
flam-
flam-





mable
mable
mable
mable
mable
mable
mable

























TABLE 4-8







Compar-











ative
Exam-
Exam-
Exam-
Exam-
Exam-
Exam-
Exam-




Example
ple
ple
ple
ple
ple
ple
ple




1-8
1-55
1-56
1-57
1-58
1-59
1-60
1-61


Item
Unit
A
D
G
H
I
G′
H′
I′

























Compo-
R32
mass %
21.6
21.6
21.6
21.6
21.6
21.6
21.6
21.6


sition
R125
mass %
38.6
11.2
34.2
21.4
1.7
33.8
22.5
3.5



1234yf
mass %
39.8
0.0
33.4
40.3
0.0
32.9
38.9
0.0



R134a
mass %
0.0
67.2
10.8
16.7
76.7
11.7
17.0
74.9
















GWP
Year
1500
1500
1500
1135
1302
1500
1178
1339


ASHRAE

Flam-
Non-
Non-
Non-
Non-
Non-
Non-
Non-


non-flammability

mable
flam-
flam-
flam-
flam-
flam-
flam-
flam-





mable
mable
mable
mable
mable
mable
mable

























TABLE 4-9







Compar-











ative
Exam-
Exam-
Exam-
Exam-
Exam-
Exam-
Exam-




Example
ple
ple
ple
ple
ple
ple
ple




1-9
1-62
1-63
1-64
1-65
1-66
1-67
1-68


Item
Unit
A
D
G
H
I
G′
H′
I′

























Compo-
R32
mass %
22.6
22.6
22.6
22.6
22.6
22.6
22.6
22.6


sition
R125
mass %
38.4
11.6
34.2
22.1
2.7
33.8
23.3
4.6



1234yf
mass %
39.0
0.0
32.8
39.4
0.0
32.3
38.0
0.0



R134a
mass %
0.0
65.8
10.4
15.9
74.7
11.3
16.1
72.8
















GWP
Year
1500
1500
1500
1155
1315
1500
1200
1114


ASHRAE

Flam-
Non-
Non-
Non-
Non-
Non-
Non-
Non-


non-flammability

mable
flam-
flam-
flam-
flam-
flam-
flam-
flam-





mable
mable
mable
mable
mable
mable
mable

























TABLE 4-10







Compar-











ative
Exam-
Exam-
Exam-
Exam-
Exam-
Exam-
Exam-




Example
ple
ple
ple
ple
ple
ple
ple




1-10
1-69
1-70
1-71
1-72
1-73
1-74
1-75


Item
Unit
A
D
G
H
I
G′
H′
I′

























Compo-
R32
mass %
23.2
23.2
23.2
23.2
23.2
23.2
23.2
23.2


sition
R125
mass %
38.3
11.8
34.2
22.6
3.3
33.8
23.8
5.2



1234yf
mass %
38.5
0.0
32.5
38.8
0.0
32.0
37.4
0.0



R134a
mass %
0.0
65.0
10.1
15.4
73.5
11.0
15.6
71.6
















GWP
Year
1500
1500
1500
1169
1323
1500
1214
1362


ASHRAE

Flam-
Non-
Non-
Non-
Non-
Non-
Non-
Non-


non-flammability

mable
flam-
flam-
flam-
flam-
flam-
flam-
flam-





mable
mable
mable
mable
mable
mable
mable

























TABLE 4-11







Compar-











ative
Exam-
Exam-
Exam-
Exam-
Exam-
Exam-
Exam-




Example
ple
ple
ple
ple
ple
ple
ple




1-11
1-76
1-77
1-78
1-79
1-80
1-81
1-82


Item
Unit
A
D
G
H
I
G′
H′
I′

























Compo-
R32
mass %
24.5
24.5
24.5
24.5
24.5
24.5
24.5
24.5


sition
R125
mass %
38.1
12.3
34.2
23.6
4.5
33.9
24.8
6.4



1234yf
mass %
37.4
0.0
31.8
37.6
0.0
31.2
36.2
0.0



R134a
mass %
0.0
63.2
9.5
14.3
71.0
10.4
14.5
69.1
















GWP
Year
1500
1500
1500
1197
1338
1500
1242
1378


ASHRAE

Flam-
Non-
Non-
Non-
Non-
Non-
Non-
Non-


non-flammability

mable
flam-
flam-
flam-
flam-
flam-
flam-
flam-





mable
mable
mable
mable
mable
mable
mable

























TABLE 4-12







Compar-











ative
Exam-
Exam-
Exam-
Exam-
Exam-
Exam-
Exam-




Example
ple
ple
ple
ple
ple
ple
ple




1-12
1-83
1-84
1-85
1-86
1-87
1-88
1-89


Item
Unit
A
D
G
H
I
G′
H′
I′

























Compo-
R32
mass %
25.6
25.6
25.6
25.6
25.6
25.6
25.6
25.6


sition
R125
mass %
37.9
12.6
34.2
24.3
5.6
33.9
25.6
7.5



1234yf
mass %
36.5
0.0
31.2
36.6
0.0
30.6
35.1
0.0



R134a
mass %
0.0
61.8
9.0
13.5
68.8
9.9
13.7
66.9
















GWP
Year
1500
1500
1500
1218
1353
1500
1266
1392


ASHRAE

Flam-
Non-
Non-
Non-
Non-
Non-
Non-
Non-


non-flammability

mable
flam-
flam-
flam-
flam-
flam-
flam-
flam-





mable
mable
mable
mable
mable
mable
mable

























TABLE 4-13







Compar-











ative
Exam-
Exam-
Exam-
Exam-
Exam-
Exam-
Exam-




Example
ple
ple
ple
ple
ple
ple
ple




1-13
1-90
1-91
1-92
1-93
1-94
1-95
1-96


Item
Unit
A
D
G
H
I
G′
H′
I′

























Compo-
R32
mass %
26.6
26.6
26.6
26.6
26.6
26.6
26.6
26.6


sition
R125
mass %
37.7
13.0
34.2
25.1
6.6
33.8
26.3
8.6



1234yf
mass %
35.7
0.0
30.6
25.6
0.0
30.1
34.2
0.0



R134a
mass %
0.0
60.4
8.6
12.7
66.8
9.5
12.9
64.8
















GWP
Year
1500
1500
1500
1241
1366
1500
1286
1407


ASHRAE

Flam-
Non-
Non-
Non-
Non-
Non-
Non-
Non-


non-flammability

mable
flam-
flam-
flam-
flam-
flam-
flam-
flam-





mable
mable
mable
mable
mable
mable
mable


























TABLE 5-1










Compar-
Compar-

Compar-
Compar-








ative
ative
Exam-
ative
ative
Exam-
Exam-
Exam-




Compar-
Example
Example
ple
Example
Example
ple
ple
ple




ative
2-1
2-2
2-1
2-3
2-4
2-2
2-3
2-4


Item
Unit
Example
A
D
G′ = B = C
H′
I′
E
F
B′





















Compo-
R32
mass %
R22
10.8
10.8
10.8
10.8
10.8
10.8
10.8
10.8


sition
R125
mass %

40.7
7.3
34.0
12.6
0.0
24.9
26.9
31.8



1234yf
mass %

48.5
0.0
38.8
49.0
18.7
43.1
28.5
39.9



R134a
mass %

0.0
81.9
16.4
27.6
70.5
21.2
33.8
17.5

















GWP
Year
1810
1500
1500
1500
911
1082
1249
1500
1438


















Perfor-
Coefficient of
(relative to
100
89.10
97.20
90.73
93.01
96.60
91.75
92.44
90.98


mance
performance
R22 %)



Refrigerating
(relative to
100
84
64
80
71
64
76
76
79



capacity
R22 %)



Outlet
° C.
149
95
116
99
101
112
100
104
99



temperature



Outlet
(relative to
100
107.1
83.0
102.5
91.2
82.1
97.5
97.5
101.25



pressure
R22 %)


















Exam-
Exam-
Exam-

Compar-



Compar-
ple
ple
ple
Exam-
ative



ative
2-5
2-6
2-7
ple
Example














Item
Unit
Example
C′
E′
F′
2-8
2-5


















Compo-
R32
mass %
R22
10.8
10.8
10.8
10.8
10.8


sition
R125
mass %

32.2
27.2
28.7
30.0
40.0



1234yf
mass %

36.2
42.0
31.1
39.2
29.2



R134a
mass %

20.8
20.0
29.4
20.0
20.0














GWP
Year
1810
1500
1313
1500
1410
1760















Perfor-
Coefficient of
(relative to
100
91.16
91.50
92.01
91.29
90.46


mance
performance
R22 %)



Refrigerating
(relative to
100
79
77
77
78
82



capacity
R22 %)



Outlet
° C.
149
100
100
103
100
101



temperature



Outlet
(relative to
100
101.25
98.75
98.75
100.18
105.5



pressure
R22 %)


























TABLE 5-2










Compar-
Compar-
Compar-
Compar-
Compar-








ative
ative
ative
ative
ative
Exam-
Exam-
Exam-




Compar-
Example
Example
Example
Example
Example
ple
ple
ple




ative
2-6
2-7
2-8
2-9
2-10
2-9
2-10
2-11


Item
Unit
Example
A
D
G′
H′
I′
B
C
E





















Compo-
R32
mass %
R22
12.4
12.4
12.4
12.4
12.4
12.4
12.4
12.4


sition
R125
mass %

40.4
7.9
34.0
14.1
0.0
29.7
30.6
20.4



1234yf
mass %

47.2
0.0
37.9
47.5
14.4
40.0
33.0
44.5



R134a
mass %

0.0
79.7
15.7
26.0
73.2
17.9
24.0
22.7

















GWP
Year
1810
1500
1500
1500
951
1131
1381
1500
1124


















Perfor-
Coefficient of
(relative to
100
89.30
97.11
90.85
92.95
96.90
91.33
91.66
92.32


mance
performance
R22 %)



Refrigerating
(relative to
100
86
66
82
74
65
80
80
76



capacity
R22 %)



Outlet
° C.
149
97
118
101
103
115
101
103
102



temperature



Outlet
(relative to
100
109.5
85.2
105.0
94.3
83.5
102.5
102.5
97.5



pressure
R22 %)




















Exam-
Exam-
Exam-
Exam-
Exam-

Compar-



Compar-
ple
ple
ple
ple
ple
Exam-
ative



ative
2-12
2-13
2-14
2-15
2-16
ple
Example
















Item
Unit
Example
F
B′
C′
E′
F′
2-17
2-11




















Compo-
R32
mass %
R22
12.4
12.4
12.4
12.4
12.4
12.4
12.4


sition
R125
mass %

24.0
27.4
28.9
22.8
25.6
25.0
15.0



1234yf
mass %

23.4
41.1
30.5
43.3
25.7
37.6
37.6



R134a
mass %

40.2
19.1
28.2
21.5
36.3
25.0
35.0
















GWP
Year
1810
1500
1317
1500
1191
1500
1318
1111

















Perfor-
Coefficient of
(relative to
100
93.24
91.59
92.07
92.08
92.86
92.14
93.46


mance
performance
R22 %)



Refrigerating
(relative to
100
76
79
79
77
77
78
74



capacity
R22 %)



Outlet
° C.
149
107
102
104
102
106
103
105



temperature



Outlet
(relative to
100
97.5
101.25
101.25
98.75
98.75
99.6
94.0



pressure
R22 %)


























TABLE 5-3










Compar-
Compar-
Compar-

Compar-








ative
ative
ative
Exam-
ative
Exam-
Exam-
Exam-




Compar-
Example
Example
Example
ple
Example
ple
ple
ple




ative
2-12
2-13
2-14
2-18
2-15
2-19
2-20
2-21


Item
Unit
Example
A
D
G′
H′ = E
I′
B
C
F





















Compo-
R32
mass %
R22
14.1
14.1
14.1
14.1
14.1
14.1
14.1
14.1


sition
R125
mass %

40.1
8.5
34.0
15.8
0.0
25.2
27.5
21.1



1234yf
mass %

45.8
0.0
36.9
45.8
9.8
41.2
27.5
18.2



R134a
mass %

0.0
77.4
15.0
24.3
76.1
19.5
30.9
46.6

















GWP
Year
1810
1500
1500
1500
997
1184
1256
1500
1500


















Perfor-
Coefficient of
(relative to
100
89.50
97.02
90.97
92.87
97.22
91.94
92.51
94.02


mance
performance
R22 %)



Refrigerating
(relative to
100
89
68
85
77
67
81
81
77



rapacity
R22 %)



Outlet
° C.
149
99
119
103
104
118
104
107
111



temperature



Outlet
(relative to
100
1121
87.5
107.5
97.5
84.9
102.5
102.5
97.5



pressure
R22 %)



















