 AZEOTROPIC COMPOSITIONS BASED ON TETRAFLUOROPROPENE
专利摘要:
The present invention relates to azeotropic compositions comprising from 74 to 81.5% by weight of HFO-1324yf, from 6.5 to 10.5% by weight of HFC-134a, and from 12 to 16% by weight of HFC-152a. , relative to the total weight of the composition, said azeotropic composition having a boiling point between -40,00 ° C. and 70,00 ° C., at a pressure of between 0.5 and 21.0 bar abs (+ / - 0.5%). The invention also relates to the uses of said compositions in heat transfer systems. 公开号:FR3057272A1 申请号:FR1659749 申请日:2016-10-10 公开日:2018-04-13 发明作者:Wissam Rached 申请人:Arkema France SA； IPC主号:
专利说明:
© Publication no .: 3 057272 (to be used only for reproduction orders) ©) National registration number: 16 59749 ® FRENCH REPUBLIC NATIONAL INSTITUTE OF INDUSTRIAL PROPERTY COURBEVOIE © Int Cl 8 : C 09 K 5/04 (2017.01), F25 B 1/00 A1 PATENT APPLICATION ©) Date of filing: 10.10.16.(© Priority: (© Applicant (s): ARKEMA FRANCE Société anonyme - FR. @ Inventor (s): RACHED WISSAM. ©) Date of public availability of the request: 04/13/18 Bulletin 18/15. ©) List of documents cited in the preliminary search report: See the end of this booklet (© References to other related national documents: ©) Holder (s): ARKEMA FRANCE Société anonyme. ©) Extension request (s): (© Agent (s): ARKEMA FRANCE Public limited company. AZEOTROPIC COMPOSITIONS BASED ON TETRAFLUOROPROPENE. FR 3 057 272 - A1 The present invention relates to azeotropic compositions comprising from 74 to 81.5% by weight of HFO1324yf, from 6.5 to 10.5% by weight of HFC-134a, and from 12 to 16% by weight of HFC-152a, per relative to the total weight of the composition, said azeotropic composition having a boiling temperature of between -40.00 ° C and 70.00 ° C, at a pressure of between 0.5 and 21.0 bar abs (+/- 0.5%). The invention also relates to the uses of said compositions in heat transfer systems. i Azeotropic compositions based on tetrafluoropropene FIELD OF THE INVENTION The present invention relates to azeotropic compositions based on tetrafluoropropene, and their uses as a heat transfer fluid, in particular in refrigeration, air conditioning and heat pump. TECHNICAL BACKGROUND The problems posed by substances that deplete the atmospheric ozone layer were dealt with in Montreal, where the protocol requiring a reduction in the production and use of chlorofluorocarbons (CFCs) was signed. This protocol has been the subject of amendments which have forced the abandonment of CFCs and extended the regulation to other products, including hydrochlorofluorocarbons (HCFCs). The refrigeration and air conditioning industry has invested heavily in the substitution of these refrigerants and this is how hydrofluorocarbons (HFCs) were marketed. In the automotive industry, the air conditioning systems of vehicles sold in many countries have gone from a chlorofluorocarbon (CFC-12) refrigerant to that of hydrofluorocarbon (1,1,1,2 tetrafluoroethane: HFC-134a ), less harmful to the ozone layer. However, with regard to the objectives set by the Kyoto protocol, HFC-134a (GWP = 1430) is considered to have a high warming power. The contribution to the greenhouse effect of a fluid is quantified by a criterion, the GWP (Global Warming Potential) which summarizes the warming power by taking a reference value of 1 for carbon dioxide. Carbon dioxide being non-toxic, non-flammable and having a very low GWP, has been proposed as refrigerant for air conditioning systems to replace HFC-134a. However, the use of carbon dioxide has several drawbacks, in particular related to the very high pressure of its use as a refrigerant in existing devices and technologies. Document JP 4110388 describes the use of hydrofluoropropenes of formula CsHmFn, with m, n representing an integer between 1 and 5 inclusive and m + n = 6, as heat transfer fluids, in particular tetrafluoropropene and trifluoropropene. Document WO2004 / 037913 discloses the use of compositions comprising at least one fluoroalkene having three or four carbon atoms, in particular pentafluoropropene and tetrafluoropropene, preferably having a GWP of at most 150, as heat transfer fluids. Document WO 2005/105947 teaches the addition to tetrafluoropropene, preferably 1,3,3,3 tetrafluoropropene, of a co-expanding agent such as difluoromethane (HFC-32), pentafluoroethane (HFC-125 ), tetrafluoroethane, difluoroethane, heptafluoropropane, hexafluoropropane, pentafluoropropane, pentafluorobutane, water and carbon dioxide. WO 2006/094303 discloses an azeotropic composition containing 70.4% by weight of 2,3,3,3 tetrafluoropropene (1234yf) and 29.6% by weight of 1,1,1,2 tetrafluoroethane (HFC-134a) . This document also discloses an azeotropic composition containing 91% by weight of 2,3,3,3 tetrafluoropropene and 9% by weight of difluoroethane (HFC-152a). In the industrial field, the most widely used refrigeration machines are based on evaporative cooling of a liquid refrigerant. After vaporization, the fluid is compressed and then cooled in order to return to the liquid state and thus continue the cycle. Lubricating oils are necessary to ensure the proper functioning of moving mechanical parts, and in particular to ensure the lubrication of the compressor bearings. However, the refrigerant, which is at each passage in the compressor in contact with the lubricant present on the moving parts, tends to take away a certain amount, which accompanies the refrigerant in its cycle, and is therefore found in the evaporator . To overcome this problem of oil migration, it is known to use an oil separation system capable of purging the accumulated oil from the high pressure at the outlet of the compressor to the low pressure (at compressor input). Thanks to their thermal stability and their miscibility with HFOs, especially HFO-1234, POE oils are commonly used in heat transfer systems, especially in refrigeration and / or air conditioning. However, due to the good solubility of HFO-1234 in POE oils, a problem has been observed with heat transfer systems comprising an oil separator: a relatively large quantity of refrigerant remains trapped by the oil. The bleeding of the oil induces the return of the trapped refrigerant from the compressor outlet directly to the compressor inlet. This results in a net loss of efficiency for the installation, insofar as the totality of the refrigerant does not carry out the entire refrigeration cycle, and also results in a deterioration of the lubrication of compressors, in particular screw compressors, due to lower oil quantity. There is therefore a need to find new compositions which make it possible in particular to overcome at least one of the abovementioned drawbacks, and in particular having a zero ODP and a GWP lower than that of existing HFCs such as R407C or R134a. DESCRIPTION OF THE INVENTION The subject of the present invention is an azeotropic composition comprising (preferably consisting of) from 74 to 81.5% by weight of HFO-1234yf, from 6.5 to 10.5% by weight of HFC-134a, and from 12 to 16 % by weight of HFC-152a, relative to the total weight of the composition, said azeotropic composition having a boiling temperature between -40.00 ° C and 70.00 ° C, at a pressure between 0.5 and 21.0 bar abs (± 0.5%). According to a preferred embodiment, the azeotropic composition comprises (preferably consists) of 75.5 to 79.5% by weight of HFO-1234yf, of 12 to 16% by weight of HFC-152a, and of 6.5 at 10.5% by