COMPOSITIONS COMPRISING 2,3,3,3-TETRAFLUOROPROPENE

Abstract

The present invention relates to compositions for use in refrigeration, air-conditioning, and heat pump systems wherein the composition comprises a 2,3,3,3-tetrafluoropropene and at least one other component. The compositions of the present invention are useful in processes for producing cooling or heat, as heat transfer fluids, foam blowing agents, aerosol propellants, and fire suppression and fire extinguishing agents.

Claims

1. A refrigerant composition comprising: 10% by weight to 35% by weight of R32; 10% by weight to 35% by weight of R1234yf; 20% by weight to 50% by weight of tetrafluoroethane, and one or more additional compounds selected from 0% to 20% by weight of R125; 0% to 10% by weight of heptafluoropropane; 0% to 10% by weight of difluoroethane; and 0% to 8% by weight of CO2.

2. The refrigerant composition as claimed in claim 1, wherein the composition comprises: 23% by weight to 27% by weight of R32; 28% by weight to 32% by weight of R1234yf; 13% by weight to 17% by weight of R125; 23% by weight to 27% by weight of tetrafluoroethane; 3% by weight to 7% by weight of heptafluoropropane; and 0.5% by weight to 2% by weight of CO2.

3. The refrigerant composition as claimed in claim 1, wherein the composition comprises: 25% by weight to 26% by weight of R32; 30% by weight to 31% by weight of R1234yf; 15% by weight to 16% by weight of R125; 25% by weight to 26% by weight of R134a; and 5% by weight to 6% by weight of R227ea.

4. The refrigerant composition as claimed in claim 1, wherein the composition comprises: 28% by weight to 32% by weight of R32; 12% by weight to 16% by weight of R1234yf; 8% by weight to 12% by weight of R125; 43% by weight to 47% by weight of R134a; and 0.5% by weight to 2% by weight of CO2.

5. The refrigerant composition as claimed in claim 1, wherein the composition comprises: 25% by weight to 30% by weight of R32; 10% by weight to 15% by weight of R1234yf; 8% by weight to 15% by weight of R125; and 40% by weight to 50% by weight of 134a.

6. The refrigerant composition as claimed in claim 1, wherein the composition comprises: 23% by weight to 27% by weight of R32; 28% by weight to 32% by weight of R1234yf; 13% by weight to 17% by weight of R125; 23% by weight to 27% by weight of 134a; and 3% by weight to 7% by weight of R152a.

7. The refrigerant composition as claimed in claim 1, wherein the composition comprises: 30% by weight to 35% by weight of R32; 13% by weight to 17% by weight of R1234yf; 42% by weight to 48% by weight of 134a; and 4% by weight to 6% by weight of R227ea.

8. The refrigerant composition of claim 1 that has a Global Warming Potential of less than 1500.

9. The refrigerant composition compositions of claim 1, wherein the refrigerant composition is a non-azeotropic composition.

10. The refrigerant composition of claim 1, wherein the refrigerant composition is used as a replacement for 404A.

Description

DETAILED DESCRIPTION OF THE INVENTION

[0034] The term “tetrafluoroethane” as used herein in the present invention refers to either 1,1,2,2-tetrafluoroethane or 1,1,1,2-tetrafluoroethane.

[0035] The term “difluoroethane” as used herein in the present invention refers to either 1,1-difluoroethane or 1,2-difluoroethane.

[0036] The term “heptafluoropropane” as used herein in the present invention refers to either 1,1,1,2,3,3,3-heptafluoropropane or 1,1,1,2,2,3,3-heptafluoropropane.

[0037] The term “about” as used in the present invention refers to 10% deviation from the specified value in both side.

[0038] The various refrigerants as used in the present invention are described in the Table-1 below.