Exam-
Exam-
Exam-
Exam-

Compar-



Compar-
ple
ple
ple
ple
Exam-
ative



ative
2-22
2-23
2-24
2-25
ple
Example















Item
Unit
Example
B′
C′
E′
F′
2-26
2-16



















Compo-
R32
mass %
R22
14.1
14.1
14.1
14.1
14.1
14.1


sition
R125
mass %

22.9
25.9
18.1
22.7
20.0
30.0



1234yf
mass %

42.3
25.1
44.6
20.5
35.9
35.9



R134a
mass %

20.7
34.9
23.2
42.7
30.0
20.0















GWP
Year
1810
1194
1500
1062
1500
1226
1433
















Perfor-
Coefficient of
(relative to
100
92.17
92.88
92.65
93.64
92.95
91.60


mance
performance
R22 %)



Refrigerating
(relative to
100
80
80
78
78
78
83



capacity
R22 %)



Outlet
° C.
149
104
108
104
110
106
104



temperature



Outlet
(relative to
100
101.25
101.25
98.75
98.75
99.0
104.9



pressure
R22 %)


























TABLE 5-4










Compar-
Compar-
Compar-

Compar-








ative
ative
ative
Exam-
ative
Exam-
Exam-
Exam-




Compar-
Example
Example
Example
ple
Example
ple
ple
ple




ative
2-17
2-18
2-19
2-27
2-20
2-28
2-29
2-30


Item
Unit
Example
A
D
G′
H′ = E′
I′
B
C
E





















Compo-
R32
mass %
R22
14.8
14.8
14.8
14.8
14.8
14.8
14.8
14.8


sition
R125
mass %

40.0
8.8
34.0
16.5
0.0
23.3
26.3
14.6



1234yf
mass %

45.2
0.0
36.5
45.1
7.9
41.7
25.3
40.8



R134a
mass %

0.0
76.4
14.7
23.6
77.3
20.2
33.6
29.8

















GWP
Year
1810
1500
1500
1500
1017
1206
1206
1500
1039


















Perfor-
Coefficient of
(relative to
100
89.58
96.98
91.02
92.84
97.36
92.17
92.83
93.34


mance
performance
R22 %)



Refrigerating
(relative to
100
90
69
86
78
67
81
81
77



capacity
R22 %)



Outlet
° C.
149
100
120
103
105
119
105
109
107



temperature



Outlet
(relative to
100
113.1
88.4
108.6
98.75
85.4
102.5
102.5
97.5



pressure
R22 %)



















Exam-
Exam-
Exam-
Exam-

Compar-



Compar-
ple
ple
ple
ple
Exam-
ative



ative
2-31
2-32
2-33
2-34
ple
Example















Item
Unit
Example
F
B′
C′
F′
2-35
2-21



















Compo-
R32
mass %
R22
14.8
14.8
14.8
14.8
14.8
14.8


sition
R125
mass %

20.1
21.0
24.7
21.6
20.0
30.0



1234yf
mass %

16.4
42.9
23.1
18.6
35.2
25.2



R134a
mass %

48.7
21.3
37.4
45.0
30.0
30.0















GWP
Year
1810
1500
1141
1500
1500
1230
1580
















Perfor-
Coefficient of
(relative to
100
94.29
92.40
93.20
93.94
93.01
92.33


mance
performance
R22 %)



Refrigerating
(relative to
100
77
80
80
78
79
83



capacity
R22 %)



Outlet
° C.
149
113
105
110
112
107
108



temperature



Outlet
(relative to
100
97.5
101.25
101.25
98.75
99.94
104.75



pressure
R22 %)


























TABLE 5-5










Compar-
Compar-
Compar-

Compar-








ative
ative
ative
Exam-
ative
Exam-
Exam-
Exam-




Compar-
Example
Example
Example
ple
Example
ple
ple
ple




ative
2-22
2-23
2-24
2-36
2-25
2-37
2-38
2-39


Item
Unit
Example
A
D
G′
H′ = B′
I′
B
C
E





















Compo-
R32
mass %
R22
16.1
16.1
16.1
16.1
16.1
16.1
16.1
16.1


sition
R125
mass %

39.7
9.3
33.9
17.6
0.0
19.9
24.2
12.9



1234yf
mass %

44.2
0.0
35.8
43.9
4.8
42.8
21.7
33.4



R134a
mass %

0.0
74.6
14.2
22.4
79.1
21.2
38.0
37.6

















GWP
Year
1810
1500
1500
1500
1047
1240
1110
1500
1099


















Perfor-
Coefficient of
(relative to
100
89.73
96.91
91.11
92.79
97.57
92.57
93.38
94.03


mance
performance
R22 %)



Refrigerating
(relative to
100
92
71
88
81
68
82
81
78



capacity
R22 %)



Outlet
° C.
149
101
121
105
106
121
106
111
110



temperature



Outlet
(relative to
100
115.0
90.2
110.4
101.25
86.3
102.5
102.5
97.5



pressure
R22 %)



















Exam-
Exam-
Exam-
Exam-

Compar-



Compar-
ple
ple
ple
ple
Exam-
ative



ative
2-40
2-41
2-42
2-43
ple
Example















Item
Unit
Example
F
C′
E′
F′
2-44
2-26



















Compo-
R32
mass %
R22
16.1
16.1
16.1
16.1
16.1
16.1


sition
R125
mass %

18.1
22.7
14.4
19.6
20.0
10.0



1234yf
mass %

12.9
19.5
36.8
15.0
23.9
53.9



R134a
mass %

52.9
41.7
32.7
49.3
40.0
20.0















GWP
Year
1810
1500
1500
1500
1500
1382
747
















Perfor-
Coefficient of
(relative to
100
94.81
93.74
94.47
94.47
93.78
93.14


mance
performance
R22 %)



Refrigerating
(relative to
100
77
80
78
78
80
78



capacity
R22 %)



Outlet
° C.
149
116
113
115
115
112
105



temperature



Outlet
(relative to
100
97.5
101.25
98.75
98.75
100.3
97.8



pressure
R22 %)


























TABLE 5-6










Compar-
Compar-
Compar-

Compar-








ative
ative
ative
Exam-
ative
Exam-
Exam-
Exam-




Compar-
Example
Example
Example
ple
Example
ple
ple
ple




ative
2-27
2-28
2-29
2-45
2-30
2-46
2-47
2-48


Item
Unit
Example
A
D
G′
H′ = B
I′
C
E
F





















Compo-
R32
mass %
R22
16.8
16.8
16.8
16.8
16.8
16.8
16.8
16.8


sition
R125
mass %

39.6
9.5
33.9
18.3
0.0
23.1
12.1
17.2



1234yf
mass %

43.6
0.0
35.4
43.3
3.1
19.7
29.7
11.2



R134a
mass %

0.0
73.7
13.9
21.6
80.1
40.4
41.4
54.8

















GWP
Year
0
1810
1500
1500
1065
1259
1500
1130
1500


















Perfor-
Coefficient of
(relative to
100
89.80
96.87
91.15
92.75
97.69
93.68
94.37
95.05


mance
performance
R22 %)



Refrigerating
(relative to
100
94
72
90
82
69
82
78
77



capacity
R22 %)



Outlet
° C.
149
102
122
106
107
123
113
112
117



temperature



Outlet
(relative to
100
116.0
91.1
111.4
102.5
86.8
102.5
97.5
97.5



pressure
R22 %)



















Exam-
Exam-
Exam-
Exam-

Compar-



Compar-
ple
ple
ple
ple
Exam-
ative



ative
2-49
2-50
2-51
2-52
ple
Example















Item
Unit
Example
B′
C′
E′
F′
2-53
2-31



















Compo-
R32
mass %
R22
16.8
16.8
16.8
16.8
16.8
16.8


sition
R125
mass %

16.6
21.7
13.5
18.6
15.0
10.0



1234yf
mass %

39.6
17.6
32.8
13.2
33.2
13.2



R134a
mass %

27.0
43.9
36.9
51.4
35.0
60.0















GWP
Year
R22
0
1500
1115
1500
1140
1322
















Perfor-
Coefficient of
(relative to
100
93.19
94.01
94.00
94.73
93.79
95.78


mance
performance
R22 %)



Refrigerating
(relative to
100
81
81
79
78
80
74



capacity
R22 %)



Outlet
° C.
149
108
114
111
116
111
118



temperature



Outlet
(relative to
100
101.25
101.25
98.75
98.75
99.6
93.9



pressure
R22 %)


























TABLE 5-7










Compar-
Compar-
Compar-
Compar-
Compar-








ative
ative
ative
ative
ative
Exam-
Exam-
Exam-




Compar-
Example
Example
Example
Example
Example
ple
ple
ple




ative
2-32
2-33
2-34
2-35
2-36
2-54
2-55
2-56


Item
Unit
Example
A
D
G′
H′
I′
B
C
E





















Compo-
R32
mass %
R22
18.1
18.1
18.1
18.1
18.1
18.1
18.1
18.1


sition
R125
mass %

39.3
10.0
33.9
19.4
0.0
16.4
21.3
10.7



1234yf
mass %

42.6
0.0
34.7
42.1
0.0
35.6
16.4
23.2



R134a
mass %

0.0
71.9
13.3
20.4
81.9
29.9
44.2
48.0

















GWP
Year
1810
1500
1500
1500
1095
1293
1125
1500
1184


















Perfor-
Coefficient of
(relative to
100
89.94
96.80
91.22
92.71
97.91
93.48
94.15
94.97


mance
performance
R22 %)



Refrigerating
(relative to
100
96
74
92
85
70
82
82
78



capacity
R22 %)



Outlet
° C.
149
103
123
107
108
125
111
116
116



temperature



Outlet
(relative to
100
117.8
92.8
113.3
105.0
87.6
102.5
102.5
97.5



pressure
R22 %)




















Exam-
Exam-
Exam-
Exam-
Exam-

Compar-



Compar-
ple
ple
ple
ple
ple
Exam-
ative



ative
2-57
2-58
2-59
2-60
2-61
ple
Example
















Item
Unit
Example
F
B′
C′
E′
F′
2-62
2-37




















Compo-
R32
mass %
R22
18.1
18.1
18.1
18.1
18.1
18.1
18.1


sition
R125
mass %

15.4
15.0
19.8
12.1
16.9
15.0
20.0



1234yf
mass %

7.9
32.6
14.3
26.3
10.1
45.0
30.0



R134a
mass %

58.6
34.3
47.8
43.5
54.9
21.9
31.9
















GWP
Year
1810
1500
1139
1500
1169
1500
1292
1252

















Perfor-
Coefficient of
(relative to
100
95.52
93.84
94.49
94.60
95.17
94.55
93.26


mance
performance
R22 %)



Refrigerating
(relative to
100
78
81
81
79
79
80
84



capacity
R22 %)



Outlet
° C.
149
120
112
117
115
119
115
111



temperature



Outlet
(relative to
100
97.5
101.25
101.25
98.75
98.75
99.7
104.1



pressure
R22 %)


























TABLE 5-8










Compar-
Compar-
Compar-
Compar-
Compar-








ative
ative
ative
ative
ative
Exam-
Exam-
Exam-




Compar-
Example
Example
Example
Example
Example
ple
ple
ple




ative
2-38
2-39
2-40
2-41
2-42
2-63
2-64
2-65


Item
Unit
Example
A
D
G′
H′
I′
B
C
E





















Compo-
R32
mass %
R22
18.7
18.7
18.7
18.7
18.7
18.7
18.7
18.7


sition
R125
mass %

39.2
10.2
33.9
20.0
0.6
15.7
20.5
10.1



1234yf
mass %

42.1
0.0
34.4
41.6
0.0
32.4
15.0
20.6



R134a
mass %

0.0
71.1
13.0
19.6
80.7
33.2
45.8
50.6

















GWP
Year
0
0
1500
1500
1108
1301
1152
1500
1204


















Perfor-
Coefficient of
(relative to
100
90.00
96.76
91.25
92.66
97.83
93.77
94.35
95.22


mance
performance
R22 %)



Refrigerating
(relative to
100
97
75
93
86
71
83
82
78



capacity
R22 %)



Outlet
° C.
149
104
124
107
109
125
112
117
117



temperature



Outlet
(relative to
100
118.6
93.6
114.1
106.2
88.5
102.5
102.6
97.5



pressure
R22 %)






















Exam-
Exam-
Exam-
Exam-
Exam-

Compar-




Compar-
ple
ple
ple
ple
ple
Exam-
ative




ative
2-66
2-67
2-68
2-69
2-70
ple
Example


Item
Unit
Example
F
B′
C′
E′
F′
2-71
2-43




















Compo-
R32
mass %
R22
18.7
18.7
18.7
18.7
18.7
18.7
18.7


sition
R125
mass %

14.7
14.3
19.0
11.5
16.1
15.0
25.0



1234yf
mass %

6.6
29.4
12.8
23.5
8.6
16.3
6.3



R134a
mass %

60.0
37.6
49.5
46.3
56.6
50.0
50.0
















GWP
Year
R22
0
1166
1500
1192
1500
1367
1301

















Perfor-
Coefficient of
(relative to
100
95.70
94.13
94.70
94.86
95.38
94.94
97.83


mance
performance
R22 %)



Refrigerating
(relative to
100
78
81
81
79
79
80
71



capacity
R22 %)



Outlet
° C.
149
121
114
118
116
120
118
125



temperature



Outlet
(relative to
100
97.5
101.25
101.25
98.75
98.75
99.5
88.5



pressure
R22 %)


