weight of HFC-134a, relative to the total weight of the composition, said composition having a boiling temperature between -40.00 ° C and 70.00 ° C, at a pressure between 0 , 5 and 21.0 bar abs (± 0.5%). Unless otherwise stated, throughout the application, the proportions of compounds indicated are given in percentages by mass. In the context of the invention, "HFO-1234yf" refers to 2,3,3,3tetrafluoropropene, The compositions of the invention advantageously have a zero ODP and a lower GWP than existing HFCs. In addition, these compositions advantageously make it possible to improve the efficiency of heat transfer systems comprising an oil separator, in particular compared to HFO-1234yf alone. The compositions according to the invention can be prepared by any known process, such as for example by simple mixing of the different compounds with each other. In the context of the invention, the term “vapor saturation pressure” or “Psat vap” means the pressure at which the first drop of liquid begins to form in a fluid in the vapor state. This pressure is also called dew pressure. In the context of the invention, the term "liquid saturation pressure" or "Psat liq" means the pressure at which the first vapor bubble begins to form in a fluid in the liquid state. This pressure is also called bubble pressure. In the context of the invention, the percentage Rp, calculated from the vapor and liquid saturation pressures, corresponds to the following equation: [(Psat liq - Psat vap)} Rp = ------— x 1O o Psat liq In the context of the invention, a mixture is azeotropic when the percentage Rp defined above is between 0 and 0.5%. In the context of the invention, by "lying between x and y" is meant an interval in which the limits x and y are included. For example, the range "between 0 and 0.5%" notably includes the values 0 and 0.5%. As an example and according to ASHRAE STANDARD 34-2013 “Designation and safety classification of refrigerants”, the mixtures in the table below are classified as azeotropes, according to this standard (the components, compositions and temperatures are indicated by the same standard) , the pressures being calculated by Refrop 9 (Reference fluid Properties, Software developed by NIST (National Institute of Standards and Technology) for the calculation of the properties of refrigerants): Product Components % by mass Temperature(° C) PsatLiq(barabs)(±0.5%) Psatvap(barabs)(±0.5%) Rp(valuerounded totenth) R500 R12 / R152a 73.8 / 26.2 0.0 3,643 3,638 0.1 R501 R22 / R12 75/25 -41.0 0.996 0.992 0.4 R502 R22 / R115 48.8 / 51.2 19.0 9.803 9,800 0.0 R504 R32 / R115 48.2 / 51.8 17.0 15,240 15,229 0.1 R507A R125 / R143a 50/50 -40.0 1.386 1.386 0.0 R508A R23 / R116 39/61 -86.0 1,111 1,111 0.0 R512A R134a / R152a 5/95 10.0 3,728 3,728 0.0 This table describes in particular refrigerants classified as azeotropic showing a relative difference in saturation pressures of less than 0.50%. Preferred azeotropic compositions according to the invention are as follows (the pressures being calculated by Refrop 9: Software developed by NIST for the calculation of the properties of refrigerants): R1234yf R 134a R 152a Temperature(° C) PsatLiq(barabs)(±0.5%) Psatvap(barabs)(±0.5%) Rp(value rounded to the nearest tenth) 77.5 8.5 14.0 -40.00 0.616 0.614 0.3 77.5 8.5 14.0 -35.00 0.783 0.781 0.3 77.5 8.5 14.0 -30.00 0.984 0.982 0.2 77.5 8.5 14.0 -25.00 1,224 1.221 0.2 77.5 8.5 14.0 -20.00 1.507 1.504 0.2 77.5 8.5 14.0 -15.00 1.838 1,835 0.2 77.5 8.5 14.0 -10.00 2,223 2,221 0.1 77.5 8.5 14.0 -5.00 2,668 2,665 0.1 77.5 8.5 14.0 0.00 3.178 3.176 0.1 77.5 8.5 14.0 5.00 3.759 3,757 0.1 77.5 8.5 14.0 10.00 4.418 4.416 0.0 77.5 8.5 14.0 15.00 5.161 5.158 0.1 77.5 8.5 14.0 20.00 5.994 5.991 0.1 77.5 8.5 14.0 25.00 6,924 6,921 0.0 77.5 8.5 14.0 26.97 7.319 7.316 0.0 77.5 8.5 14.0 30.00 7.959 7,956 0.0 77.5 8.5 14.0 35.00 9,106 9,102 0.0 77.5 8.5 14.0 40.00 10.371 10.367 0.0 77.5 8.5 14.0 45.00 11,765 11,760 0.0 77.5 8.5 14.0 50.00 13,293 13,288 0.0 77.5 8.5 14.0 55.00 14.966 14,960 0.0 77.5 8.5 14.0 60.00 16,793 16,786 0.0 77.5 8.5 14.0 65.00 18,783 18,775 0.0 77.5 8.5 14.0 70.00 20,948 20,938 0.0 Preferred azeotropic compositions according to the invention are as follows: R1234yf R 134a R 152a Temperature(° C) PsatLiq(barabs)(±0.5%) Psatvap(barabs)(±0.5%) Rp(value rounded to the nearest tenth) 77.5 6.5 16.0 -40.00 0.615 0.613 0.3 77.5 6.5 16.0 -35.00 0.782 0.779 0.4 77.5 6.5 16.0 -30.00 0.982 0.979 0.3 77.5 6.5 16.0 -25.00 1.221 1.218 0.2 77.5 6.5 16.0 -20.00 1.504 1.501 0.2 77.5 6.5 16.0 -15.00 1.834 1,831 0.2 77.5 6.5 16.0 -10.00 2,219 2,216 0.1 77.5 6.5 16.0 -5.00 2,663 2,660 0.1 77.5 6.5 16.0 0.00 3.172 3.169 0.1 77.5 6.5 16.0 5.00 3,752 3,749 0.1 77.5 6.5 16.0 10.00 4.409 4.406 0.1 77.5 6.5 16.0 15.00 5.150 5.147 0.1 77.5 6.5 16.0 20.00 5,981 5,979 0.0 77.5 6.5 16.0 25.00 6,910 6.907 0.0 77.5 6.5 16.0 26.97 7,304 7,301 0.0 77.5 6.5 16.0 30.00 7,942 7,939 0.0 77.5 6.5 16.0 35.00 9.086 9.083 0.0 77.5 6.5 16.0 40.00 10.349 10.346 0.0 77.5 6.5 16.0 45.00 11,740 11,736 0.0 77.5 6.5 16.0 50.00 13,265 13,261 0.0 77.5 6.5 16.0 55.00 14.935 14,930 0.0 77.5 6.5 16.0 60.00 16,757 16,752 0.0 77.5 6.5 16.0 65.00 18,743 18,737 0.0 77.5 6.5 16.0 70.00 20,903 20,897 0.0 Preferred azeotropic compositions according to the invention are as follows: R1234 yf R 134a R 152a Temperature(° C) Psat Liq (bar abs)(± 0.5%) Psat vap (bar abs) (± 0.5%) Rp(value rounded to the nearest tenth) 81.5 6.5 12.0 -40.00 0.619 0.618 0.2 81.5 6.5 12.0 -35.00 0.787 0.785 0.3 81.5 6.5 12.0 -30.00 0.988 0.986 0.2 81.5 6.5 12.0 -25.00 1.228 1.226 0.2 81.5 6.5 12.0 -20.00 1.511 1.509 0.1 81.5 6.5 12.0 -15.00 1,842 1,841 0.1 81.5 6.5 12.0 -10.00 2,228 2,226 0.1 81.5 6.5 12.0 -5.00 2.672 2,671 0.0 81.5 6.5 12.0 0.00 3.182 3.181 0.0 81.5 6.5 12.0 5.00 3,763 3,761 0.1 81.5 6.5 12.0 10.00 4.420 4.419 0.0 81.5 6.5 12.0 15.00 5.162 5,160 0.0 81.5 6.5 12.0 20.00 5.993 5.991 0.0 81.5 6.5 12.0 25.00 6,922 6,919 0.0 81.5 6.5 12.0 26.97 7.316 7.313 0.0 81.5 6.5 12.0 30.00 7.954 7,951 0.0 81.5 6.5 12.0 35.00 9.097 9.094 0.0 81.5 6.5 12.0 40.00 10,359 10.355 0.0 81.5 6.5 12.0 45.00 11,748 11,743 0.0 81.5 6.5 12.0 50.00 13,272 13,266 0.0 81.5 6.5 12.0 55.00 14,939 14,932 0.0 81.5 6.5 12.0 60.00 16,759 16,751 0.0 81.5 6.5 12.0 65.00 18,742 18,732 0.1 81.5 6.5 12.0 70.00 20,898 20,887 0.1 Preferred azeotropic compositions according to the invention are as follows: R1234yf R 134a R 152a Temperature(° C) Psat Liq (bar abs)(± 0.5%) Psat vap (bar abs)(± 0.5%) Rp(valueroundedattenth) 75.5 10.0 14.5 -40.00 0.615 0.612 0.5 75.5 10.0 14.5 -35.00 0.782 0.778 0.5 75.5 10.0 14.5 -30.00 0.983 0.979 0.4 75.5 10.0 14.5 -25.00 1.222 1.218 0.3 75.5 10.0 14.5 -20.00 1.505 1.501 0.3 75.5 10.0 14.5 -15.00 1.836 1.833 0.2 75.5 10.0 14.5 -10.00 2,222 2,218 0.2 75.5 10.0 14.5 -5.00 2,667 2,663 0.1 75.5 10.0 14.5 0.00 3.177 3.173 0.1 75.5 10.0 14.5 5.00 3.759 3,755 0.1 75.5 10.0 14.5 10.00 4.418 4.415 0.1 75.5 10.0 14.5 15.00 5.161 5.158 0.1 75.5 10.0 14.5 20.00 5.995 5.992 0.1 75.5 10.0 14.5 25.00 6,927 6,923 0.1 75.5 10.0 14.5 26.97 7,323 7.319 0.1 75.5 10.0 14.5 30.00 7,963 7,960 0.0 75.5 10.0 14.5 35.00 9,112 9,108 0.0 75.5 10.0 14.5 40.00 10,380 10.375 0.0 75.5 10.0 14.5 45.00 11,775 11,770 0.0 75.5 10.0 14.5 50.00 13,307 13.301 0.0 75.5 10.0 14.5 55.00 14,983 14.977 0.0 75.5 10.0 14.5 60.00 16,814 16.806 0.0 75.5 10.0 14.5 65.00 18.808 18,800 0.0 75.5 10.0 14.5 70.00 20,978 20,968 0.0 Preferred azeotropic compositions according to