TABLE-US-00001 TABLE 1 Refrigerant Chemical name Chemical formula R32 Difluoromethane CH.sub.2F.sub.2 R125 Pentafluoroethane CF.sub.3CHF.sub.2 R-134 1,1,2,2-tetrafluoroethane CHF.sub.2CHF.sub.2 R134a 1,1,1,2-tetrafluoroethane CH.sub.2FCF.sub.3 R152a 1,1-difluoroethane CHF.sub.2CH.sub.3 R152 1,2-difluoroethane CH.sub.2FCH.sub.2F R227ea 1,1,1,2,3,3,3-heptafluoropropane CF.sub.3CHFCF.sub.3 R227ca 1,1,1,2,2,3,3-Heptafluoropropane CHF.sub.2CF.sub.2CF.sub.3 R1234yf 2,3,3,3-tetrafluoropropene CF.sub.3CF═CH.sub.2

[0039] In an aspect, the present invention provides a refrigerant composition comprising: [0040] 25% by weight to 35% by weight of R32; [0041] 12% by weight to 30% by weight of R1234yf; [0042] 2% by weight to 15% by weight of R125; [0043] 25% by weight to 48% by weight of tetrafluoroethane; [0044] 0% by weight to 5% by weight of heptafluoropropane; [0045] 0% by weight to 5% by weight of difluoroethane; and [0046] 0% by weight to 2% by weight of CO.sub.2.

[0047] In an embodiment, the present invention provides refrigerant composition comprising: [0048] 20% by weight to 25% by weight of R32; [0049] 25% by weight to 30% by weight of R1234yf; [0050] 10% by weight to 15% by weight of R125; [0051] 25% by weight to 45% by weight of tetrafluoroethane; and [0052] 2% by weight to 5% by weight of heptafluoropropane.

[0053] In another embodiment, the present invention provides a refrigerant composition comprising R32, R1234yf, R125, R134a, and R227ea comprises the steps of: [0054] a) mixing 227ea, 134a and 1234yf to get a mixture; [0055] b) adding R125 and R32 to the mixture of step a), [0056] wherein the mixing is assisted with recirculation or agitators. [0057] The addition of R125 and R32 is preferentially done one by one, i.e., addition of R125 followed by addition of R32.

[0058] In another embodiment, the present invention provides a refrigerant composition 1 (C-1) comprising: [0059] about 25% by weight of R32; [0060] about 30% by weight of R1234yf; [0061] about 15% by weight of R125; [0062] about 25% by weight of tetrafluoroethane; and [0063] about 5% by weight of heptafluoropropane.

[0064] In another embodiment, the present invention provides a refrigerant composition comprising: [0065] 20% by weight to 25% by weight of R32; [0066] 20% by weight to 28% by weight of R1234yf; [0067] 10% by weight to 15% by weight of R125; [0068] 20% by weight to 25% by weight of 134a; [0069] 2% by weight to 5% by weight of 227ea; and [0070] 0.5% by weight to 2% by weight of CO.sub.2.

[0071] In another embodiment, the present invention provides refrigerant composition comprising R32, R1234yf, R125, R134a, R227ea, and carbon dioxide comprises the steps of: [0072] a) mixing 227ea, 134a and 1234yf to get first mixture; [0073] b) adding R125 and R32 to the mixture of step a) to get a second mixture; [0074] c) adding carbon dioxide to the second mixture,

[0075] wherein the mixing is assisted with recirculation or agitators.

[0076] The addition of R125 and R32 is preferentially done one by one, i.e., addition of R125 followed by addition of R32.

[0077] In another embodiment, the present invention provides a refrigerant composition 1a (C-1a) comprising: [0078] about 25% by weight of R32; [0079] about 28% by weight of R1234yf; [0080] about 15% by weight of R125; [0081] about 25% by weight of 134a; [0082] about 5% by weight of 227ea; and [0083] about 2% by weight of CO.sub.2.

[0084] In another embodiment, the present invention provides a refrigerant composition comprising: [0085] 28% by weight to 32% by weight of R32; [0086] 12% by weight to 16% by weight of R1234yf; [0087] 8% by weight to 12% by weight of R125; [0088] 43% by weight to 47% by weight of 134a; and [0089] 0% by weight to 8% by weight of CO.sub.2.