TABLE 5-9










Compar-
Compar-
Compar-
Compar-
Compar-







ative
ative
ative
ative
ative
Exam-
Exam-
Exam-



Compar-
Example
Example
Example
Example
Example
ple
ple
ple



ative
2-44
2-45
2-46
2-47
2-48
2-72
2-73
2-74

















Item
Unit
Example
A
D
G′
H′
I′
B
C
E





















Compo-
R32
mass %
R22
20.0
20.0
20.0
20.0
20.0
20.0
20.0
20.0


sition
R125
mass %

38.9
10.7
33.8
21.2
1.8
14.4
18.8
9.0



1234yf
mass %

41.1
0.0
33.7
40.4
0.0
26.2
11.8
15.0



R134a
mass %

0.0
69.3
12.5
18.4
78.2
39.4
49.4
56.0

















GWP
Year
0
0
1500
1500
1142
1316
1203
1500
1251


















Perfor-
Coefficient of
(relative to
100
90.13
96.68
91.33
92.60
97.67
94.33
94.80
95.73


mance
performance
R22 %)



Refrigerating
(relative to
100
99
76
95
88
73
83
83
78



capacity
R22 %)



Outlet
° C.
149
105
125
109
110
127
116
120
121



temperature



Outlet
(relative to
100
120.3
95.4
115.9
108.6
90.6
102.5
102.5
97.5



pressure
R22 %)




















Exam-
Exam-
Exam-
Exam-
Exam-

Compar-



Compar-
ple
ple
ple
ple
ple
Exam-
ative



ative
2-75
2-76
2-77
2-78
2-79
ple
Example
















Item
Unit
Example
F
B′
C′
E′
F′
2-80
2-49




















Compo-
R32
mass %
R22
20.0
20.0
20.0
20.0
20.0
20.0
20.0


sition
R125
mass %

13.1
13.0
17.3
10.4
14.5
14.0
20.0



1234yf
mass %

3.5
23.3
9.6
17.9
5.5
13.0
30.0



R134a
mass %

63.4
43.7
53.1
51.7
60.0
53.0
30.0
















GWP
Year
R22
0
1216
1500
1239
1500
1383
1265

















Perfor-
Coefficient of
(relative to
100
96.12
94.69
95.15
95.36
95.80
95.29
93.39


mance
performance
R22 %)



Refrigerating
(relative to
100
78
82
81
80
79
80
86



capacity
R22 %)



Outlet
° C.
149
123
117
121
119
123
120
113



temperature



Outlet
(relative to
100
97.5
101.25
101.25
98.75
98.75
99.9
106.4



pressure
R22 %)


























TABLE 5-10










Compar-

Compar-
Compar-
Compar-







ative
Exam-
ative
ative
ative
Exam-
Exam-
Exam-



Compar-
Example
ple
Example
Example
Example
ple
ple
ple



ative
2-50
2-81
2-51
2-52
2-53
2-82
2-83
2-84

















Item
Unit
Example
A
D = F
G′
H′
I′
B
C
E





















Compo-
R32
mass %
R22
21.6
21.6
21.6
21.6
21.6
21.6
21.6
21.6


sition
R125
mass %

38.6
11.3
33.8
22.5
3.5
13.0
16.8
7.8



1234yf
mass %

39.8
0.0
32.9
38.9
0.0
19.3
8.0
8.8



R134a
mass %

0.0
67.1
11.7
17.0
74.9
46.1
53.6
61.8

















GWP
Year
1810
1500
1500
1500
1178
1339
1261
1500
1303


















Perfor-
Coefficient of
(relative to
100
90.28
96.59
91.40
92.54
97.45
94.95
95.31
96.30


mance
performance
R22 %)



Refrigerating
(relative to
100
101
79
97
91
75
83
83
79



capacity
R22 %)



Outlet
° C.
149
107
127
110
111
128
120
123
124



temperature



Outlet
(relative to
100
122.4
97.5
118.1
111.4
93.2
102.5
102.5
97.5



pressure
R22 %)



















Exam-
Exam-
Exam-
Exam-

Compar-



Compar-
ple
ple
ple
ple
Exam-
ative



ative
2-85
2-86
2-87
2-88
ple
Example















Item
Unit
Example
B′
C′
E′
F′
2-89
2-54



















Compo-
R32
mass %
R22
21.6
21.6
21.6
21.6
21.6
21.6


sition
R125
mass %

11.7
15.4
9.1
12.7
15.0
15.0



1234yf
mass %

16.9
6.0
11.4
2.0
8.4
33.4



R134a
mass %

49.8
57.0
57.9
63.7
55.0
30.0















GWP
Year
1810
1268
1500
1293
1500
1458
1101
















Perfor-
Coefficient of
(relative to
100
95.27
101.01
95.96
96.27
95.50
93.80


mance
performance
R22 %)



Refrigerating
(relative to
100
82
87
80
80
82
87



capacity
R22 %)



Outlet
° C.
149
121
124
123
126
123
115



temperature



Outlet
(relative to
100
101.25
101.25
98.75
98.75
101.5
106.0



pressure
R22 %)


























TABLE 5-11










Compar-

Compar-
Compar-
Compar-







ative
Exam-
ative
ative
ative
Exam-
Exam-
Exam-



Compar-
Example
ple
Example
Example
Example
ple
ple
ple



ative
2-55
2-90
2-56
2-57
2-58
2-91
2-92
2-93

















Item
Unit
Example
A
D = F′
G′
H′
I′
B
C
E





















Compo-
R32
mass %
R22
22.6
22.6
22.6
22.6
22.6
22.6
22.6
22.6


sition
R125
mass %

38.4
11.6
33.8
23.3
4.6
12.2
15.6
7.2



1234yf
mass %

39.0
0.0
32.3
38.0
0.0
15.4
5.8
5.3



R134a
mass %

0.0
65.8
11.3
16.1
72.8
49.8
56.0
64.9

















GWP
Year
1810
1500
1500
1500
1200
1355
1292
1500
1333


















Perfor-
Coefficient of
(relative to
100
90.37
96.54
91.45
92.49
97.31
95.30
95.61
96.61


mance
performance
R22 %)



Refrigerating
(relative to
100
103
80
99
93
77
83
83
79



capacity
R22 %)



Outlet
° C.
149
108
127
111
112
129
122
125
127



temperature



Outlet
(relative to
100
123.6
98.75
119.4
113.2
94.9
102.5
102.5
97.5



pressure
R22 %)



















Exam-
Exam-
Exam-
Exam-

Compar-



Compar-
ple
ple
ple
ple
Exam-
ative



ative
2-94
2-95
2-96
2-97
ple
Example















Item
Unit
Example
F
B′
C′
E′
2-98
2-59



















Compo-
R32
mass %
R22
22.6
22.6
22.6
22.6
22.6
22.6


sition
R125
mass %

9.4
11.0
14.3
8.4
12.5
20.0



1234yf
mass %

0.0
13.0
3.9
7.7
4.9
7.4



R134a
mass %

68.0
53.4
59.2
61.3
60.0
50.0















GWP
Year
1810
1454
1302
1500
1322
1448
1568
















Perfor-
Coefficient of
(relative to
100
96.78
95.61
95.91
101.57
96.04
94.96


mance
performance
R22 %)



Refrigerating
(relative to
100
79
82
82
85
82
86



capacity
R22 %)



Outlet
° C.
149
128
123
126
125
126
123



temperature



Outlet
(relative to
100
97.5
101.3
101.25
98.75
100.4
105.5



pressure
R22 %)


























TABLE 5-12










Compar-
Compar-
Compar-
Compar-








ative
ative
ative
ative
Exam-
Exam-
Exam-
Exam-



Compar-
Example
Example
Example
Example
ple
ple
ple
ple



ative
2-60
2-61
2-62
2-63
2-99
2-100
2-101
2-102

















Item
Unit
Example
A
D
G
H′
I′ = E = F
B
C
B′





















Compo-
R32
mass %
R22
24.2
24.2
24.2
24.2
24.2
24.2
24.2
24.2


sition
R125
mass %

38.1
12.2
33.9
24.6
6.2
11.1
13.9
9.9



1234yf
mass %

37.7
0.0
31.4
36.5
0.0
9.8
2.5
7.2



R134a
mass %

0.0
63.6
10.5
14.8
69.6
54.9
59.4
58.7

















GWP
Year
1810
1500
1500
1500
1237
1376
1337
1500
1350


















Perfor-
Coefficient of
(relative to
100
90.52
96.43
91.50
92.43
97.09
95.80
96.04
96.13


mance
performance
R22 %)



Refrigerating
(relative to
100
105
82
101
96
79
84
84
83



capacity
R22 %)



Outlet
° C.
149
109
129
113
114
130
126
128
127



temperature



Outlet
(relative to
100
125.6
100.9
121.6
116.0
97.5
102.5
102.5
101.25



pressure
R22 %)


















Exam-
Exam-
Exam-

Compar-



Compar-
ple
ple
ple
Exam-
ative



ative
2-103
2-104
2-105
ple
Example














Item
Unit
Example
C′
E′
F′
2-106
2-64


















Compo-
R32
mass %
R22
24.2
24.2
24.2
24.2
24.2


sition
R125
mass %

12.6
7.4
8.5
10.0
25.0



1234yf
mass %

0.6
2.4
0.0
0.8
30.8



R134a
mass %

62.6
66.0
67.3
65.0
20.0














GWP
Year
1810
1500
1366
1423
1443
1326















Perfor-
Coefficient of
(relative to
100
96.34
96.78
96.84
96.62
92.72


mance
performance
R22 %)



Refrigerating
(relative to
100
83
81
81
81
96



capacity
R22 %)



Outlet
° C.
149
129
129
130
129
115



temperature



Outlet
(relative to
100
101.25
98.75
98.75
99.8
115.4



pressure
R22 %)


























TABLE 5-13










Compar-

Compar-
Compar-








ative
Exam-
ative
ative
Exam-
Exam-
Exam-
Exam-



Compar-
Example
ple
Example
Example
ple
ple
ple
ple



ative
2-65
2-107
2-66
2-67
2-108
2-109
2-110
2-111

















Item
Unit
Example
A
D = C′
G′
H′
I′
B
C
B′





















Compo-
R32
mass %
R22
24.5
24.5
24.5
24.5
24.5
24.5
24.5
24.5


sition
R125
mass %

38.1
12.3
33.9
24.8
6.4
10.8
13.6
9.6



1234yf
mass %

37.4
0.0
31.2
36.2
0.0
8.7
1.9
6.3



R134a
mass %

0.0
63.2
10.4
14.5
69.1
56.0
60.0
59.6

















GWP
Year
0
1500
1500
1500
1242
1378
1345
1500
1354


















Perfor-
Coefficient of
(relative to
100
90.54
96.42
91.52
92.42
97.06
95.91
96.12
96.23


mance
performance
R22 %)



Refrigerating
(relative to
100
106
83
102
97
80
84
84
83



capacity
R22 %)



Outlet
° C.
149
110
129
113
114
130
126
128
128



temperature



Outlet
(relative to
100
126.0
101.25
122.0
116.5
97.9
102.5
102.5
101.25



pressure
R22 %)

















Exam-
Exam-

Compar-



Compar-
ple
ple
Exam-
ative



ative
2-112
2-113
ple
Example













Item
Unit
Example
E′
F′
2-114
2-68

















Compo-
R32
mass %
R22
24.5
24.5
24.5
24.5


sition
R125
mass %

7.2
7.9
10.0
10.0



1234yf
mass %

1.6
0.0
0.5
15.5



R134a
mass %

66.7
67.6
65.0
50.0













GWP
Year
R22
1371
1409
1445
1231














Perfor-
Coefficient of
(relative to
100
96.85
96.90
96.63
95.52


mance
performance
R22 %)



Refrigerating
(relative to
100
81
81
82
85



capacity
R22 %)



Outlet
° C.
149
130
130
129
124



temperature



Outlet
(relative to
100
98.75
98.75
100.1
103.4



pressure
R22 %)


























TABLE 5-14










Compar-

Compar-
Compar-








ative
Exam-
ative
ative
Exam-
Exam-
Exam-
Exam-



Compar-
Example
ple
Example
Example
ple
ple
ple
ple



ative
2-69
2-115
2-70
2-71
2-116
2-117
2-118
2-119

















Item
Unit
Example
A
D
G′
H′
I′ = E′ = F′
B
C
B′





















Compo-
R32
mass %
R22
25.1
25.1
25.1
25.1
25.1
25.1
25.1
25.1


sition
R125
mass %

38.0
12.5
33.9
25.2
7.1
10.5
13.0
9.3



1234yf
mass %

36.9
0.0
30.9
35.6
0.0
6.6
0.7
4.3



R134a
mass %

0.0
62.4
10.1
14.1
67.8
57.8
61.2
61.3

















GWP
Year
1810
1500
1500
1500
1244
1381
1364
1500
1372


















Perfor-
Coefficient of
(relative to
100
90.59
96.38
91.54
92.48
97.01
96.09
96.27
96.40


mance
performance
R22 %)



Refrigerating
(relative to
100
106
84
103
97
81
84
84
83



capacity
R22 %)