the invention are as follows: R1234yf R 134a R 152a Temperature(° C) Psat Liq (bar abs)(± 0.5%) Psat vap (bar abs)(± 0.5%) Rp(valueroundedattenth) 77.5 10.5 12.0 -40.00 0.618 0.615 0.5 77.5 10.5 12.0 -35.00 0.785 0.783 0.3 77.5 10.5 12.0 -30.00 0.987 0.984 0.3 77.5 10.5 12.0 -25.00 1.227 1,224 0.2 77.5 10.5 12.0 -20.00 1.510 1.508 0.1 77.5 10.5 12.0 -15.00 1,842 1,840 0.1 77.5 10.5 12.0 -10.00 2,229 2,226 0.1 77.5 10.5 12.0 -5.00 2.674 2.672 0.1 77.5 10.5 12.0 0.00 3.186 3.183 0.1 77.5 10.5 12.0 5.00 3,768 3,766 0.1 77.5 10.5 12.0 10.00 4.429 4.426 0.1 77.5 10.5 12.0 15.00 5,173 5,170 0.1 77.5 10.5 12.0 20.00 6.008 6.005 0.0 77.5 10.5 12.0 25.00 6,940 6,937 0.0 77.5 10.5 12.0 26.97 7.336 7.332 0.1 77.5 10.5 12.0 30.00 7,978 7,974 0.1 77.5 10.5 12.0 35.00 9,127 9,122 0.1 77.5 10.5 12.0 40.00 10,395 10,390 0.0 77.5 10.5 12.0 45.00 11,791 11,785 0.1 77.5 10.5 12.0 50.00 13,324 13,316 0.1 77.5 10.5 12.0 55.00 15,000 14.992 0.1 77.5 10.5 12.0 60.00 16,831 16,821 0.1 77.5 10.5 12.0 65.00 18,826 18,815 0.1 77.5 10.5 12.0 70.00 20.996 20,983 0.1 According to a preferred embodiment, the azeotropic composition according to the invention comprises (preferably consists of) 77.5% (± 0.2%) by weight of HFO1234yf, 14% (± 0.2%) by weight of HFC-152a and 8.5% (± 0.2%) by weight of HFC-134a, relative to the total weight of the composition, said composition having a boiling temperature between -40.00 ° C and 70, 00 ° C, at a pressure between 0.5 and 21.0 bar abs (± 0.5%). According to a preferred embodiment, the azeotropic composition according to the invention comprises (preferably consists of) 77.5% (± 0.2%) by weight of HFO1234yf, 14% (± 0.2%) by weight of HFC-152a and 8.5% (± 0.2%) by weight of HFC-134a, relative to the total weight of the composition, said composition having a boiling temperature of 26.97 ° C (± 0.50 ° C) at a pressure of 7.3 bar abs (± 0.5%). According to a preferred embodiment, the azeotropic composition according to the invention comprises (preferably consists of) 77.5% (± 0.2%) by weight of HFO1234yf, 16% (± 0.2%) by weight of HFC-152a and 6.5% (± 0.2%) by weight of HFC-134a, relative to the total weight of the composition, said composition having a boiling temperature between -40.00 ° C and 70, 00 ° C, at a pressure between 0.5 and 21.0 bar abs (± 0.5%), and preferably between 0.6 and 20.9 bar abs (± 0.5%). According to a preferred embodiment, the azeotropic composition according to the invention comprises (preferably consists of) 77.5% (± 0.2%) by weight of HFO1234yf, 16% (± 0.2%) by weight of HFC-152a and 6.5% (± 0.2%) by weight of HFC-134a, relative to the total weight of the composition, said composition having a boiling temperature of 26.97 ° C (± 0.50 ° C) at a pressure of 7.3 bar abs (± 0.5%). According to a preferred embodiment, the azeotropic composition according to the invention comprises (preferably consists of) 81.5% (± 0.2%) by weight of HFO1234yf, 12% (± 0.2%) by weight of HFC-152a and 6.5% (± 0.2%) by weight of HFC-134a, relative to the total weight of the composition, said composition having a boiling temperature between -40.00 ° C and 70, 00 ° C, at a pressure between 0.5 and 21.0 bar abs (± 0.5%), and preferably between 0.6 and 20.9 bar abs (± 0.5%). According to a preferred embodiment, the azeotropic composition according to the invention comprises (preferably consists of) 81.5% (± 0.2%) by weight of HFO3057272 1234yf, 12% (± 0.2%) by weight of HFC-152a and 6.5% (± 0.2%) by weight of HFC-134a, relative to the total weight of the composition, said composition having a temperature boiling point of 26.97 ° C (± 0.50 ° C) at a pressure of 7.3 bar abs (± 0.5%). According to a preferred embodiment, the azeotropic composition according to the invention comprises (preferably consists of) 75.5% (± 0.2%) by weight of HFO1234yf, 14.5% (± 0.2%) in weight of HFC-152a and 10% (± 0.2%) by weight of HFC-134a, relative to the total weight of the composition, said composition having a boiling temperature between -40.00 ° C and 70, 00 ° C, at a pressure between 0.5 and 21.0 bar abs (± 0.5%), and preferably between 0.78 and 20.98 bar abs (± 0.5%). According to a preferred embodiment, the azeotropic composition according to the invention comprises (preferably consists of) 75.5% (± 0.2%) by weight of HFO1234yf, 14.5% (± 0.2%) in weight of HFC-152a and 10% (± 0.2%) by weight of HFC-134a, relative to the total weight of the composition, said composition having a boiling temperature of 26.97 ° C (± 0.50 ° C) at a pressure of 7.3 bar abs (± 0.5%). According to a preferred embodiment, the azeotropic composition according to the invention comprises (preferably consists of) 77.5% (± 0.2%) by weight of HFO1234yf, 12% (± 0.2%) by weight of HFC-152a and 10.5% (± 0.2%) by weight of HFC-134a, relative to the total weight of the composition, said composition having a boiling temperature between -40.00 ° C and 70, 00 ° C, at a pressure between 0.5 and 21.0 bar abs (± 0.5%), and preferably between 0.61 and 21.00 bar abs (± 0.5%). According to a preferred embodiment, the azeotropic composition according to the invention comprises (preferably consists of) 77.5% (± 0.2%) by weight of HFO1234yf, 12% (± 0.2%) by weight of HFC-152a and 10.5% (± 0.2%) by weight of HFC-134a, relative to the total weight of the composition, said composition having a boiling temperature of 26.97 ° C (± 0.50 ° C) at a pressure of 7.3 (± 0.5%). Heat transfer fluid composition According to one embodiment, the azeotropic composition of the invention is a heat transfer fluid. The azeotropic composition according to the invention can comprise one or more additives (which are essentially not heat transfer compounds for the intended application). The additives can in particular be chosen from nanoparticles, stabilizers, surfactants, tracer agents, fluorescent agents, odorous agents, lubricants and solubilizing agents. By “heat transfer compound”, respectively “heat transfer fluid” or “refrigerant”, is meant a compound, respectively a fluid, capable of absorbing heat by evaporating at low temperature and low pressure and to reject heat by condensing at high temperature and high pressure, in a vapor compression circuit. Generally, a heat transfer fluid can comprise a single, two, three or more of three heat transfer compounds. By "heat transfer composition" is meant a composition comprising a heat transfer fluid and optionally one or more additives which are not heat transfer compounds for the intended application. The present invention also relates to a heat transfer composition comprising (preferably consisting of) the azeotropic composition according to the above-mentioned invention, and at least one additive chosen in particular from nanoparticles, stabilizers, surfactants, tracer agents, agents fluorescent, odorants, lubricants and solubilizers. Preferably, the additive is chosen from lubricants, and in particular lubricants based on polyol esters. The stabilizer or stabilizers, when they are present, preferably represent at most 5% by mass in the heat transfer composition. Among the stabilizers, mention may in particular be made of nitromethane, ascorbic acid, terephthalic acid, azoles such as tolutriazole or benzotriazole, phenolic compounds such as tocopherol, hydroquinone, t-butyl hydroquinone, 2,6-di-ter-butyl-4-methylphenol, epoxides (optionally fluorinated or perfluorinated or alkenyl or aromatic alkyl) such as n-butyl glycidyl ether, hexanediol diglycidyl ether, allyl