[0090] In another embodiment, the present invention provides refrigerant composition comprising R32, R1234yf, R125, R134a, and carbon dioxide comprises the steps of: [0091] a) mixing 134a and 1234yf to get first mixture; [0092] b) adding R125 and R32 to the mixture of step a) to get a second mixture; [0093] c) adding carbon dioxide to the second mixture, [0094] wherein the mixing is assisted with recirculation or agitators.

[0095] The addition of R125 and R32 is preferentially done one by one, i.e., addition of R125 followed by addition of R32.

[0096] In another embodiment, the present invention provides a refrigerant composition comprising: [0097] 25% by weight to 30% by weight of R32; [0098] 10% by weight to 15% by weight of R1234yf; [0099] 8% by weight to 12% by weight of R125; [0100] 30% by weight to 50% by weight of tetrafluoroethane; and [0101] 2% by weight to 8% by weight of CO.sub.2.

[0102] In another embodiment, the present invention provides a refrigerant composition 2a (C-2a) comprising: [0103] about 28% by weight of R32; [0104] about 15% by weight of R1234yf; [0105] about 10% by weight of R125; [0106] about 45% by weight of 134a; and [0107] about 2% by weight of CO.sub.2.

[0108] In another embodiment, the present invention provides a refrigerant composition comprising: [0109] 25% by weight to 30% by weight of R32; [0110] 10% by weight to 15% by weight of R1234yf; [0111] 8% by weight to 15% by weight of R125; and [0112] 40% by weight to 50% by weight of tetrafluoroethane

[0113] In another embodiment, the present invention provides a refrigerant composition comprising R32, R1234yf, R125, and R134a comprises the steps of: [0114] a) mixing 134a and 1234yf to get first mixture; [0115] b) adding R125 and R32 to the mixture of step a) to get the composition;

[0116] wherein the mixing is assisted with recirculation or agitators.

[0117] The addition of R125 and R32 is preferentially done one by one, i.e., addition of R125 followed by addition of R32.

[0118] In another embodiment, the present invention provides a refrigerant composition comprising: [0119] 25% by weight to 30% by weight of R32; [0120] 10% by weight to 15% by weight of R1234yf; [0121] 8% by weight to 15% by weight of R125; and [0122] 40% by weight to 50% by weight of 134a

[0123] In a particular embodiment, the present invention provides a refrigerant composition 2 (C-2) comprising: [0124] about 30% by weight of R32; [0125] about 15% by weight of R1234yf; [0126] about 10% by weight of R125; and [0127] about 45% by weight of 134a.

[0128] In another embodiment, the present invention provides a refrigerant composition comprising: [0129] 20% by weight to 25% by weight of R32; [0130] 25% by weight to 30% by weight of R1234yf; [0131] 10% by weight to 15% by weight of R125; [0132] 20% by weight to 30% by weight of tetrafluoroethane; and [0133] 2% by weight to 10% by weight of difluoroethane.

[0134] In another embodiment, the present invention provides a refrigerant composition comprising: [0135] 23% by weight to 27% by weight of R32; [0136] 28% by weight to 32% by weight of R1234yf; [0137] 13% by weight to 17% by weight of R125; [0138] 23% by weight to 27% by weight of 134a; and [0139] 3% by weight to 7% by weight of R152a.

[0140] In another embodiment, the present invention provides refrigerant composition comprising R32, R1234yf, R125, R134a, and 152a comprises the steps of: [0141] a) mixing 152a, 134a and 1234yf to get a mixture; [0142] b) adding R125 and R32 to the mixture of step a) to get the composition,

[0143] wherein the mixing is assisted with recirculation or agitators.

[0144] The addition of R125 and R32 is preferentially done one by one, i.e., addition of R125 followed by addition of R32.

[0145] In another embodiment, the present invention provides a refrigerant composition 3 (C-3) comprising: [0146] about 25% by weight of R32; [0147] about 30% by weight of R1234yf; [0148] about 15% by weight of R125; [0149] about 25% by weight of 134a; and [0150] about 5% by weight of R152a.