Outlet
° C.
149
110
130
114
114
131
128
129
129



temperature



Outlet
(relative to
100
126.3
102.0
122.8
116.7
98.75
102.5
102.5
101.25



pressure
R22 %)














Exam-



Compar-
ple



ative
2-120













Item

Unit
Example
C′

















Compo-
R32
mass %
R22
25.1



sition
R125
mass %

11.1




1234yf
mass %

0.0




R134a
mass %

63.8










GWP
Year
1810
1470













Perfor-
Coefficient of
(relative to
100
96.54



mance
performance
R22 %)




Refrigerating
(relative to
100
83




capacity
R22 %)




Outlet
° C.
149
130




temperature




Outlet
(relative to
100
101.25




pressure
R22 %)



























TABLE 6-1










Compar-
Compar-

Compar-
Compar-
Compar-
Compar-
Compar-




ative
ative
Exam-
ative
ative
ative
ative
ative



Compar-
Example
Example
ple
Example
Example
Example
Example
Example



ative
3-1
3-2
3-1
3-3
3-4
3-5
3-6
3-7

















Item
Unit
Example
A
D
G′ = J = K
H′
I′
Q
R
S





















Compo-
R32
mass %
R404A
11.6
11.6
11.6
11.6
11.6
11.6
11.6
11.6


sition
R125
mass %

40.6
7.6
34.0
13.4
00
0.0
10.6
18.9



1234yf
mass %

47.8
0.0
38.3
48.2
16.5
9.8
4.3
45.6



R134a
mass %

0.0
80.8
16.1
26.8
71.9
78.6
73.5
23.9

















GWP
Year
3922
1500
1500
1500
932
1107
1203
1500
1083


















Perfor-
Coefficient of
(relative to
100
103.97
113.25
105.83
108.38
112.78
113.37
112.39
107.75


mance
performance
R404A %)



Refrigerating
(relative to
100
89
68
85
76
68
67
70
78



capacity
R404A %)



Outlet
° C.
93
96
117
100
102
113
115
115
101



temperature

















ASHRAE

Non-
Flam-
Non-
Non-
Non-
Non-
Non-
Non-
Non-


non-flammability

flam-
mable
flam-
flam-
flam-
flam-
flam-
flam-
flam-




mable

mable
mable
mable
mable
mable
mable
mable














Compar-




ative



Compar-
Example



ative
3-8












Item
Unit
Example
T

















Compo-
R32
mass %
R404A
11.6



sition
R125
mass %

27.1




1234yf
mass %

28.3




R134a
mass %

33.0










GWP
Year
3922
1500













Perfor-
Coefficient of
(relative to
100
107.75



mance
performance
R404A %)




Refrigerating
(relative to
100
81




capacity
R404A %)




Outlet
° C.
93
105




temperature










ASHRAE

Non-
Non-


non-flammability

flam-
flam-




mable
mable


























TABLE 6-2










Compar-
Compar-

Compar-
Compar-


Compar-




ative
ative
Exam-
ative
ative
Exam-
Exam-
ative



Compar-
Example
Example
ple
Example
Example
ple
ple
Example



ative
3-9
3-10
3-2
3-11
3-12
3-3
3-4
3-13

















Item
Unit
Example
A
D
G′
H′
I′
J
K = T
Q





















Compo-
R32
mass %
R404A
14.2
14.2
14.2
14.2
14.2
14.2
14.2
142


sition
R125
mass %

40.1
8.6
34.0
15.9
0.0
24.7
27.8
3.5



1234yf
mass %

45.7
0.0
36.9
45.7
9.5
41.5
27.9
17.5



R134a
mass %

0.0
77.2
14.9
24.2
76.3
19.6
30.1
64.8

















GWP
Year
3922
1500
1500
1500
1000
1187
1242
1500
1146


















Perfor-
Coefficient of
(relative to
100
104.34
113.08
106.04
108.25
113.35
107.21
107.75
112.18


mance
performance
R404A %)



Refrigerating
(relative to
100
94
72
90
81
70
85
85
72



capacity
R404A %)



Outlet
° C.
93
99
119
103
104
118
104
107
115



temperature

















ASHRAE

Non-
Flam-
Non-
Non-
Non-
Non-
Non-
Non-
Non-


non-flammability

flam-
mable
flam-
flam-
flam-
flam-
flam-
flam-
flam-




mable

mable
mable
mable
mable
mable
mable
mable

















Compar-
Compar-






ative
ative

Compar-



Compar-
Example
Example
Exam-
ative



ative
3-14
3-15
ple
Example













Item
Unit
Example
R
S
3-5
3-16

















Compo-
R32
mass %
R404A
14.2
14.2
14.2
14.2


sition
R125
mass %

15.7
20.2
30.0
20.0



1234yf
mass %

10.4
43.7
35.8
35.8



R134a
mass %

59.7
21.9
20.0
30.0













GWP
Year
3922
1500
1118
1433
1226














Perfor-
Coefficient of
(relative to
100
111.09
107.75
106.79
108.36


mance
performance
R404A %)



Refrigerating
(relative to
100
77
83
87
82



capacity
R404A %)



Outlet
° C.
93
115
104
104
106



temperature













ASHRAE

Non-
Non-
Non-
Non-
Non-


non-flammability

flam-
flam-
flam-
flam-
flam-




mable
mable
mable
mable
mable


























TABLE 6-3










Compar-
Compar-

Compar-
Compar-


Compar-




ative
ative
Exam-
ative
ative
Exam-
Exam-
ative



Compar-
Example
Example
ple
Example
Example
ple
ple
Example



ative
3-17
3-18
3-6
3-19
3-20
3-7
3-8
3-21

















Item
Unit
Example
A
D
G′ = L = M
H′
I′
J
K
Q





















Compo-
R32
mass %
R404A
14.5
14.5
14.5
14.5
14.5
14.5
14.5
14.5


sition
R125
mass %

40.0
8.7
34.0
16.2
0.0
23.6
26.9
4.2



1234yf
mass %

45.5
0.0
36.7
45.5
8.7
41.8
26.5
18.2



R134a
mass %

0.0
76.8
14.8
23.9
76.8
20.1
32.1
63.1

















GWP
Year
3922
1500
1500
1500
1008
1196
1213
1500
1148


















Perfor-
Coefficient of
(relative to
100
104.38
113.06
106.07
108.23
113.41
107.37
108.01
112.03


mance
performance
R404A %)



Refrigerating
(relative to
100
94
72
90
82
70
85
85
73



capacity
R404A %)



Outlet
° C.
93
99
120
103
105
118
104
108
115



temperature

















ASHRAE

Non-
Flam-
Non-
Non-
Non-
Non-
Non-
Non-
Non-


non-flammability

flam-
mable
flam-
flam-
flam-
flam-
flam-
flam-
flam-




mable

mable
mable
mable
mable
mable
mable
mable



















Compar-
Compar-








ative
ative
Exam-
Exam-

Compar-



Compar-
Example
Example
ple
ple
Exam-
ative



ative
3-22
3-23
3-9
3-10
ple
Example















Item
Unit
Example
R
S
T
U
3-11
3-24



















Compo-
R32
mass %
R404A
14.5
14.5
14.5
14.5
14.5
14.5


sition
R125
mass %

16.2
20.4
27.9
25.6
27.0
20.0



1234yf
mass %

11.0
43.4
27.8
32.6
28.5
45.5



R134a
mass %

58.3
21.7
29.8
27.3
30.0
20.0















GWP
Year
3922
1500
1124
1500
1386
1473
1435
















Perfor-
Coefficient of
(relative to
100
110.96
107.75
107.75
107.74
107.84
106.82


mance
performance
R404A %)



Refrigerating
(relative to
100
77
83
66
85
85
88



capacity
R404A %)



Outlet
° C.
93
115
104
107
106
107
104



temperature















ASHRAE

Non-
Non-
Non-
Non-
Non-
Non-
Non-


non-flammability

flam-
flam-
flam-
flam-
flam-
flam-
flam-




mable
mable
mable
mable
mable
mable
mable


























TABLE 6-4










Compar-
Compar-

Compar-
Compar-







ative
ative
Exam-
ative
ative
Exam-
Exam-
Exam-



Compar-
Example
Example
ple
Example
Example
ple
ple
ple



ative
3-25
3-26
3-12
3-27
3-28
3-13
3-14
3-15

















Item
Unit
Example
A
D
G′
H′
I′
J = S
K
L





















Compo-
R32
mass %
R404A
15.3
15.3
15.3
15.3
15.3
15.3
15.3
15.3


sition
R125
mass %

39.9
9.0
34.0
16.9
0.0
20.9
25.3
31.3



1234yf
mass %

44.8
0.0
36.2
44.7
6.7
42.7
23.7
37.6



R134a
mass %

0.0
75.7
14.5
23.1
78.0
21.1
35.7
15.8

















GWP
Year
3922
1500
1500
1500
1027
1219
1138
1500
1426


















Perfor-
Coefficient of
(relative to
100
104.48
113.01
106.13
108.19
113.58
107.75
108.51
106.47


mance
performance
R404A %)



Refrigerating
(relative to
100
96
73
91
83
71
85
85
90



capacity
R404A %)



Outlet
° C.
93
100
121
104
106
120
105
110
104



temperature

















ASHRAE

Non-
Flam-
Non-
Non-
Non-
Non-
Non-
Non-
Non-


non-flammability

flam-
mable
flam-
flam-
flam-
flam-
flam-
flam-
flam-




mable

mable
mable
mable
mable
mable
mable
mable


















Compar-
Compar-





Exam-
ative
ative
Exam-



Compar-
ple
Example
Example
ple



ative
3-16
3-29
3-30
3-17













Item
Unit
Example
M
Q
R
T

















Compo-
R32
mass %
R404A
15.3
15.3
15.3
15.3


sition
R125
mass %

32.1
5.8
17.7
28.1



1234yf
mass %

33.6
19.7
12.6
27.7



R134a
mass %

19.0
59.2
54.4
28.9













GWP
Year
3922
1500
1154
1500
1500














Perfor-
Coefficient of
(relative to
100
106.64
111.68
110.59
107.75


mance
performance
R404A %)



Refrigerating
(relative to
100
90
75
80
87



capacity
R404A %)



Outlet
° C.
93
105
115
115
108



temperature













ASHRAE

Non-
Non-
Non-
Non-
Non-


non-flammability

flam-
flam-
flam-
flam-
flam-




mable
mable
mable
mable
mable


























TABLE 6-5










Compar-
Compar-


Compar-







ative
ative
Exam-
Exam-
ative
Exam-
Exam-
Exam-



Compar-
Example
Example
ple
ple
Example
ple
ple
ple



ative
3-31
3-32
3-18
3-19
3-33
3-20
3-21
3-22

















Item
Unit
Example
A
D
G′
H′ = J
I′
K
L
M





















Compo-
R32
mass %
R404A
16.2
16.2
16.2
16.2
16.2
16.2
16.2
16.2


sition
R125
mass %

39.7
9.3
33.9
17.7
0.0
23.5
28.3
30.1



1234yf
mass %

44.1
0.0
35.8
43.8
4.6
20.6
38.6
30.2



R134a
mass %

0.0
74.5
14.1
22.3
79.2
39.7
16.9
23.5

















GWP
Year
3922
1500
1500
1500
1049
1242
1500
1343
1500


















Perfor-
Coefficient of
(relative to
100
104.60
112.95
106.20
108.16
113.75
109.05
106.91
107.25


mance
performance
R404A %)



Refrigerating
(relative to
100
97
75
93
85
72
85
90
90



capacity
R404A %)



Outlet
° C.
93
101
121
105
106
121
112
105
108



temperature

















ASHRAE

Non-
Flam-
Non-
Non-
Non-
Non-
Non-
Non-
Non-


non-flammability

flam-
mable
flam-
flam-
flam-
flam-
flam-
flam-
flam-




mable

mable
mable
mable
mable
mable
mable
mable



















Compar-
Compar-








ative
ative
Exam-
Exam-

Compar-



Compar-
Example
Example
ple
ple
Exam-
ative



ative
3-34
3-35
3-23
3-24
ple
Example















Item
Unit
Example
Q
R
S
T
3-25
3-36



















Compo-
R32
mass %
R404A
16.2
16.2
16.2
16.2
16.2
16.2


sition
R125
mass %

7.7
19.2
21.2
28.2
25.0
10.0



1234yf
mass %

21.7
14.4
42.1
27.4
28.8
13.8



R134a
mass %

54.4
50.2
20.5
28.2
30.0
60.0















GWP
Year
3922
1158
1500
1146
1500
1415
1318
















Perfor-
Coefficient of
(relative to
100
111.25
110.22
107.75
107.75
108.16
111.59


mance
performance
R404A %)



Refrigerating
(relative to
100
77
82
87
89
87
77



capacity
R404A %)