glycidyl ether, butylphenylglycidyl ether, phosphites, phosphonates, thiols and lactones. As nanoparticles, it is possible in particular to use carbon nanoparticles, metal oxides (copper, aluminum), T1O2, AI2O3, M0S2 ... As tracer agents (capable of being detected), mention may be made of hydrofluorocarbons, deuterated or not, deuterated hydrocarbons, perfluorocarbons, fluoroethers, brominated compounds, iodinated compounds, alcohols, aldehydes, ketones, nitrous oxide and combinations thereof. The tracer is different from the heat transfer compound (s) making up the heat transfer fluid. As solubilizers, mention may be made of hydrocarbons, dimethyl ether, polyoxyalkylene ethers, amides, ketones, nitriles, chlorocarbons, esters, lactones, aryl ethers, fluoroethers and 1.1 , 1trifluoroalkanes. The solubilizer is different from the heat transfer compound (s) making up the heat transfer fluid. Mention may be made, as fluorescent agents, of naphthalimides, perylenes, coumarins, anthracenes, phenanthracenes, xanthenes, thioxanthenes, naphthoxanhtenes, fluoresceins and derivatives and combinations thereof. As odorants, mention may be made of alkylacrylates, allylacrylates, acrylic acids, acrylesters, alkyl ethers, alkyl esters, alkynes, aldehydes, thiols, thioethers, disulfides, allylisothiocyanates, alkanoic acids , amines, norbornenes, norbornene derivatives, cyclohexene, heterocyclic aromatics, ascaridole, o-methoxy (methyl) -phenol and combinations thereof. In the context of the invention, the terms "lubricant", "lubricating oil" and "lubricating oil" are used in an equivalent manner. As lubricants, it is possible in particular to use oils of mineral origin, silicone oils, paraffins of natural origin, naphthenes, synthetic paraffins, alkylbenzenes, poly-alpha olefins, polyalkene glycols, polyol esters. and / or polyvinyl ethers. According to one embodiment, the lubricant is based on polyol esters. In particular, the lubricant comprises one or more polyol ester (s). According to one embodiment, the polyol esters are obtained by reaction of at least one polyol, with a carboxylic acid or with a mixture of carboxylic acids. In the context of the invention, and unless otherwise stated, the term "polyol" means a compound containing at least two hydroxyl groups (-OH). Polyol esters A) According to one embodiment, the polyol esters according to the invention correspond to the following formula (I): R 1 [OC (O) R 2 ] n (I) in which: R 1 is a linear or branched hydrocarbon radical, optionally substituted with at least one hydroxyl group and / or comprising at least one heteroatom chosen from the group consisting of -O-, -N-, and -S-; each R 2 is, independently of each other, chosen from the group consisting of: o i) H; o ii) an aliphatic hydrocarbon radical; o iii) a branched hydrocarbon radical; o iv) a mixture of a radical ii) and / or iii), with an aliphatic hydrocarbon radical comprising from 8 to 14 carbon atoms; and n is an integer of at least 2. In the context of the invention, the term “hydrocarbon radical” is understood to mean a radical composed of carbon and hydrogen atoms. According to one embodiment, the polyols have the following general formula (II): R 1 (OH) n (II) in which: R 1 is a linear or branched hydrocarbon radical, optionally substituted by at least one hydroxyl group, preferably by two hydroxyl groups, and / or comprising at least one heteroatom chosen from the group consisting of -O-, -N-, and -S-; and n is an integer of at least 2. Preferably, R 1 is a hydrocarbon radical, linear or branched, comprising from 4 to 40 carbon atoms, preferably from 4 to 20 carbon atoms. Preferably, R 1 is a hydrocarbon radical, linear or branched, comprising at least one oxygen atom. Preferably, R 1 is a branched hydrocarbon radical comprising from 4 to 10 carbon atoms, preferably 5 carbon atoms, substituted by two hydroxyl groups. According to a preferred embodiment, the polyols comprise from 2 to 10 hydroxyl groups, preferably from 2 to 6 hydroxyl groups. The polyols according to the invention may comprise one or more oxyalkylene groups, in this particular case it is polyether polyols. The polyols according to the invention can also comprise one or more nitrogen atoms. For example, the polyols can be alkanol amines containing from 3 to 6 OH groups. Preferably, the polyols are alkanol amines containing at least two OH groups, and preferably at least three. According to the present invention, the preferred polyols are chosen from the group consisting of ethylene glycol, diethylene glycol, triethylene glycol, propylene glycol, dipropylene glycol, glycerol, neopentyl glycol, 1,2-butanediol, 1,4-butanediol, 1,3-butanediol, pentaerythritol, dipentaerythritol, tripentaerythritol, triglycerol, trimethylolpropane, sorbitol, hexaglycerol, and mixtures thereof. According to the invention, the carboxylic acids can correspond to the following general formula (III): R 2 COOH (III) in which: R 2 is chosen from the group consisting of: oi) H; o ii) an aliphatic hydrocarbon radical; o iii) a branched hydrocarbon radical; o iv) a mixture of a radical ii) and / or iii), with an aliphatic hydrocarbon radical comprising from 8 to 14 carbon atoms. Preferably, R 2 is an aliphatic hydrocarbon radical comprising from 1 to 10, preferably from 1 to 7 carbon atoms, and in particular from 1 to 6 carbon atoms. Preferably, R 2 is a branched hydrocarbon radical comprising from 4 to 20 carbon atoms, in particular from 5 to 14 carbon atoms, and preferably from 6 to 8 carbon atoms. According to a preferred embodiment, a branched hydrocarbon radical has the following formula (IV): -C (R 3 ) R 4 ) (R 5 ) (IV) in which R 3 , R 4 and R 5 are, independently of each other, an alkyl group, and at least one of the alkyl groups contains at least two atoms of carbon. Such branched alkyl groups, once linked to the carboxyl group, are known under the name "neo group", and the corresponding acid as "neo acid". Preferably, R 3 and R 4 are methyl groups and R 10 is an alkyl group comprising at least two carbon atoms. According to the invention, the radical R 2 may comprising one or more carboxy groups, or ester groups such as -COOR 6 , with R 6 representing an alkyl, hydroxyalkyl radical or a hydroxyalkyloxy alkyl group. Preferably, the acid R 2 COOH of formula (III) is a monocarboxylic acid. Examples of carboxylic acids in which the hydrocarbon radical is aliphatic are in particular: formic acid, acetic acid, propionic acid, butyric acid, pentanoic acid, hexanoic acid and heptanoic acid . Examples of carboxylic acids in which the hydrocarbon radical is branched are in particular: 2-ethyl-n-butyric acid, 2-hexyldecanoic acid, isostearic acid, 2-methyl-hexanoic acid, 2-methylbutanoic acid, 3methylbutanoic acid, 3,5,5-trimethyl-hexanoic acid, 2-ethylhexanoic acid, neoheptanoic acid, and neodecanoic acid. The third type of carboxylic acids which can be used in the preparation of polyol esters of formula (I) are carboxylic acids comprising an aliphatic hydrocarbon radical comprising from 8 to 14 carbon atoms. Mention may for example be made of: decanoic acid, dodecanoic acid, lauric acid, stearic acid, myristic acid, behenic acid, etc. Among the dicarboxylic acids, mention may be made of maleic acid , succinic acid, adipic acid, sebacic acid ... According to a preferred embodiment, the carboxylic acids used to prepare the polyol esters of formula (I) comprise a mixture of monocarboxylic