[0151] In another embodiment, the present invention provides a refrigerant composition comprising: [0152] 30% by weight to 35% by weight of R32; [0153] 12% by weight to 15% by weight of R1234yf; [0154] 42% by weight to 48% by weight of tetrafluoroethane and [0155] 2% by weight to 5% by weight of heptafluoropropane.

[0156] In another embodiment, the present invention provides a refrigerant composition comprising: [0157] 30% by weight to 35% by weight of R32; [0158] 13% by weight to 17% by weight of R1234yf; [0159] 42% by weight to 48% by weight of 134a; and [0160] 4% by weight to 6% by weight of R227ea.

[0161] In another embodiment, the present invention provides refrigerant composition comprising R32, R1234yf, R134a, and R227ea comprises the steps of: [0162] a) mixing 227ea, 134a and 1234yf to get a mixture; [0163] b) adding R32 to the mixture of step a) to get the composition,

[0164] wherein the mixing is assisted with recirculation or agitators.

[0165] In another embodiment, the present invention provides a refrigerant composition 4 (C-4) comprising: [0166] about 33.7% by weight of R32; [0167] about 14.7% by weight of R1234yf; [0168] about 46.6% by weight of 134a and [0169] about 5% by weight of R227ea.

[0170] The compositions of the present invention are preferably non-azeotropic compositions.

[0171] As used herein, a refrigerant is defined as a heat transfer fluid that undergoes a phase change from liquid to gas and back again during a cycle used to transfer of heat.

[0172] The recirculation is carried out using a pump to ensure homogeneity of the composition.

[0173] Non-azeotropic composition is a mixture of two or more substances that behaves as a simple mixture rather than a single substance. One way to characterize a non-azeotropic composition is that the vapor produced by partial evaporation or distillation of the liquid has a substantially different composition as the liquid from which it was evaporated or distilled, that is, the admixture distills/refluxes with substantial composition change.

[0174] The composition of the present invention has lower molecular weight thus has large enthalpy of evaporation. This results in higher cooling capacity. The higher the cooling capacity, the lower will be energy loss across compression and thus higher will be COP value. The comparative data for enthalpy of evaporation is given in Table-2 below.

TABLE-US-00002 TABLE 2 Molar mass (Kg/Kmol) Enthalpy (kj/kg) at −25° C. in at 25° C. in at −25° C. in at 25° C. in Refrigerant vapour phase liquid phase vapour phase liquid phase R404a 97.604 97.604 352.33 236.3 Composition 1 87.488 87.488 386.02 236.8 Composition 2 81.133 81.133 406.65 237.71 Composition 1a 85.403 85.403 388.47 237.24 Composition 2a 79.813 79.813 407.69 238.08 Composition 3 84.083 84.083 395.68 237.51 Composition 4 79.189 79.189 413.29 237.96

[0175] Coefficient of performance (COP) is the amount of heat removed divided by the required energy input to operate the cycle. The higher the COP, the higher is the energy efficiency. COP is directly related to the energy efficiency ratio (EER) that is the efficiency rating for refrigeration or air conditioning equipment at a specific set of internal and external temperatures.

[0176] The composition 2 of the present invention has COP of about 110 to 113.

[0177] The composition 3 of the present invention has COP of about 100 to 105.

[0178] Flammability is a term used to mean the ability of a composition to ignite and/or propagate a flame. Determination of whether a refrigerant compound or mixture is flammable or non-flammable can be done by testing under the conditions of ASTM-681. The compositions of the present invention are mostly non-flammable.

[0179] Global warming potential (GWP) is an index for estimating relative global warming contribution due to atmospheric emission of a kilogram of a particular greenhouse gas compared to emission of a kilogram of carbon dioxide. GWP can be calculated for different time horizons showing the effect of atmospheric lifetime for a given gas. The GWP for the 100-year time horizon is commonly the value referenced. For mixtures, a weighted average can be calculated based on the individual GWPs for each component. The standard GWP values for R22, R32, R125 and tetrafluoroethane has been taken from IIPCC 5.sup.th Assessment report 2014 (AR5). The GWP of the refrigerant mixture has been derived from mass fraction and the corresponding GWP values.