Outlet
° C.
93
115
115
106
109
109
117



temperature















ASHRAE

Non-
Non-
Non-
Non-
Non-
Non-
Non-


non-flammability

flam-
flam-
flam-
flam-
flam-
flam-
flam-




mable
mable
mable
mable
mable
mable
mable


























TABLE 6-6










Compar-
Compar-


Compar-







ative
ative
Exam-
Exam-
ative
Exam-
Exam-
Exam-



Compar-
Example
Example
ple
ple
Example
ple
ple
ple



ative
3-37
3-38
3-26
3-27
3-39
3-28
3-29
3-30

















Item
Unit
Example
A
D
G′
H′
I′
J
K
L





















Compo-
R32
mass %
R404A
17.0
17.0
17.0
17.0
17.0
17.0
17.0
17.0


sition
R125
mass %

39.5
9.6
33.9
18.4
0.0
16.4
22.0
25.6



1234yf
mass %

43.5
0.0
35.3
43.1
2.6
38.7
18.1
39.5



R134a
mass %

0.0
73.4
13.8
21.5
80.4
27.9
42.9
17.9

















GWP
Year
3922
1500
1500
1500
1068
1265
1089
1500
1268


















Perfor-
Coefficient of
(relative to
100
104.70
112.90
106.26
108.12
113.91
108.72
109.49
107.29


mance
performance
R404A %)



Refrigerating
(relative to
100
98
76
94
87
72
85
85
90



capacity
R404A %)



Outlet
° C.
93
102
122
106
107
123
109
114
107



temperature

















ASHRAE

Non-
Flam-
Non-
Non-
Non-
Non-
Non-
Non-
Non-


non-flammability

flam-
mable
flam-
flam-
flam-
flam-
flam-
flam-
flam-




mable

mable
mable
mable
mable
mable
mable
mable


















Compar-
Compar-





Exam-
ative
ative
Exam-



Compar-
ple
Example
Example
ple



ative
3-31
3-40
3-41
3-32













Item
Unit
Example
M = T
Q
R
S

















Compo-
R32
mass %

17.0
17.0
17.0
17.0


sition
R125
mass %
R404A
28.3
9.4
20.5
21.6



1234yf
mass %

27.2
23.3
15.8
41.5



R134a
mass %

27.5
50.3
46.7
19.9













GWP
Year
3922
1500
1164
1500
1157














Perfor-
Coefficient of
(relative to
100
107.78
110.88
109.90
107.75


mance
performance
R404A %)



Refrigerating
(relative to
100
90
80
84
88



capacity
R404A %)



Outlet
° C.
93
110
115
115
107



temperature













ASHRAE

Non-
Non-
Non-
Non-
Non-


non-flammability

flam-
flam-
flam-
flam-
flam-




mable
mable
mable
mable
mable


























TABLE 6-7










Compar-
Compar-


Compar-







ative
ative
Exam-
Exam-
ative
Exam-
Exam-
Exam-



Compar-
Example
Example
ple
ple
Example
ple
ple
ple



ative
3-42
3-43
3-33
3-34
3-44
3-35
3-36
3-37

















Item
Unit
Example
A
D
G′ = O = P
H′
I′
J
K = R
L





















Compo-
R32
mass %
R404A
17.5
17.5
17.5
17.5
17.5
17.5
17.5
17.5


sition
R125
mass %

39.4
9.8
33.9
18.9
0.0
15.6
21.1
23.9



1234yf
mass %

43.1
0.0
35.0
42.6
1.4
35.5
16.5
40.1



R134a
mass %

0.0
72.7
13.6
21.0
81.1
31.4
44.9
18.5

















GWP
Year
3922
1500
1500
1500
1082
1278
1115
1500
1221


















Perfor-
Coefficient of
(relative to
100
104.77
112.86
106.29
108.09
114.01
109.07
109.76
107.52


mance
performance
R404A %)



Refrigerating
(relative to
100
99
77
95
88
73
85
85
90



capacity
R404A %)



Outlet
° C.
93
103
123
106
108
124
110
115
107



temperature

















ASHRAE

Non-
Flam-
Non-
Non-
Non-
Non-
Non-
Non-
Non-


non-flammability

flam-
mable
flam-
flam-
flam-
flam-
flam-
flam-
flam-




mable

mable
mable
mable
mable
mable
mable
mable



















Compar-







Exam-
ative
Exam-
Exam-
Exam-



Compar-
ple
Example
ple
ple
ple



ative
3-38
3-45
3-39
3-40
3-41














Item
Unit
Example
M
Q
S
T
V


















Compo-
R32
mass %

17.5
17.5
17.5
17.5
17.5


sition
R125
mass %
R404A
27.5
10.4
22.0
28.5
25.6



1234yf
mass %

25.8
24.2
41.1
27.2
33.4



R134a
mass %

29.2
47.9
19.4
26.8
23.5














GWP
Year
3922
1500
1168
1167
1500
1352















Perfor-
Coefficient of
(relative to
100
108.03
110.67
107.75
107.75
107.75


mance
performance
R404A %)



Refrigerating
(relative to
100
90
81
89
91
90



capacity
R404A %)



Outlet
° C.
93
111
115
107
110
109



temperature














ASHRAE

Non-
Non-
Non-
Non-
Non-
Non-


non-flammability

flam-
flam-
flam-
flam-
flam-
flam-




mable
mable
mable
mable
mable
mable


























TABLE 6-8










Compar-
Compar-


Compar-

Compar-





ative
ative
Exam-
Exam-
ative
Exam-
ative
Exam-



Compar-
Example
Example
ple
ple
Example
ple
Example
ple



ative
3-46
3-47
3-42
3-43
3-48
3-44
3-49
3-45

















Item
Unit
Example
A
D
G′
H′
I′
J
K
L = S





















Compo-
R32
mass %
R404A
18.0
18.0
18.0
18.0
18.0
18.0
18.0
18.0


sition
R125
mass %

39.3
10.0
33.9
19.3
0.0
14.8
20.2
22.2



1234yf
mass %

42.7
0.0
34.8
42.2
0.2
32.5
14.9
40.8



R134a
mass %

0.0
72.0
13.4
20.5
81.8
34.7
46.9
19.0

















GWP
Year
3922
1500
1500
1500
1092
1291
1137
1500
1172


















Perfor-
Coefficient of
(relative to
100
104.83
112.83
106.33
108.07
114.11
109.41
110.03
107.73


mance
performance
R404A %)



Refrigerating
(relative to
100
100
77
96
89
73
85
85
90



capacity
R404A %)



Outlet
° C.
93
103
123
107
108
125
112
116
108



temperature

















ASHRAE

Non-
Flam-
Non-
Non-
Non-
Non-
Non-
Non-
Non-


non-flammability

flam-
mable
flam-
flam-
flam-
flam-
flam-
flam-
flam-




mable

mable
mable
mable
mable
mable
mable
mable
























Compar-








Exam-
Exam-
Exam-
ative
Exam-
Exam-
Exam-



Compar-
ple
ple
ple
Example
ple
ple
ple
Exam-



ative
3-46
3-47
3-48
3-50
3-49
3-50
3-51
ple

















Item
Unit
Example
M
O
P
Q
R
T
X
3-52





















Compo-
R32
mass %
R404A
18.0
18.0
18.0
18.0
18.0
18.0
18.0
18.0


sition
R125
mass %

26.6
32.2
32.8
11.4
22.2
28.7
18.6
20.0



1234yf
mass %

24.1
35.7
33.2
25.1
17.8
27.1
43.3
32.0



R134a
mass %

31.3
14.1
16.0
45.5
42.1
26.2
20.0
30.0

















GWP
Year
3922
1500
1452
1500
1172
1500
1500
1394
1252


















Perfor-
Coefficient of
(relative to
100
108.30
106.53
106.62
110.46
109.49
107.75
109.84
108.70


mance
performance
R404A %)



Refrigerating
(relative to
100
90
95
95
82
87
92
85
88



capacity
R404A %)



Outlet
° C.
93
112
107
107
115
115
110
115
111



temperature

















ASHRAE

Non-
Non-
Non-
Non-
Non-
Non-
Non-
Non-
Non-


non-flammability

flam-
flam-
flam-
flam-
flam-
flam-
flam-
flam-
flam-




mable
mable
mable
mable
mable
mable
mable
mable
mable




















Compar-






Compar-
ative






ative
Example



Item

Unit
Example
3-51

















Compo-
R32
mass %
R404A
18.0



sition
R125
mass %

10.0




1234yf
mass %

52.0




R134a
mass %

20.0










GWP
Year
3922
760













Perfor-
Coefficient of
(relative to
100
108.72



mance
performance
R404A %)




Refrigerating
(relative to
100
85




capacity
R404A %)




Outlet
° C.
93
107




temperature










ASHRAE

Non-
Flam-


non-flammability

flam-
mable




mable


























TABLE 6-9










Compar-
Compar-


Compar-

Compar-






ative
ative
Exam-
Exam-
ative
Exam-
ative
Exam-




Compar-
Example
Example
ple
ple
Example
ple
Example
ple




ative
3-52
3-53
3-53
3-54
3-54
3-55
3-55
3-56


Item
Unit
Example
A
D
G′
H′ = L
I′
J
K
M





















Compo-
R32
mass %
R404A
18.7
18.7
18.7
18.7
18.7
18.7
18.7
18.7


sition
R125
mass %

39.2
10.2
33.9
20.0
0.6
13.9
19.0
25.3



1234yf
mass %

42.1
0.0
34.4
41.6
0.0
28.6
12.8
21.9



R134a
mass %

0.0
71.1
13.0
19.7
80.7
38.8
49.5
34.1

















GWP
Year
3922
1500
1500
1500
1110
1301
1169
1500
1500


















Perfor-
Coefficient of
(relative to
100
104.90
112.79
106.37
108.02
114.04
109.87
110.39
108.69


mance
performance
R404A %)



Refrigerating
(relative to
100
101
78
97
90
74
85
85
90



capacity
R404A %)



Outlet
° C.
93
104
124
107
109
125
114
118
114



temperature

















ASHRAE

Non-
Flam-
Non-
Non-
Non-
Non-
Non-
Non-
Non-


non-flammability

flam-
mable
flam-
flam-
flam-
flam-
flam-
flam-
flam-




mable

mable
mable
mable
mable
mable
mable
mable
























Compar-









Exam-
Exam-
ative
Exam-
Exam-
Exam-
Exam-




Compar-
ple
ple
Example
ple
ple
ple
ple




ative
3-57
3-58
3-56
3-59
3-60
3-61
3-62


Item
Unit
Example
O
P
Q
R
S
T
X




















Compo-
R32
mass %
R404A
18.7
18.7
18.7
18.7
18.7
18.7
18.7


sition
R125
mass %

30.0
31.4
12.8
23.3
22.4
28.9
15.0



1234yf
mass %

36.4
30.7
26.2
19.0
40.4
26.9
24.7



R134a
mass %

14.9
19.2
42.3
39.0
18.5
25.5
41.6
















GWP
Year
3922
1391
1500
1180
1500
1176
1500
1247

















Perfor-
Coefficient of
(relative to
100
106.85
107.05
110.17
109.23
107.75
107.75
109.98


mance
performance
R404A %)



Refrigerating
(relative to
100
95
95
84
88
91
93
85



capacity
R404A %)



Outlet
° C.
93
108
109
115
115
109
111
115



temperature
















ASHRAE

Non-
Non-
Non-
Non-
Non-
Non-
Non-
Non-


non-flammability

flam-
flam-
flam-
flam-
flam-
flam-
flam-
flam-




mable
mable
mable
mable
mable
mable
mable
mable


























TABLE 6-10










Compar-
Compar-


Compar-

Compar-






ative
ative
Exam-
Exam-
ative
Exam-
ative
Exam-




Compar-
Example
Example
ple
ple
Example
ple
Example
ple




ative
3-57
3-58
3-63
3-64
3-59
3-65
3-60
3-66


Item
Unit
Example
A
D
G′
H′
I′
J = Q
K
L





















Compo-
R32
mass %
R404A
19.0
19.0
19.0
19.0
19.0
19.0
19.0
19.0


sition
R125
mass %

39.1
10.3
33.8
20.3
0.8
13.4
18.5
19.5



1234yf
mass %

41.9
0.0
34.3
41.3
0.0
26.7
11.9
39.7



R134a
mass %

0.0
70.7
12.9
19.4
80.2
40.9
50.6
21.8

















GWP
Year
3922
1500
1500
1500
1118
1303
1183
1500
1124


















Perfor-
Coefficient of
(relative to
100
104.94
112.77
106.40
108.00
114.00
110.05
110.54
108.23


mance
performance
R404A %)



Refrigerating
(relative to
100
102
79
98
91
75
85
85
90



capacity
R404A %)



Outlet
° C.
93
104
124
108
109
126
115
119
110



temperature

















ASHRAE

Non-
Flam-
Non-
Non-
Non-
Non-
Non-
Non-
Non-


non-flammability

flam-
mable
flam-
flam-
flam-
flam-
flam-
flam-
flam-




mable

mable
mable
mable
mable
mable
mable
mable























Compar-








Exam-
Exam-
ative
Exam-
Exam-
Exam-




Compar-
ple
ple
Example
ple
ple
ple




ative
3-67
368
3-61
3-69
3-70
3-71


Item
Unit
Example
M
O
P
R
S
T



















Compo-
R32
mass %
R404A
19.0
19.0
19.0
19.0
19.0
19.0


sition
R125
mass %

24.7
29.1
30.8
23.7
22.4
28.8



1234yf
mass %

21.0
36.8
29.7
19.5
40.3
26.9



R134a
mass %

35.3
15.1
20.5
37.8
18.3
25.3















GWP
Year
3922
1500
1364
1500
1500
1176
1500
















Perfor-
Coefficient of
(relative to
100
108.86
106.97
107.22
109.13
107.75
107.75


mance
performance
R404A %)