and dicarboxylic acids, the proportion of monocarboxylic acids being in the majority. The presence of dicarboxylic acids results in particular in the formation of polyol esters of high viscosity. In particular, the reaction for forming the polyol esters of formula (I) by reaction between the carboxylic acid and the polyols is an acid-catalyzed reaction. These include a reversible reaction, which can be completed by the use of a large amount of acid or by removing the water formed during the reaction. The esterification reaction can be carried out in the presence of organic or inorganic acids, such as sulfuric acid, phosphoric acid, etc. Preferably, the reaction is carried out in the absence of a catalyst. The amount of carboxylic acid and polyol can vary in the mixture depending on the desired results. In the particular case where all the hydroxyl groups are esterified, a sufficient quantity of carboxylic acid must be added to react with all the hydroxyls. According to one embodiment, when using mixtures of carboxylic acids, these can react sequentially with the polyols. According to a preferred embodiment, when using a mixture of carboxylic acids, a polyol reacts first with a carboxylic acid, typically the highest molecular weight carboxylic acid, followed by the reaction with the acid. carboxylic having an aliphatic hydrocarbon chain. According to one embodiment, the esters can be formed by reaction between the carboxylic acids (or their anhydride derivatives or esters) with the polyols, in the presence of acids at high temperature, while removing the water formed during the reaction. . Typically, the reaction can be carried out at a temperature of from 75 to 200 ° C. According to another embodiment, the polyol esters formed may comprise hydroxyl groups which have not all reacted, in this case these are partially esterified polyol esters. According to a preferred embodiment, the polyol esters are obtained from pentaerythritol alcohol, and from a mixture of carboxylic acids: isononanoic acid, at least one acid having an aliphatic hydrocarbon radical comprising from 8 to 10 carbon atoms, and heptanoic acid. The preferred polyol esters are obtained from pentaerythritol, and from a mixture of 70% isononanoic acid, 15% of at least one carboxylic acid having an aliphatic hydrocarbon radical comprising from 8 to 10 carbon atoms, and 15% heptanoic acid. We can for example quote the oil Solest 68 marketed by CPI Engineering Services Inc. Polyol esters B) According to another embodiment, the polyol esters of the invention comprise at least one ester of one or more branched carboxylic acids comprising at most 8 carbon atoms. The ester is obtained in particular by reacting said branched carboxylic acid with one or more polyols. Preferably, the branched carboxylic acid comprises at least 5 carbon atoms. In particular, the branched carboxylic acid contains from 5 to 8 carbon atoms, and preferably it contains 5 carbon atoms. Preferably, the above-mentioned branched carboxylic acid does not contain 9 carbon atoms. In particular, said carboxylic acid is not 3,5,5-trimethylhexanoic acid. According to a preferred embodiment, the branched carboxylic acid is chosen from 2-methylbutanoic acid, 3-methylbutanoic acid, and their mixtures. According to a preferred embodiment, the polyol is chosen from the group consisting of neopentyl glycol, glycerol, trimethylol propane, pentaerythritol, dipentaerythritol, tripentaerythritol, and their mixtures. According to a preferred embodiment, the polyol esters are obtained from: i) a carboxylic acid chosen from 2-methylbutanoic acid, 3methylbutanoic acid, and mixtures thereof; and ii) a polyol selected from the group consisting of neopentyl glycol, glycerol, trimethylol propane, pentaerythritol, dipentaerythritol, tripentaerythritol, and mixtures thereof. Preferably, the polyol ester is that obtained from 2methylbutanoic acid and pentaerythritol. Preferably the polyol estermethylbutanoic acid and dipentaerythritol. East the one got at go of the acid Preferably the polyol estermethylbutanoic and pentaerythritol. East the one got at go of the acid Preferably the polyol estermethylbutanoic acid and dipentaerythritol. East the one got at go of the acid Preferably the polyol estermethylbutanoic and neopentyl glycol. East the one got at go of the acid Polyol esters C) According to another embodiment, the polyol esters according to the invention are poly (neopentylpolyol) esters obtained by: i) reaction of a neopentylpolyol having the following formula (V): HO-CH2-C-CH2-OR • H (V) in which: each R represents, independently of one another, CH3, C2H5 or CH2OH; p is an integer ranging from 1 to 4; with at least one monocarboxylic acid having 2 to 15 carbon atoms, and in the presence of an acid catalyst, the molar ratio between the carboxyl groups and the hydroxyl groups being less than 1: 1, to form a poly (neopentyl ) partially esterified polyol; and ii) reaction of the partially esterified poly (neopentyl) polyol composition obtained at the end of step i), with another carboxylic acid having from 2 to 15 carbon atoms, to form the final ester composition ( s) of poly (neopentylpolyol). Preferably, reaction i) is carried out with a molar ratio ranging from 1: 4 to 1: 2. Preferably, the neopentylpolyol has the following formula (VI): cii 2 oh R — C — R in which each R represents, independently of each other, CH3, C2H5 or CH2OH. Preferred neopentylpolyols are those chosen from pentaerythritol, dipentaerythritol, tripentaerythritol, tetraerythritol, trimethylolpropane, trimethylolethane, and neopentyl glycol. In particular, neopentylpolyol is pentaerythritol. Preferably, a single neopentylpolyol is used to produce the POE-based lubricant. In some cases, two or more neopentylpolyols are used. This is especially the case when a commercial pentaerythritol product includes small amounts of dipentaerythritol, tripentaerythritol, and tetraerythritol. According to a preferred embodiment, the abovementioned monocarboxylic acid comprises from 5 to 11 carbon atoms, preferably from 6 to 10 carbon atoms. The monocarboxylic acids have in particular the following general formula (VII): R’C (O) OH (VII) in which R ’is a linear or branched C1-C12 alkyl radical, a C6-C12 aryl radical, a C6-C30 aralkyl radical. Preferably, R ’is a C4-C10, and preferably C5-C9, alkyl radical. In particular, the monocarboxylic acid is chosen from the group consisting of butanoic acid, pentanoic acid, hexanoic acid, heptanoic acid, n-octanoic acid, n acid -nonanoic, n-decanoic acid, 3-methylbutanoic acid, 2-methylbutanoic acid, 2,4dimethylpentanoic acid, 2-ethylhexanoic acid, 3.3 acid , 5 trimethylhexanoic acid, benzoic acid, and mixtures thereof. According to a preferred embodiment, the monocarboxylic acid is nheptanoic acid, or a mixture of n-heptanoic acid with another linear monocarboxylic acid, in particular n-octanoic acid and / or ndecanoic acid. Such a mixture of monocarboxylic acid can comprise between 15 and 100 mol% of heptanoic acid and between 85 and 0 mol% of other monocarboxylic acid (s). In particular, the mixture comprises between 75 and 100 mol% of heptanoic acid, and between 25 and 0 mol% of a mixture of octanoic acid and decanoic acid in a 3: 2 molar ratio. According to a preferred embodiment, the polyol esters comprise: i) from 45% to 55% by weight of a monopentaerythritol ester with at least one monocarboxylic acid having from 2 to 15 