[0180] The compositions of the present invention has lower GWP value as compared with R-404 shown in the below Table-3.

TABLE-US-00003 TABLE 3 Refrigerant GWP R-404A 3920 Composition 1 1214 Composition 1a 1214 Composition 2 1197 Composition 2a 1183 Composition 3 1059 Composition 4 1056

[0181] Ozone depletion potential (ODP) is a number that refers to the amount of ozone depletion caused by a substance. The ODP is the ratio of the impact on ozone of a chemical compared to the impact of a similar mass of CFC-11 (fluorotrichloromethane). Thus, the ODP of CFC-11 is defined to be 1.0. Other CFCs and HCFCs have ODPs that range from 0.01 to 1.0. HFCs have zero ODP because they do not contain chlorine or other ozone depleting halogens. The composition of the present invention has zero ODP value.

[0182] In another embodiment of this aspect of the present invention, the refrigerant composition may contain optional components selected from the group consisting of lubricants, dyes (including Ultra Violet dyes), solubilizing agents, compatibilizers, stabilizers, tracers, perfluoropolyethers, anti-wear agents, extreme pressure agents, corrosion and oxidation inhibitors, metal surface energy reducers, metal surface deactivators, free radical scavengers, foam control agents, viscosity index improvers, pour point depressants, detergents, viscosity adjusters, and mixtures thereof. Indeed, many of these optional other components fit into one or more of these categories and may have qualities that lend themselves to achieve one or more performance characteristic.

[0183] In another embodiment of this aspect of the present invention, the refrigerant compositions are non-azeotropic mixture.

[0184] In another embodiment of this aspect of the present invention, the refrigerant composition is preferably charged in liquid form.

[0185] Additionally the composition of the present invention comprises a flame retardant, selected from phosphorus-based materials and non-phosphorus-based materials, to reduce the flammability of compositions.

[0186] The non-phosphorus-based materials comprises inert filler materials, such as calcium carbonate, aluminium trihydrate, magnesium hydroxide and calcium carbonate. Similarly the phosphorus-based flame-retardants comprises salt of melamine and bis(pentaerythritol phosphate) phosphoric acid and ammonium polyphosphate.

[0187] The refrigerant composition of the present invention has higher specific heat capacity as given in Table-4 below. Cp (Specific Heat in constant pressure) is the amount of heat required to increase temperature by 1° C. when heat is given at constant pressure, Cv (Specific heat in constant volume) means the amount of heat required to increase temperature by 1° C., when heat is given at constant volume.

TABLE-US-00004 TABLE 4 Cp/Cv at −25° Cp/Cv at −25° Cp/Cv at 25° C. in liquid C. in vapour C. in liquid Refrigerant phase phase phase R404a 1.5327 1.1859 1.6678 Composition 1 1.5631 1.1966 1.6918 Composition 2 1.5874 1.2117 1.7119 Composition 1a 1.5768 1.2007 1.7142 Composition 2a 1.5977 1.2141 1.7303 Composition 3 1.5657 1.2009 1.6922 Composition 4 1.593 1.2149 1.7168

[0188] In another embodiment of this aspect, the present invention provides a refrigeration process using the refrigerant composition comprising the steps of: [0189] a) condensing the refrigerant composition; [0190] b) evaporating the refrigerant composition. [0191] The vapor compression refrigeration cycle is given in FIG. 1.

[0192] Further, the refrigerant composition of present invention has higher thermal conductivity.

TABLE-US-00005 TABLE 5 Thermal conductivity Thermal conductivity (mW/m-K) at −25° C. in (mW/m-K) at 25° C. in Refrigerant liquid phase liquid phase R404a 82.918 62.714 Composition 1 104.76 80.781 Composition 2 113.14 87.494 Composition 1a 114.99 81.734 Composition 2a 123.53 87.911 Composition 3 107.19 82.914 Composition 4 116.86 90.662

[0193] The refrigerant compositions of the present invention may be used in stationary or mobile air conditioning systems or heat exchanger systems. Preferably, the refrigerant compositions would be utilized in domestic room air conditioning systems.