Refrigerating
(relative to
100
90
95
95
89
92
93



capacity
R404A %)



Outlet
° C.
93
114
108
110
115
109
111



temperature















ASHRAE

Non-
Non-
Non-
Non-
Non-
Non-
Non-


non-flammability

flam-
flam-
flam-
flam-
flam-
flam-
flam-




mable
mable
mable
mable
mable
mable
mable


























TABLE 6-11










Compar-
Compar-


Compar-








ative
ative
Exam-
Exam-
ative
Exam-
Exam-
Exam-




Compar-
Example
Example
ple
ple
Example
ple
ple
ple




ative
3-62
3-63
3-72
3-73
3-64
3-74
3-75
3-76


Item
Unit
Example
A
D
G′
H′
I′
L
M = R
O





















Compo-
R32
mass %
R404A
19.3
19.3
19.3
19.3
19.3
19.3
19.3
19.3


sition
R125
mass %

39.0
10.4
33.9
20.6
1.1
19.0
24.2
28.1



1234yf
mass %

41.7
0.0
34.1
41.0
0.0
37.8
20.0
37.1



R134a
mass %

0.0
70.3
12.7
19.1
79.6
23.9
36.5
15.5

















GWP
Year
3922
1500
1500
1500
1126
1307
1139
1500
1337


















Perfor-
Coefficient of
(relative to
100
104.98
112.75
106.40
107.98
113.96
108.44
109.01
107.11


mance
performance
R404A %)



Refrigerating
(relative to
100
102
79
98
91
75
90
90
95



capacity
R404A %)



Outlet
° C.
93
104
124
108
109
126
111
115
109



temperature

















ASHRAE

Non-
Flam-
Non-
Non-
Non-
Non-
Non-
Non-
Non-


non-flammability

flam-
mable
flam-
flam-
flam-
flam-
flam-
flam-
flam-




mable

mable
mable
mable
mable
mable
mable
mable























Exam-
Exam-
Exam-
Exam-






Compar-
ple
ple
ple
ple






ative
3-77
3-78
3-79
3-80



Item

Unit
Example
P
Q
S
T




















Compo-
R32
mass %
R404A
19.3
19.3
19.3
19.3



sition
R125
mass %

30.2
14.0
22.5
28.8




1234yf
mass %

28.7
27.2
40.1
26.8




R134a
mass %

21.8
39.5
18.1
25.1













GWP
Year
3922
1500
1186
1178
1500
















Perfor-
Coefficient of
(relative to
100
107.40
109.93
107.75
107.75



mance
performance
R404A %)




Refrigerating
(relative to
100
95
86
92
94




capacity
R404A %)




Outlet
° C.
93
111
115
109
112




temperature













ASHRAE

Non-
Non-
Non-
Non-
Non-


non-flammability

flam-
flam-
flam-
flam-
flam-




mable
mable
mable
mable
mable


























TABLE 6-12










Compar-
Compar-


Compar-

Compar-






ative
ative
Exam-
Exam-
ative
Exam-
ative
Exam-




Compar-
Example
Example
ple
ple
Example
ple
Example
ple




ative
3-65
3-66
3-81
3-82
3-67
3-83
3-68
3-84


Item
Unit
Example
A
D
G′
H′
I′
L
M
O





















Compo-
R32
mass %
R404A
20.0
20.0
20.0
20.0
20.0
20.0
20.0
20.0


sition
R125
mass %

38.9
10.7
33.8
21.2
1.8
18.0
23.0
25.9



1234yf
mass %

41.1
0.0
33.7
40.4
0.0
33.9
17.9
37.9



R134a
mass %

0.0
69.3
12.5
18.4
78.2
28.1
39.1
16.2

















GWP
Year
3922
1500
1500
1500
1142
1316
1168
1500
1275


















Perfor-
Coefficient of
(relative to
100
105.06
112.70
106.46
107.94
113.85
108.87
109.37
107.41


mance
performance
R404A %)



Refrigerating
(relative to
100
103
80
99
93
76
90
90
95



capacity
R404A %)



Outlet
° C.
93
105
125
109
110
127
113
117
110



temperature

















ASHRAE

Non-
Flam-
Non-
Non-
Non-
Non-
Non-
Non-
Non-


non-flammability

flam-
mable
flam-
flam-
flam-
flam-
flam-
flam-
flam-




mable

mable
mable
mable
mable
mable
mable
mable




















Exam-
Exam-
Exam-
Exam-
Exam-




Compar-
ple
ple
ple
ple
ple




ative
3-85
3-86
3-87
3-88
3-89


Item
Unit
Example
P = T
Q
R
S
Y


















Compo-
R32
mass %
R404A
20.0
20.0
20.0
20.0
20.0


sition
R125
mass %

28.9
15.4
25.2
22.8
21.0



1234yf
mass %

26.5
28.3
21.1
39.6
24.2



R134a
mass %

24.6
36.3
33.7
17.6
34.8














GWP
Year
3922
1500
1194
1500
1186
1369















Perfor-
Coefficient of
(relative to
100
107.75
109.65
108.78
107.75
109.16


mance
performance
R404A %)



Refrigerating
(relative to
100
95
88
92
93
90



capacity
R404A %)



Outlet
° C.
93
112
115
115
110
115



temperature














ASHRAE

Non-
Non-
Non-
Non-
Non-
Non-


non-flammability

flam-
flam-
flam-
flam-
flam-
flam-




mable
mable
mable
mable
mable
mable


























TABLE 6-13










Compar-
Compar-


Compar-

Compar-






ative
ative
Exam-
Exam-
ative
Exam-
ative
Exam-




Compar-
Example
Example
ple
ple
Example
ple
Example
ple




ative
3-69
3-70
3-90
3-91
3-71
3-92
3-72
3-93


Item
Unit
Example
A
D
G′
H′
I′
L = Q
M
O = S





















Compo-
R32
mass %
R404A
20.8
20.8
20.8
20.8
20.8
20.8
20.8
20.8


sition
R125
mass %

38.7
11.0
33.8
21.8
2.7
16.9
21.6
23.0



1234yf
mass %

40.5
0.0
33.3
39.7
0.0
29.5
15.5
39.2



R134a
mass %

0.0
68.2
12.1
17.7
76.5
32.8
42.1
17.0

















GWP
Year
3922
1500
1500
1500
1158
1329
1202
1500
1190


















Perfor-
Coefficient of
(relative to
100
105.15
112.64
106.50
107.91
113.71
109.35
109.77
107.76


mance
performance
R404A %)



Refrigerating
(relative to
100
105
81
101
94
77
90
90
95



capacity
R404A %)



Outlet
° C.
93
106
126
109
111
127
115
118
111



temperature

















ASHRAE

Non-
Flam-
Non-
Non-
Non-
Non-
Non-
Non-
Non-


non-flammability

flam-
mable
flam-
flam-
flam-
flam-
flam-
flam-
flam-




mable

mable
mable
mable
mable
mable
mable
mable






















Exam-
Exam-
Exam-






Compar-
ple
ple
ple






ative
3-94
3-95
3-96



Item

Unit
Example
P
R
T



















Compo-
R32
mass %
R404A
20.8
20.8
20.8



sition
R125
mass %

27.5
26.3
29.1




1234yf
mass %

24.1
22.4
26.4




R134a
mass %

27.6
30.5
23.7












GWP
Year
3922
1500
1500
1500















Perfor-
Coefficient of
(relative to
100
108.19
108.51
107.76



mance
performance
R404A %)




Refrigerating
(relative to
100
95
94
96




capacity
R404A %)




Outlet
° C.
93
114
115
113




temperature












ASHRAE

Non-
Non-
Non-
Non-


non-flammability

flam-
flam-
flam-
flam-




mable
mable
mable
mable


























TABLE 6-14










Compar-
Compar-


Compar-








ative
ative
Exam-
Exam-
ative
Exam-
Exam-
Exam-




Compar-
Example
Example
ple
ple
Example
ple
ple
ple




ative
3-73
3-74
3-97
3-98
3-75
3-99
3-100
3-101


Item
Unit
Example
A
D
G′
H′ = O
I′
P = R
Q
S





















Compo-
R32
mass %
R404A
21.2
21.2
21.2
21.2
21.2
21.2
21.2
21.2


sition
R125
mass %

38.7
11.1
33.8
22.2
31
26.8
17.7
23.3



1234yf
mass %

40.1
0.0
33.0
39.3
0.0
22.9
30.0
38.8



R134a
mass %

0.0
67.7
11.9
17.3
75.7
29.1
31.1
16.7

















GWP
Year
3922
1500
1500
1500
1169
1334
1500
1228
1199


















Perfor-
Coefficient of
(relative to
100
105.19
112.62
106.52
107.88
113.65
108.39
108.70
107.75


mance
performance
R404A %)



Refrigerating
(relative to
100
105
82
101
95
78
95
95
96



capacity
R404A %)



Outlet
° C.
93
106
126
110
111
128
115
115
111



temperature

















ASHRAE

Non-
Flam-
Non-
Non-
Non-
Non-
Non-
Non-
Non-


non-flammability

flam-
mable
flam-
flam-
flam-
flam-
flam-
flam-
flam-




mable

mable
mable
mable
mable
mable
mable
mable




















Exam-






Compar-
ple






ative
3-102



Item

Unit
Sample
T

















Compo-
R32
mass %
R404A
21.2



sition
R125
mass %

29.1




1234yf
mass %

26.3




R134a
mass %

23.4










GWP
Year
3922
1500













Perfor-
Coefficient of
(relative to
100
107.75



mance
performance
R404A %)




Refrigerating
(relative to
100
97




capacity
R404A %)




Outlet
° C.
93
113




temperature










ASHRAE

Non-
Non-


non-flammability

flam-
flam-




mable
mable


























TABLE 6-15










Compar-
Compar-


Compar-








ative
ative
Exam-
Exam-
ative
Exam-
Exam-
Exam-




Compar-
Example
Example
ple
ple
Example
ple
ple
ple




ative
3-76
3-77
3-103
3-104
3-78
3-105
3-106
3-107


Item
Unit
Example
A
D
G′
H′
I′
O
P
Q





















Compo-
R32
mass %
R404A
21.6
21.6
21.6
21.6
21.6
21.6
21.6
21.6


sition
R125
mass %

38.6
11.2
33.8
22.5
3.5
21.5
26.1
18.5



1234yf
mass %

39.8
0.0
32.9
38.9
0.0
36.7
21.6
30.5



R134a
mass %

0.0
67.2
11.7
17.0
74.9
20.2
30.7
29.4

















GWP
Year
3922
1500
1500
1500
1178
1339
1189
1500
1215


















Perfor-
Coefficient of
(relative to
100
105.23
112.60
106.54
107.86
107.86
108.17
108.60
109.05


mance
performance
R404A %)



Refrigerating
(relative to
100
106
82
102
96
79
95
95
92



capacity
R404A %)



Outlet
° C.
93
107
127
110
111
128
112
116
115



temperature

















ASHRAE

Non-
Flam-
Non-
Non-
Non-
Non-
Non-
Non-
Non-


non-flammability

flam-
mable
flam-
flam-
flam-
flam-
flam-
flam-
flam-




mable

mable
mable
mable
mable
mable
mable
mable























Exam-
Exam-
Exam-
Exam-






Compar-
ple
ple
ple
ple






ative
3-108
3-109
3-110
3-111



Item

Unit
Example
R
S
T
Z




















Compo-
R32
mass %
R404A
21.6
21.6
21.6
21.6



sition
R125
mass %

27.4
23.4
29.1
24.9




1234yf
mass %

23.5
38.5
26.2
25.5




R134a
mass %

27.5
16.5
23.1
28.0













GWP
Year
3922
1500
1202
1500
1419
















Perfor-
Coefficient of
(relative to
100
108.25
107.75
107.75
108.48



mance
performance
R404A %)




Refrigerating
(relative to
100
96
96
98
95




capacity
R404A %)




Outlet
° C.
93
115
111
114
115




temperature













ASHRAE

Non-
Non-
Non-
Non-
Non-


non-flammability

flam-
flam-
flam-
flam-
flam-




mable
mable
mable
mable
mable


























TABLE 6-16










Compar-
Compar-


Compar-

Compar-






ative
ative
Exam-
Exam-
ative
Exam-
ative
Exam-




Compar-
Example
Example
ple
ple
Example
ple
Example
ple




ative
3-79
3-80
3-112
3-113
3-81
3-114
3-82
3-115


Item
Unit
Example
A
D
G′
H′
I′
O = Q
P
R





















Compo-
R32
mass %
R404A
22.6
22.6
22.6
22.6
22.6
22.6
22.6
22.6


sition
R125
mass %

38.4
11.6
33.8
23.3
4.6
20.3
24.5
28.8



1234yf
mass %

39.0
0.0
32.3
38.0
0.0
31.7
18.7
25.0



R134a
mass %

0.0
65.8
11.3
16.1
72.8
25.4
34.2
23.6

















GWP
Year
3922
1500
1500
1500
1200
1355
1228
1500
1500


















Perfor-
Coefficient of
(relative to
100
105.34
112.52
106.60
107.81
113.42
108.70
109.07
107.93


mance
performance
R404A %)