carbon atoms; ii) less than 13% by weight of a dipentaerythritol ester with at least one monocarboxylic acid having from 2 to 15 carbon atoms; iii) less than 10% by weight of a tripentaerythritol ester with at least one monocarboxylic acid having from 2 to 15 carbon atoms; and iv) at least 25% by weight of an ester of tetraerythritol and other pentaerythritol oligomers, with at least one monocarboxylic acid having 2 to 15 carbon atoms. Polyol esters D) According to another embodiment, the polyol esters according to the invention have the following formula (VIII): H (VIII) in which: R 7 , R 8 , R 9 , R 10 , R 11 and R 12 are, independently of each other, H or CH3; a, b, c, y, x and z, are, independently of each other, an integer; a + x, b + y, and c + z are, independently of each other, integers ranging from 1 to 20; R 13 , R 14 and R 15 are, independently of each other, chosen from the group consisting of aliphatic or branched alkyls, alkenyls, cycloalkyls, aryls, alkylaryls, arylalkyls, alkylcycloalkyls, cycloalkylalkyls, arylcycloalkyls cycloalkylaryl, alkylcycloalkylaryl, alkylarylcycloalkyle, arylcycloalkylalkyle, arylalkylcycloalkyle, cycloalkylalkylaryl and cycloalkylarylalkyle, R 13 , R 14 and R 15 , having from 1 to 17 carbon atoms, and which may be optionally substituted. According to a preferred embodiment, each of R 13 , R 14 and R 15 represents, independently of each other, a linear or branched alkyl group, an alkenyl group, a cycloalkyl group, said alkyl, alkenyl or cycloalkyl groups which may comprise at least at least one heteroatom chosen from N, O, Si, F or S. Preferably, each of R 13 , R 14 and R 15 has, independently of each other, from 3 to 8 carbon atoms, preferably from 5 to 7 carbon atoms. Preferably, a + x, b + y, and c + z are, independently of each other, integers ranging from 1 to 10, preferably from 2 to 8, and even more preferably from 2 to 4. Preferably, R 7 , R 8 , R 9 , R 10 , R 11 and R 12 represent H. The polyol esters of formula (VIII) above can typically be prepared as described in paragraphs [0027] to [0030] of international application WO2012 / 177742. In particular, the polyol esters of formula (VIII) are obtained by esterification of glycerol alkoxylates (as described in paragraph [0027] of WO2012 / 177742) with one or more monocarboxylic acids having from 2 to 18 carbon atoms. According to a preferred embodiment, the monocarboxylic acids have one of the following formulas: R 13 COOH R 14 COOH and R 15 COOH in which R 13 , R 14 and R 15 are as defined above. Derivatives of carboxylic acids can also be used, such as anhydrides, esters and acyl halides. The esterification can be carried out with one or more monocarboxylic acids. Preferred monocarboxylic acids are those chosen from the group consisting of acetic acid, propanoic acid, butyric acid, isobutanoic acid, pivalic acid, pentanoic acid, isopentanoic acid, acid hexanoic, heptanoic acid, octanoic acid, 2-ethylhexanoic acid, 3,3,5-trimethylhexanoic acid, nonanoic acid, decanoic acid, neodecanoic acid, undecanoic acid, dodecanoic acid, tridecanoic acid, myristic acid, pentadecanoic acid, palmitic acid, stearic acid, oleic acid, linoleic acid, palmitoleic acid, lemonellic acid, undecenoic acid, lauric acid, undecylenic acid, linolenic acid, arachidic acid, behenic acid, tetrahydrobenzoic acid, abietic acid, hydrogenated or not, 2-ethylhexanoic acid, furoic acid, benzoic acid, 4acetylbenzoic acid, pyruvic acid, 4-tert-butyl-benzoic acid, naphthenic acid, 2-methyl benzoic acid, salicylic acid, their isomers, their methyl esters, and mixtures thereof. Preferably, the esterification is carried out with one or more monocarboxylic acids chosen from the group consisting of pentanoic acid, 2methylbutanoic acid, n-hexanoic acid, n-heptanoic acid, 3,3,5-trimethylhexanoic , 2-ethylhexanoic acid, n-octanoic acid, nnonanoic acid and isononanoic acid. Preferably, the esterification is carried out with one or more monocarboxylic acids chosen from the group consisting of butyric acid, isobutyric acid, n-pentanoic acid, 2-methylbutanoic acid, 3methylbutanoic acid, l n-hexanoic greedy, n-heptanoic greedy, n-octanoic acid, 2-ethylhexanoic acid, 3,3,5-trimethylhexanoic acid, n-nonanoic acid, decanoic acid, undecanoic acid, undecelenic acid, lauric acid, stearic acid, isostearic acid, and mixtures thereof. According to another embodiment, the polyol esters according to the invention have the following formula (IX): .19 in which: - each of R 17 and R 18 , is, independently of one another, H or CH3; each of m and n, is, independently of one another, an integer, with m + n, being an integer ranging from 1 to 10; R 16 and R 19 are, independently of one another, chosen from the group consisting of aliphatic or branched alkyls, alkenyls, cycloalkyls, aryls, alkylaryls, arylalkyls, alkylcycloalkyls, cycloalkylalkyls, arylcycloalkyls cycloalkylaryl, alkylcycloalkylaryl, alkylarylcycloalkyle, arylcycloalkylalkyle, arylalkylcycloalkyle, cycloalkylalkylaryl and cycloalkylarylalkyle, R 16 and R 19 , having from 1 to 17 carbon atoms, and which may be optionally substituted. According to a preferred embodiment, each of R 16 and R 19 represents, independently of one another, a linear or branched alkyl group, an alkenyl group, a cycloalkyl group, said alkyl, alkenyl or cycloalkyl groups which may comprise at least at least one heteroatom chosen from N, O, Si, F or S. Preferably, each of R 16 and R 19 has, independently of one another, from 3 to 8 carbon atoms, preferably from 5 to 7 carbon atoms. According to a preferred embodiment, each of R 17 and R 18 represents H, and / or m + n is an integer ranging from 2 to 8, from 4 to 10, from 2 to 5, or from 3 to 5. In particular , m + n is 2, 3 or 4. According to a preferred embodiment, the polyol esters of formula (IX) above are diesters of triethylene glycol, diesters of tetraethylene glycol, in particular with one or two monocarboxylic acids having from 4 to 9 carbon atoms. The polyol esters of formula (IX) above can be prepared by esterifications of an ethylene glycol, of a propylene glycol, or of an oligo- or polyalkylene glycol, (which can be an oligo- or polyethylene glycol, oligo- or polypropylene glycol, or an ethylene glycol-propylene glycol block copolymer), with one or two monocarboxylic acids having from 2 to 18 carbon atoms. The esterification can be carried out in an identical manner to the esterification reaction used to prepare the polyol esters of formula (VIII) above. In particular, monocarboxylic acids identical to those used to prepare the polyol esters of formula (VIII) above, can be used to form the polyol esters of formula (IX). According to one embodiment, the lubricant based on polyol esters according to the invention comprises from 20 to 80%, preferably from 30 to 70%, and preferably from 40 to 60% by weight of at least one ester of polyol of formula (VIII), and from 80 to 20%, preferably from 70 to 30%, and preferably from 60 to 40% by weight of at least one polyol ester of formula (IX). In general, certain alcohol functions may not be esterified during the esterification reaction, however their proportion remains low. Thus, the POEs can comprise between 0 and 5 mol% relative of CH2OH units with respect to the -CH 2 -OC (= O) - units. The preferred POE lubricants according to the invention are those having a viscosity of 1 to 1000 centiStokes (cSt) at 40 ° C, preferably from 10 to 200 cSt, even more