[0194] The present invention thus provides an R404a replacement refrigerant compositions that are compatible with existing mineral oil and alike lubricants and do not require replacement of the expensive devices in the legacy system.

[0195] R32 is commercially available or may be prepared by methods known in the art, such as by dechlorofluorination of methylene chloride.

[0196] R125 is commercially available or may be prepared by methods known in the art, such as dechlorofluorination of 2,2-dichloro-1,1,1-trifluoroethane as described in U.S. Pat. No. 5,399,549, incorporated herein by reference.

[0197] Tetrafluoroethane is commercially available or may be prepared by methods know in the art, such as by the hydrogenation of 1,1-dichloro-1,2,2,2-tetrafluoroethane (i.e., CCI.sub.2FCF.sub.3 or CFC-114a) to 1,1,1,2-tetrafluoroethane.

[0198] Heptafluoropropane is commercially available or may be prepared by methods known in the art.

[0199] R1234yf is commercially available or may be prepared by methods known in the art. It is against this and other backgrounds, which shall be filed in a detailed manner in complete specifications, in due course, the present invention is brought out and explained in following non-limiting examples.

[0200] It will be apparent to those skilled in the art that various modifications and variations can be made in the present invention and specific examples provided herein without departing from the spirit and scope of the invention. Thus, it is intended that the present invention covers the modifications and variations of this invention that come within the scope of any claims and their equivalents.

EXAMPLE

[0201] The refrigerant compositions according to the invention having composition of R125:R134a:R32:R227ea:R1234yf were prepared at 20 to 30° C. at atmospheric pressure and tested with standard ASHRAE modeling program maintaining indoor at 5° C. dry bulb temperature (DBT) and 4° C. wet bulb temperature (WBT) and outdoor at 35 DBT and 24 WBT.

[0202] The analytical results of the various refrigerant compositions are shown in below tables.

TABLE-US-00006 TABLE 6 Analysis at 25° C. in liquid phase R404a C-1 C-1a C-2 C-2a C-3 C-4 Pressure 12.546 12.309 13.786 12.173 13.56 12.048 12.001 (bar) Density 1044.1 1094.5 1088.1 1096.9 1090.2 1074.1 1092.5 (kg/m.sup.3) Volume 0.0009578 0.0009137 0.000919 0.0009117 0.0009173 0.000931 0.0009154 (m.sup.3/kg) Int. Energy 235.1 235.67 235.98 236.6 236.84 236.39 236.86 (kj/kg) Enthalpy 236.3 236.8 237.24 237.71 238.08 237.51 237.96 (kj/kg) Entropy 1.125 1.1269 1.1283 1.1301 1.1312 1.1294 1.131 (kJ/kg-K) Cv (kJ/kg-K) 0.92472 0.91223 0.91282 0.92106 0.92174 0.92817 0.92321 Cp (kJ/kg-K) 1.5423 1.5433 1.5647 1.5768 1.5949 1.5706 1.585 Cp/Cv 1.6678 1.6918 1.7142 1.7119 1.7303 1.692 1.7168 Molar 97.604 87.488 85.403 81.133 79.813 84.083 79.189 mass(Kg/K Thermal 62.714 80.781 81.734 87.494 87.911 82.914 90.662 conductivity (mW/m-K) Viscosity 128.27 139.22 136.74 NA 142.16 139.1 144.54 (uPa-s)