Refrigerating
(relative to
100
108
84
104
98
81
95
95
99



capacity
R404A %)



Outlet
° C.
93
108
127
111
112
129
115
118
115



temperature

















ASHRAE

Non-
Flam-
Non-
Non-
Non-
Non-
Non-
Non-
Non-


non-flammability

flam-
mable
flam-
flam-
flam-
flam-
flam-
flam-
flam-




mable

mable
mable
mable
mable
mable
mable
mable

















Exam-
Exam-

Compar-



Compar-
ple
ple
Exam-
ative



ative
3-116
3-117
ple
Example













Item
Unit
Example
S
T
3-118
3-83

















Compo-
R32
mass %
R404A
22.6
22.6
22.6
22.6


sition
R125
mass %

23.8
29.3
25.0
15.0



1234yf
mass %

37.7
26.0
32.4
42.4



R134a
mass %

159
22.1
20.0
20.0













GWP
Year
3922
1214
1500
1315
1425














Perfor-
Coefficient of
(relative to
100
107.75
107.75
107.96
114.07


mance
performance
R404A %)



Refrigerating
(relative to
100
98
99
98
91



capacity
R404A %)



Outlet
° C.
93
112
115
114
117



temperature













ASHRAE

Non-
Non-
Non-
Non-
Flam-


non-flammability

flam-
flam-
flam-
flam-
mable




mable
mable
mable
mable


























TABLE 6-17










Compar-
Compar-


Compar-
Compar-
Compar-






ative
ative
Exam-
Exam-
ative
ative
ative
Exam-




Compar-
Example
Example
ple
ple
Example
Example
Example
ple




ative
3-84
3-85
3-119
3-120
3-86
3-87
3-88
3-121


Item
Unit
Example
A
D
G′
H′
I′
O
P
Q





















Compo-
R32
mass %
R404A
23.2
23.2
23.2
23.2
23.2
23.2
23.2
23.2


sition
R125
mass %

38.3
11.8
33.8
23.8
5.2
19.5
23.5
21.3



1234yf
mass %

38.5
0.0
32.0
37.4
0.0
28.8
17.0
32.4



R134a
mass %

0.0
65.0
11.0
15.6
71.6
28.5
36.3
23.1

















GWP
Year
3922
1500
1500
1500
1214
1362
1248
1500
1234


















Perfor-
Coefficient of
(relative to
100
105.40
112.48
106.62
107.79
113.33
109.03
109.35
108.51


mance
performance
R404A %)



Refrigerating
(relative to
100
109
85
105
99
82
95
95
97



capacity
R404A %)



Outlet
° C.
93
108
128
112
113
129
117
120
115



temperature

















ASHRAE

Non-
Flam-
Non-
Non-
Non-
Non-
Non-
Non-
Non-


non-flammability

flam-
mable
flam-
flam-
flam-
flam-
flam-
flam-
flam-




mable

mable
mable
mable
mable
mable
mable
mable

















Exam-
Exam-

Compar-



Compar-
ple
ple
Exam-
ative



ative
3-122
3-123
ple
Example













Item
Unit
Sample
R = T
S
3-124
3-89

















Compo-
R32
mass %
R404A
23.2
23.2
23.2
23.2


sition
R125
mass %

29.6
23.8
25.0
15.0



1234yf
mass %

25.8
37.4
31.8
41.8



R134a
mass %

21.4
15.6
20.0
20.0













GWP
Year
3922
1500
1214
1319
969














Perfor-
Coefficient of
(relative to
100
107.75
107.75
108.00
108.75


mance
performance
R404A %)



Refrigerating
(relative to
100
101
99
99
95



capacity
R404A %)



Outlet
° C.
93
115
113
114
114



temperature













ASHRAE

Non-
Non-
Non-
Non-
Flam-


non-flammability

flam-
flam-
flam-
flam-
mable




mable
mable
mable
mable


























TABLE 6-18










Compar-
Compar-


Compar-
Compar-
Compar-






ative
ative
Exam-
Exam-
ative
ative
ative
Exam-




Compar-
Example
Example
ple
ple
Example
Example
Example
ple




ative
3-90
3-91
3-125
3-126
3-92
3-93
3-94
3-127


Item
Unit
Example
A
D
G′
H′
I′
O
P
Q





















Compo-
R32
mass %
R404A
24.7
24.7
24.7
24.7
24.7
24.7
24.7
24.7


sition
R125
mass %

38.1
12.3
33.9
24.9
6.6
17.8
21.3
24.0



1234yf
mass %

37.2
0.0
31.1
36.0
0.0
22.0
13.0
34.2



R134a
mass %

0.0
63.0
10.3
14.4
68.7
35.5
41.0
17.1

















GWP
Year
3922
1500
1500
1500
1270
1403
1298
1500
1253


















Perfor-
Coefficient of
(relative to
100
105.55
112.38
106.73
107.67
112.97
109.77
109.99
107.98


mance
performance
R404A %)



Refrigerating
(relative to
100
111
87
107
102
85
95
95
101



capacity
R404A %)



Outlet
° C.
93
110
129
113
114
130
121
123
115



temperature

















ASHRAE

Non-
Flam-
Non-
Non-
Non-
Non-
Non-
Non-
Non-


non-flammability

flam-
mable
flam-
flam-
flam-
flam-
flam-
flam-
flam-




mable

mable
mable
mable
mable
mable
mable
mable























Exam-
Exam-
Exam-
Exam-






Compar-
ple
ple
ple
ple






ative
3-128
3-129
3-130
3-131



Item

Unit
Example
R
S
T
α




















Compo-
R32
mass %
R404A
24.7
24.7
24.7
24.7



sition
R125
mass %

31.6
24.8
29.8
26.6




1234yf
mass %

27.8
35.8
25.2
32.1




R134a
mass %

15.9
14.7
20.3
16.6













GWP
Year
3922
1500
1246
1500
1336
















Perfor-
Coefficient of
(relative to
100
107.29
107.75
107.75
107.75



mance
performance
R404A %)




Refrigerating
(relative to
100
105
102
103
103




capacity
R404A %)




Outlet
° C.
93
115
114
116
115




temperature













ASHRAE

Non-
Non-
Non-
Non-
Non-


non-flammability

flam-
flam-
flam-
flam-
flam-




mable
mable
mable
mable
mable


























TABLE 6-19










Compar-
Compar-


Compar-
Compar-
Compar-






ative
ative
Exam-
Exam-
ative
ative
ative
Exam-




Compar-
Example
Example
ple
ple
Example
Example
Example
ple




ative
3-95
3-96
3-132
3-133
3-97
3-98
3-99
3-134


Item
Unit
Example
A
D
G′
H′
I′
O
P
Q = S





















Compo-
R32
mass %
R404A
25.4
25.4
25.4
25.4
25.4
25.4
25.4
25.4


sition
R125
mass %

37.9
12.6
33.9
25.4
7.3
17.1
20.3
25.2



1234yf
mass %

36.7
0.0
30.7
35.3
0.0
19.1
11.2
35.0



R134a
mass %

0.0
62.0
10.0
13.9
67.3
38.4
43.1
14.4

















GWP
Year
3922
1500
1500
1500
1261
1389
1320
1500
1261


















Perfor-
Coefficient of
(relative to
100
105.63
112.32
106.72
107.70
113.00
110.08
110.27
107.75


mance
performance
R404A %)



Refrigerating
(relative to
100
112
88
108
104
85
95
95
103



capacity
R404A %)



Outlet
° C.
93
111
130
114
115
131
122
124
115



temperature

















ASHRAE

Non-
Flam-
Non-
Non-
Non-
Non-
Non-
Non-
Non-


non-flammability

flam-
mable
flam-
flam-
flam-
flam-
flam-
flam-
flam-




mable

mable
mable
mable
mable
mable
mable
mable






















Compar-







Exam-
ative






Compar-
ple
Example






ative
3-135
3-100



Item

Unit
Example
R
T


















Compo-
R32
mass %
R404A
25.4
25.4



sition
R125
mass %

32.3
29.9




1234yf
mass %

28.6
25.1




R134a
mass %

13.7
19.6











GWP
Year
3922
1500
1500














Perfor-
Coefficient of
(relative to
100
107.12
107.75



mance
performance
R404A %)




Refrigerating
(relative to
100
107
104




capacity
R404A %)




Outlet
° C.
93
115
117




temperature











ASHRAE

Non-
Non-
Non-


non-flammability

flam-
flam-
flam-




mable
mable
mable


























TABLE 6-20










Compar-
Compar-


Compar-
Compar-
Compar-






ative
ative
Exam-
Exam-
ative
ative
ative
Exam-




Compar-
Example
Example
ple
ple
Example
Example
Example
ple




ative
3-101
3-102
3-136
3-137
3-103
3-104
3-105
3-138


Item
Unit
Example
A
D
G′
H′ = Q
I′
O
P
R





















Compo-
R32
mass %
R404A
25.6
25.6
25.6
25.6
25.6
25.6
25.6
25.6


sition
R125
mass %

37.9
12.6
33.9
25.6
7.5
16.9
20.0
32.5



1234yf
mass %

36.5
0.0
30.6
35.1
0.0
18.3
10.6
28.8



R134a
mass %

0.0
61.8
9.9
13.7
66.9
39.2
43.8
13.1

















GWP
Year
3922
1500
1500
1500
1266
1392
1326
1500
1500


















Perfor-
Coefficient of
(relative to
100
105.64
112.31
106.72
107.68
112.97
110.17
110.36
107.08


mance
performance
R404A %)



Refrigerating
(relative to
100
113
88
109
104
86
95
95
107



capacity
R404A %)



Outlet
° C.
93
111
130
114
115
131
123
125
115



temperature

















ASHRAE

Non-
Flam-
Non-
Non-
Non-
Non-
Non-
Non-
Non-


non-flammability

flam-
mable
flam-
flam-
flam-
flam-
flam-
flam-
flam-




mable

mable
mable
mable
mable
mable
mable
mable





















Compar-
Compar-







ative
ative






Compar-
Example
Example






ative
3-106
3-107



Item

Unit
Example
S
T


















Compo-
R32
mass %
R404A
25.6
25.6



sition
R125
mass %

25.3
29.9




1234yf
mass %

34.8
25.0




R134a
mass %

14.3
19.5











GWP
Year
3922
1264
1500














Perfor-
Coefficient of
(relative to
100
107.75
107.75



mance
performance
R404A %)




Refrigerating
(relative to
100
104
105




capacity
R404A %)




Outlet
° C.
93
115
117




temperature











ASHRAE

Non-
Non-
Non-


non-flammability

flam-
flam-
flam-




mable
mable
mable


























TABLE 6-21










Compar-
Compar-

Compar-
Compar-
Compar-
Compar-
Compar-





ative
ative
Exam-
ative
ative
ative
ative
ative




Compar-
Example
Example
ple
Example
Example
Example
Example
Example




ative
3-108
3-109
3-139
3-110
3-111
3-112
3-113
3-114


Item
Unit
Example
A
D
G′ = Q = R
H′
I′
O
P
S





















Compo-
R32
mass %
R404A
26.6
26.6
26.6
26.6
26.6
26.6
26.6
26.6


sition
R125
mass %

37.7
13.0
33.8
26.3
8.6
16.0
18.6
25.8



1234yf
mass %

35.7
0.0
30.1
34.2
0.0
14.4
8.1
33.5



R134a
mass %

0.0
60.4
9.5
12.9
64.8
43.0
46.7
14.1

















GWP
Year
3922
1500
1500
1500
1286
1407
1355
1500
1286


















Perfor-
Coefficient of
(relative to
100
105.75
112.23
106.78
107.64
112.80
110.58
110.75
107.75


mance
performance
R404A %)



Refrigerating
(relative to
100
114
90
110
106
88
95
95
105



capacity
R404A %)



Outlet
° C.
93
112
131
115
116
132
125
127
116



temperature

















ASHRAE

Non-
Flam-
Non-
Non-
Non-
Non-
Non-
Non-
Non-


non-flammability

flam-
mable
flam-
flam-
flam-
flam-
flam-
flam-
flam-




mable

mable
mable
mable
mable
mable
mable
mable




















Compar-







ative






Compar-
Example






ative
3-115



Item

Unit
Example
T

















Compo-
R32
mass %
R404A
26.6



sition
R125
mass %

29.9




1234yf
mass %

24.4




R134a
mass %

19.1










GWP
Year
3922
1500













Perfor-
Coefficient of
(relative to
100
107.75



mance
performance
R404A %)




Refrigerating
(relative to
100
106




capacity
R404A %)




Outlet
° C.
93
118




temperature










ASHRAE

Non-
Non-


non-flammability

flam-
flam-




mable
mable









Examples 3-52 and 3-124, and Comparative Examples 3-51 and 3-89

The flammability of Examples 3-52 and 3-124, and Comparative Examples 3-51 and 3-89 was examined according to ASHRAE34-2013.