preferably from 20 to 100 cSt, and advantageously from 30 to 80 cSt . The international classification of oils is given in particular by standard ISO3448-1992 (NF T60-141) and according to which oils are designated by their class of average viscosity measured at a temperature of 40 ° C. According to one embodiment, the content of azeotropic composition according to the invention in the heat transfer composition ranges from 1 to 5% by weight; or from 5 to 10%; or from 10 to 15%; or from 15 to 20%; or from 20 to 25%; or from 25 to 30%; or from 30 to 35%; or from 35 to 40%; or from 40 to 45%; or from 45 to 50%; or from 50 to 55%; or from 55 to 60%; or from 60 to 65%; or from 65 to 70%; or from 70 to 75%; or from 75 to 80%; or from 85%; or from 85 to 90%; or from 90 to 95%; or from 95 to 99%; or from 99 to 99.5%; or from 99.5 to 99.9%; or more than 99.9%, based on the total weight of the heat transfer composition. The content of azeotropic composition according to the invention can also vary in several of the above ranges: for example from 50 to 55%, and from 55 to 60%, that is to say from 50 to 60%, etc. . According to a preferred embodiment, the heat transfer composition comprises more than 50% by weight of azeotropic composition according to the invention, and in particular from 50% to 99% by weight, relative to the total weight of the transfer composition heat. In the heat transfer composition according to the invention, the mass proportion of lubricant, and in particular of lubricant based on polyol esters (POE), can represent in particular from 1 to 5% of the composition; or from 5 to 10% of the composition; or from 10 to 15% of the composition; or from 15 to 20% of the composition; or from 20 to 25% of the composition; or from 25 to 30% of the composition; or from 30 to 35% of the composition; or from 35 to 40% of the composition; or from 40 to 45% of the composition; or from 45 to 50% of the composition; or from 50 to 55% of the composition; or from 55 to 60% of the composition; or from 60 to 65% of the composition; or from 65 to 70% of the composition; or from 70 to 75% of the composition; or from 75 to 80% of the composition; or from 80 to 85% of the composition; or from 85 to 90% of the composition; or from 90 to 95% of the composition; or from 95 to 99% of the composition; or from 99 to 99.5% of the composition; or from 99.5 to 99.9% of the composition; or more than 99.9% of the composition. The lubricant content can also vary in several of the above ranges: for example from 50 to 55%, and from 55 to 60%, that is to say from 50 to 60%, etc. According to one embodiment, the transfer composition comprises (preferably consists of): the azeotropic composition according to the invention comprising (preferably consists of) 77.5% (± 0.2%) by weight of HFO-1234yf, 14% (± 0.2%) by weight of HFC-152a and 8 0.5% (± 0.2%) by weight of HFC-134a, said composition having a boiling point of 26.97 ° C (± 0.50 ° C) at a pressure of 7.3 bar abs (± 0.5%); and at least one lubricant based on polyol esters (POE), in particular chosen from the polyol esters A), B), C) or D) described above, in particular the polyol esters of formulas (I), (VIII) or (XI). Uses The present invention also relates to the use of an azeotropic composition or of a heat transfer composition according to the invention, in a heat transfer system containing a vapor compression circuit, said circuit preferably comprising a separator 'oil. According to one embodiment, the heat transfer system is: - an air conditioning system; or - a refrigeration system; or - a freezing system; or - a heat pump system. The present invention also relates to a heat transfer method based on the use of a heat transfer installation containing a vapor compression circuit which comprises the azeotropic composition or the heat transfer composition according to the invention, said circuit preferably comprising an oil separator. The heat transfer process can be a process of heating or cooling a fluid or a body. The azeotropic composition or the heat transfer composition can also be used in a process for producing mechanical work or electricity, in particular in accordance with a Rankine cycle. The invention also relates to a heat transfer installation comprising a vapor compression circuit containing the azeotropic composition or the heat transfer composition according to the invention, said circuit preferably containing an oil separator, and in particular a compressor. to screw. According to one embodiment, this installation is chosen from mobile or stationary refrigeration, heating (heat pump), air conditioning and freezing installations, and heat engines. It can notably be a heat pump installation, in which case the fluid or body that is heated (generally air and possibly one or more products, objects or organisms) is located in a room or a vehicle interior (for mobile installation). According to a preferred embodiment, it is an air conditioning installation, in which case the fluid or body which is cooled (generally air and possibly one or more products, objects or organisms) is located in a room or vehicle interior (for mobile installation). It can be a refrigeration installation or a freezing installation (or cryogenic installation), in which case the fluid or body that is cooled generally comprises air and one or more products, objects or organisms , located in a room or container. In particular, the heat transfer installation is a heat pump, or an air conditioning installation, for example a chiller. The invention also relates to a method of heating or cooling a fluid or a body by means of a vapor compression circuit containing a heat transfer fluid or a heat transfer composition, said method successively comprising evaporation of the fluid or heat transfer composition, compression of the fluid or heat transfer composition, condensation of the fluid or heat transfer composition, and expansion of the fluid or the heat transfer composition, in which the heat transfer fluid is the azeotropic composition according to the invention, or the heat transfer composition is that described above, said compression circuit preferably comprising an oil separator. The invention also relates to a method of producing electricity by means of a heat engine, said method successively comprising the evaporation of the heat transfer fluid or of a heat transfer composition, the expansion of the fluid or of the heat transfer composition in a turbine for generating electricity, the condensation of the fluid or the heat transfer composition and the compression of the fluid or the heat transfer composition, wherein the transfer fluid heat is the azeotropic composition according to the invention and the heat transfer composition is that described above. The vapor compression circuit, containing a fluid or a heat transfer composition according to the invention, comprises at least one evaporator, preferably a screw compressor, a condenser and an expansion valve, as well as lines for transporting the fluid or of the heat transfer composition between these elements, and optionally an oil separator. The evaporator and the condenser include a heat exchanger allowing heat exchange between the fluid or the heat transfer composition and another fluid or body. The evaporator used in the context of the invention can be an overheated evaporator or a flooded evaporator. In an overheated evaporator, all of the above fluid or heat transfer