TABLE-US-00007 TABLE 7 Analysis at 25° C. in vapor phase R404a C-1 C-1a C-2 C-2a C-3 C-4 Pressure 12.412 10.597 11.053 10.488 10.856 10.358 10.249 (bar) Density 65.274 46.78 47.564 42.555 43.271 43.714 40.394 (kg/m.sup.3) Volume 0.01532 0.021377 0.021024 0.023499 0.02311 0.022876 0.024756 (m.sup.3/kg) Int. Energy 357.54 387.83 389.41 405.42 405.91 396.67 411.39 (kJ/kg) Enthalpy 376.55 410.48 412.65 430.06 431 420.37 436.76 (kJ/kg) Entropy 1.5958 1.7156 1.7251 1.7819 1.7873 1.7491 1.805 (kJ/kg-K) Cv (kJ/kg-K) 0.89151 0.86448 0.86028 0.86835 0.86339 0.87388 0.86943 Cp (kJ/kg-K) 1.2214 1.1499 1.149 1.1705 1.1658 1.1634 1.1719 Cp/Cv 1.3701 1.3302 1.3356 1.3479 1.3502 1.3313 1.3478 Molar 97.604 87.488 85.403 81.133 79.813 84.083 79.189 mass(Kg/ Kmol) Thermal 17.003 14.581 14.725 NA 14.671 14.603 14.497 conductivity Viscosity 12.229 12.334 12.446 NA 12.239 12.205 12.055 (uPa-s)

TABLE-US-00008 TABLE 8 Analysis at −25° C. in liquid phase R404a C-1 C-1a C-2 C-2a C-3 C-4 Pressure 2.5373 2.4395 2.9446 2.374 2.8548 2.3782 2.3367 (bar) Density 1238.6 1277.9 1273.9 1275.5 1270.8 1251 1268.1 (kg/m.sup.3) Volume 0.0008074 0.0007825 0.000785 0.000784 0.0007869 0.0007993 0.0007886 (m.sup.3/kg) Int. Energy 166.21 165.42 164.99 164.43 164.08 164.71 164.17 (kJ/kg) Enthalpy 166.41 165.61 165.22 164.62 164.3 164.9 164.36 (kJ/kg) Entropy 0.87225 0.86912 0.86775 0.86529 0.86419 0.86636 0.86426 (kJ/kg-K) Cv (kJ/kg-K) 0.84874 0.85464 0.85658 0.86776 0.86957 0.87164 0.8712 Cp (kJ/kg-K) 1.3008 1.3359 1.3506 1.3775 1.3893 1.3647 1.3879 Cp/Cv 1.5327 1.5631 1.5768 1.5874 1.5977 1.5657 1.593 Molar 97.604 87.488 85.403 81.133 79.813 84.083 79.189 mass(Kg/ Kmol) Thermal 82.918 104.76 106.5 113.14 114.18 107.19 116.86 conductivity (mW/m-K) Viscosity 249.25 257.95 254.24 267.16 263.01 256.47 264.85 (uPa-s)

TABLE-US-00009 TABLE 9 Analysis at −25° C. in vapour phase R404a C-1 C-1a C-2 C-2a C-3 C-4 Pressure 2.4752 1.8868 1.9658 1.8199 1.8824 1.8331 1.7662 (bar) Density 12.797 8.5463 8.6866 7.6199 7.7484 7.9673 7.2074 (kg/m.sup.3) Volume 0.078143 0.11701 0.11512 0.13124 0.12906 0.12551 0.13875 (m.sup.3/kg) Int. Energy 332.99 363.94 365.84 382.76 383.39 372.67 388.78 (kJ/kg) Enthalpy 352.33 386.02 388.47 406.65 407.69 395.68 413.29 (kJ/kg) Entropy 1.6226 1.7697 1.7839 1.8542 1.8629 1.8092 1.8821 (kJ/kg-K) Cv (kJ/kg-K) 0.7316 0.70979 0.70677 0.70638 0.70355 0.71639 0.70698 Cp (kJ/kg-K) 0.86763 0.84931 0.84863 0.85589 0.85418 0.86028 0.8589 Cp/Cv 1.1859 1.1966 1.2007 1.2117 1.2141 1.2009 1.2149 Molar 97.604 87.488 85.403 81.133 79.813 84.083 79.189 mass(Kg/ Kmol) Thermal 10.868 9.9927 10.086 9.9796 10.06 9.9472 9.9594 conductivity (mW/m-K) Viscosity 10.039 10.111 10.211 10.035 10.117 10.004 9.9637 (uPa-s)