In order to determine WCFF, leak calculations were performed for the following seven cases using REFPROP 9.0.


Storage/Shipping Condition


Leak temperature: (1) boiling point+10° C. (because the boiling point+10° C. is higher than −40° C.), (2) 23° C., (3) 54.4° C.


Equipment Condition


Leak temperature: (4) boiling point+10° C. (because the boiling point+10° C. is higher than −40° C.), (5) 23° C., (6) 60° C.


Leak/Recharge Testing


Leak temperature: (7) 23±3° C.


Tables 7 and 8 show the results. In all cases, the vapor phase during cylinder-filling at (1) boiling point+10° C. was WCFF under the storage/shipping condition.


















TABLE 7





Example








Flammability determination


Comparative

R32
R125
1234yf
R134a



from non-flammability limit


Example
Refrigerant
(wt %)
(wt %)
(wt %)
(wt %)
(2)
(4)
(2) − (4)
of binary mixed refrigerant







Example
Composition
18.0
20.0
32.0
30.0






3-52
WCFF
34.0
27.0
23.2
15.8
  7.032
−0.686
  7.717
Non-flammable



(−33.9° C. (boiling point + 10° C.)



storage/shipping condition)


Comparative
Composition
18.0
10.0
52.0
20.0






Example
WCFF
37.5
13.8
37.4
11.3
−11.62
18.56 
−30.18
Flammable


3-51
(−31.3° C. (boiling point + 10° C.)



storage/shipping condition)

























TABLE 8





Example








Flammability determination


Comparative

R32
R125
1234yf
R134a



from non-flammability limit


Example
Refrigerant
(wt %)
(wt %)
(wt %)
(wt %)
(2)
(4)
(2) − (4)
of binary mixed refrigerant
























Example
Composition
23.2
25.0
31.8
20.0






3-124
WCFF
39.0
30.4
21.3
9.3
 7.495
 1.629
  5.867
Non-flammable



(−36.2° C. (boiling point + 10° C.)



storage/shipping condition)


Comparative
Composition
23.2
15.0
41.8
20.0






Example
WCFF
42.3
19.1
28.8
9.8
−7.85
12.96
−20.81
Flammable


3-89
(−35.6° C. (boiling point + 10° C.)



storage/shipping condition)









When a combustion test was conducted according to ASTM E681 (a standard test method for concentration limits of flammability) for the WCFF shown in Examples 3-52 and 3-124, and Comparative Examples 3-51 and 3-89, flame propagation was not observed in the WCFF compositions of the Examples, and flame propagation was observed in the WCFF compositions of the Comparative Examples.


The results showed that the Examples were classified as being ASHRAE non-flammable (Class 1), and the Comparative Examples were classified as being ASHRAE flammable (Class 2 or 3).


REFERENCE SIGNS LIST



  • A: Composition ratio in which GWP=1500 and the concentration (wt %) of R134a is 0 wt %

  • D: Composition ratio in which GWP=1500 and the concentration (wt %) of 1234yf is 0 wt %

  • G: Composition ratio in which GWP=1500 and which shows an ASHRAE non-flammability limit (when the WCFF becomes a liquid phase composition after 95% leak under the storage/shipping conditions)

  • H: Composition ratio showing an ASHRAE non-flammability limit (when the WCFF becomes a liquid phase composition after 95% leak under the storage/shipping conditions, and becomes a vapor phase composition at the time of 0% leak)

  • I: Composition ratio showing an ASHRAE non-flammability limit, in which the concentration (wt %) of 1234yf is 0 wt % (the WCFF is a vapor phase composition at the time of 0% leak under the storage/shipping conditions)

  • G′: Composition ratio showing an intersection of a line segment in which GWP=1500 and a line segment obtained by adding 1 wt % of non-flammable refrigerant R134a to line segment GH, which shows an ASHRAE non-flammability limit, in order to take into consideration safety ratio of non-flammability

  • H′: Composition ratio showing an intersection of a line segment obtained by adding 1 wt % of non-flammable refrigerant R134a to line segment GH, which shows an ASHRAE non-flammability limit, and a line segment obtained by adding 1 wt % of non-flammable refrigerant R125 to line segment HI

  • I′: Composition ratio on a line segment obtained by adding 1 wt % of non-flammable refrigerant R125 to line segment HI, which shows an ASHRAE non-flammability limit, in order to take into consideration safety ratio of non-flammability, in which the concentration (wt %) of 1234yf is 0 wt %

  • B: Composition ratio present on line segments G′H′I′, in which the compressor outlet pressure is 102.5% of the R22 pressure

  • C: Composition ratio in which GWP=1500 and the compressor outlet pressure is 102.5% of the R22 pressure

  • E: Composition ratio present on line segments G′H′I′, in which the compressor outlet pressure is 97.5% of the R22 pressure

  • F: Composition ratio in which GWP=1500 and the compressor outlet pressure is 97.5% of the R22 pressure

  • B′: Composition ratio present on line segments G′H′I′, in which the compressor outlet pressure is 101.25% of the R22 pressure

  • C′: Composition ratio in which GWP=1500 and the compressor outlet pressure is 101.25% of the R22 pressure

  • E′: Composition ratio present on line segments G′H′I′, in which the compressor outlet pressure is 98.75% of the R22 pressure

  • F′: Composition ratio in which GWP=1500 and the compressor outlet pressure is 98.75% of the R22 pressure

  • J: Composition ratio present on line segments G′H′I′, in which the refrigerating capacity relative to that of R404 is 85%

  • K: Composition ratio in which GWP=1500 and the refrigerating capacity relative to that of R404 is 85%

  • L: Composition ratio present on line segments G′H′I′, in which the refrigerating capacity relative to that of R404 is 90%

  • M: Composition ratio in which GWP=1500 and the refrigerating capacity relative to that of R404 is 90%

  • O: Composition ratio present on line segments G′H′I′, in which the refrigerating capacity relative to that of R404 is 95%

  • P: Composition ratio in which GWP=1500 and the refrigerating capacity relative to that of R404 is 95%

  • Q: Composition ratio present on line segments G′H′I′, in which the compressor outlet temperature is 115° C.

  • R: Composition ratio in which GWP=1500 and the compressor outlet temperature is 115° C.

  • S: Composition ratio present on line segments G′H′I′, in which COP is 107.75% of that of R404A

  • T: Composition ratio in which GWP=1500, and COP is 107.75% of that of R404A

  • U: Intersection of line segment ST and line segment JK

  • V: Intersection of line segment ST and line segment LM

  • W: Intersection of line segment ST and line segment OP

  • X: Intersection of line segment QR and line segment JK

  • Y: Intersection of line segment OR and line segment LM

  • Z: Intersection of line segment QR and line segment OP

  • α: Intersection of line segment ST and line segment QR

  • N: Point in which R125=0 and R134a=0 (0/0/100−x)


Claims
  • 1. A composition comprising a mixture or mixtures of fluorinated hydrocarbons; the composition comprising at least one member selected from the group consisting of the following mixtures 1 to 6, wherein the composition ratio of the fluorinated hydrocarbons contained in each mixture is indicated in a ternary composition diagram in which the sum of the concentrations of R125, 1234yf, and R134a is represented by (100−x) wt %, when the sum of the concentrations of R32, R125, 1234yf, and R134a is 100 wt %, and the concentration of R32 is x wt %:mixture 1 having a composition ratio in which
  • 2. A composition comprising a mixture or mixtures of fluorinated hydrocarbons; the composition comprising at least one member selected from the group consisting of the following mixtures 1 to 6, wherein the composition ratio of the fluorinated hydrocarbons contained in each mixture is indicated in a ternary composition diagram in which the sum of the concentrations of R125, 1234yf, and R134a is represented by (100−x) wt %, when the sum of the concentrations of R32, R125, 1234yf, and R134a is 100 wt %, and the concentration of R32 is x wt %:mixture 1 having a composition ratio in which
  • 3. A composition comprising a mixture or mixtures of fluorinated hydrocarbons; the composition comprising at least one member selected from the group consisting of the following mixtures 1 to 7, wherein the composition ratio of the fluorinated hydrocarbons contained in each mixture is indicated in a ternary composition diagram in which the sum of the concentrations of R125, 1234yf, and R134a is represented by (100−x) wt %, when the sum of the concentrations of R32, R125, 1234yf, and R134a is 100 wt %, and the concentration of R32 is x wt %:mixture 1 having a composition ratio in which
  • 4. A composition comprising a mixture or mixtures of fluorinated hydrocarbons, the composition comprising at least one member selected from the group consisting of the following mixtures 1 to 9, wherein the composition ratio of the fluorinated hydrocarbons contained in each mixture is indicated in a ternary composition diagram in which the sum of the concentrations of R125, 1234yf, and R134a is represented by (100−x) wt %, when the sum of the concentrations of R32, R125, 1234yf, and R134a is 100 wt %, and the concentration of R32 is x wt %:mixture 1 having a composition ratio in which
  • 5. A composition comprising a mixture or mixtures of fluorinated hydrocarbons; the composition comprising at least one member selected from the group consisting of the following mixtures 1 to 7, wherein the composition ratio of the fluorinated hydrocarbons contained in each mixture is indicated in a ternary composition diagram in which the sum of the concentrations of R125, 1234yf, and R134a is represented by (100−x) wt %, when the sum of the concentrations of R32, R125, 1234yf, and R134a is 100 wt %, and the concentration of R32 is x wt %:mixture 1 having a composition ratio in which
  • 6. A composition comprising a mixture of fluorinated hydrocarbons, the mixture comprising R32, R125, R134a, 1234yf, and at least one fluorinated hydrocarbon selected from the group consisting of HCFC-1122, HCFC-124, CFC-1113, and 3,3,3-trifluoropropyne; wherein the content of other components different from the four basic components R32, R125, 1234yf, and R134a in the mixture is 0.5 wt % or less.
  • 7. A composition comprising a mixture of fluorinated hydrocarbons, the mixture comprising R32, R125, R134a, 1234yf, and at least one halogenated organic compound represented by formula (1): CmHnXp, wherein each X independently represents a fluorine atom, a chlorine atom, or a bromine atom, m is 1 or 2, 2m+2≥n+p, and p≥1; wherein the content of other components different from the four basic components R32, R125, 1234yf, and R134a in the mixture is 0.5 wt % or less.
  • 8. A composition comprising a mixture of fluorinated hydrocarbons, the mixture comprising R32, R125, R134a, 1234yf, and at least one organic compound represented by formula (2): CmHnXp, wherein each X independently represents an atom that is not a halogen atom, m is 1 or 2, 2m+2≥n+p, and p≥1; wherein the content of other components different from the four basic components R32, R125, 1234yf, and R134a in the mixture is 0.5 wt % or less.
  • 9. A composition comprising a mixture of fluorinated hydrocarbons, the mixture comprising R32, R125, R134a, 1234yf, and water; wherein the content of other components including water different from the four basic components R32, R125, 1234yf, and R134a in the mixture is 0.5 wt % or less.
  • 10. The composition according to claim 1, comprising a refrigerant oil.
  • 11. The composition according to claim 10, wherein the refrigerant oil comprises at least one polymer selected from the group consisting of polyalkylene glycol (PAG), polyol ester (POE), and polyvinyl ether (PVE).
  • 12. The composition according to claim 1, wherein the composition is an alternative refrigerant for R404A (R125/R134a/R143a=44/4/52 wt %), which is a mixed refrigerant.
  • 13. The composition according to claim 1, wherein the composition is an alternative refrigerant for R22, which is an HCFC refrigerant.
  • 14. The composition according to claim 1, comprising at least one substance selected from the group consisting of tracers, compatibilizers, ultraviolet fluorescence dyes, stabilizers, and polymerization inhibitors.
  • 15. The composition according to claim 1, wherein the composition consists of the mixture of fluorinated hydrocarbons.
  • 16. A refrigeration method comprising the step of operating a refrigeration cycle using the composition according to claim 1.
  • 17. A method for operating a refrigerating device, comprising operating a refrigeration cycle using the composition according to claim 1.
  • 18. A refrigerating device comprising the composition according to claim 1.
  • 19. The composition according to claim 1, which is used for at least one member selected from the group consisting of refrigerators, freezers, water coolers, ice machines, refrigerating showcases, freezing showcases, freezing and refrigerating units, refrigerating devices for freezing and refrigerating warehouses, chillers (chilling units), turbo refrigerators, and screw refrigerators.
Priority Claims (1)
Number Date Country Kind
2015-227938 Nov 2015 JP national
PCT Information
Filing Document Filing Date Country Kind
PCT/JP2016/083873 11/15/2016 WO 00
Publishing Document Publishing Date Country Kind
WO2017/086328 5/26/2017 WO A
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Number Date Country
20180371303 A1 Dec 2018 US