composition is evaporated at the outlet of the evaporator, and the vapor phase is superheated. In a flooded evaporator, the fluid / heat transfer composition in liquid form does not completely evaporate. A flooded evaporator has a liquid phase and vapor phase separator. As a compressor, it is possible in particular to use a centrifugal compressor with one or more stages or a centrifugal mini-compressor. Rotary, piston or screw compressors can also be used. According to one embodiment, the vapor compression circuit comprises a centrifugal compressor, and preferably a centrifugal compressor and a flooded evaporator. According to another embodiment, the vapor compression circuit comprises a screw compressor, preferably twin-screw or single-screw. In particular, the vapor compression circuit includes a twin-screw compressor, capable of implementing a substantial flow of oil, for example up to 6.3 L / s. A centrifugal compressor is characterized in that it uses rotating elements to radially accelerate the fluid or the heat transfer composition; it typically comprises at least one rotor and one diffuser housed in an enclosure. The heat transfer fluid or the heat transfer composition is introduced into the center of the rotor and flows to the periphery of the rotor under acceleration. Thus, on the one hand the static pressure increases in the rotor, and especially on the other hand at the level of the diffuser, the speed is converted into an increase in the static pressure. Each rotor / diffuser assembly constitutes a stage of the compressor. Centrifugal compressors can have from 1 to 12 stages, depending on the desired final pressure and the volume of fluid to be treated. The compression ratio is defined as the ratio of the absolute pressure of the fluid / composition of heat transfer at the outlet to the absolute pressure of said fluid or of said composition at the inlet. The speed of rotation for large centrifugal compressors ranges from 3000 to 7000 rpm. Small centrifugal compressors (or mini centrifugal compressors) generally operate at a rotational speed ranging from 40,000 to 70,000 revolutions per minute and have a small rotor (generally less than 0.15 m). A multi-stage rotor can be used to improve the efficiency of the compressor and limit the energy cost (compared to a single-stage rotor). For a two-stage system, the output of the first stage of the rotor feeds the inlet of the second rotor. The two rotors can be mounted on a single axis. Each stage can provide a fluid compression ratio of approximately 4 to 1, that is, the absolute outlet pressure can be approximately four times the absolute suction pressure. Examples of two-stage centrifugal compressors, in particular for automotive applications, are described in documents US 5,065,990 and US 5,363,674. The centrifugal compressor can be driven by an electric motor or by a gas turbine (for example powered by vehicle exhaust gases, for mobile applications) or by gear. The installation may include a coupling of the regulator with a turbine to generate electricity (Rankine cycle). The installation can also optionally comprise at least one heat transfer fluid circuit used to transmit heat (with or without change of state) between the circuit of the heat transfer fluid or of the heat transfer composition, and the fluid or body to be heated or cooled. The installation can also optionally include two (or more) vapor compression circuits, containing identical or distinct fluids / heat transfer compositions. For example, the vapor compression circuits can be coupled together. The vapor compression circuit operates according to a conventional vapor compression cycle. The cycle includes changing the state of the fluid / heat transfer composition from a liquid phase (or two-phase liquid / vapor) to a vapor phase at a relatively low pressure, then compressing the fluid / composition into vapor phase to a relatively high pressure, the change of state (condensation) of the fluid / heat transfer composition from the vapor phase to the liquid phase at a relatively high pressure, and reducing the pressure to start again the cycle. In the case of a cooling process, heat from the fluid or from the body which is cooled (directly or indirectly, via a heat transfer fluid) is absorbed by the fluid / the heat transfer composition, during the 'evaporation of the latter, and at a relatively low temperature compared to the environment. The cooling methods include the methods of air conditioning (with mobile installations, for example in vehicles, or stationary), refrigeration and freezing or cryogenics. In the field of air conditioning, mention may be made of domestic, commercial or industrial air conditioning, where the equipment used is either chillers or direct expansion equipment. In the field of refrigeration, we can cite domestic, commercial refrigeration, cold rooms, the food industry, refrigerated transport (trucks, boats). In the case of a heating process, heat is transferred (directly or indirectly, via a heat transfer fluid) from the fluid / heat transfer composition, during the condensation thereof / this, to fluid or to the body that is heated, and this at a relatively high temperature compared to the environment. The installation for carrying out the heat transfer is called in this case "heat pump". They may in particular be medium and high temperature heat pumps. It is possible to use any type of heat exchanger for implementing the compositions (azeotropics or heat transfer) according to the invention, and in particular co-current heat exchangers or, preferably, exchangers against the current. However, according to a preferred embodiment, the invention provides that the cooling and heating methods, and the corresponding installations, include a counter-current heat exchanger, either in the condenser or in the evaporator. In fact, the compositions according to the invention (azeotropic composition or heat transfer composition defined above) are particularly effective with countercurrent heat exchangers. Preferably, both the evaporator and the condenser include a counter-current heat exchanger. According to the invention, by "counter-current heat exchanger" means a heat exchanger in which heat is exchanged between a first fluid and a second fluid, the first fluid at the inlet of the exchanger exchanging heat with the second fluid at the outlet of the exchanger, and the first fluid at the outlet of the exchanger exchanging heat with the second fluid at the inlet of the exchanger. For example, counter-current heat exchangers include devices in which the flow of the first fluid and the flow of the second fluid are in opposite directions, or almost opposite. Exchangers operating in cross-current mode with counter-current tendency are also included among the counter-current heat exchangers within the meaning of the present application. Under different operating conditions (air conditioning, refrigeration, heat pump, etc.), the compositions according to the invention are such that they advantageously induce overheating of the compressor (difference between temperature at the separator and temperature at the condenser) greater than that HFO-1234yf, and / or HFO-1234ze. In "low temperature refrigeration" processes, the temperature of entry of the composition according to the invention (azeotropic or heat transfer composition) to the evaporator is preferably from -45 ° C to -15 ° C, in particular from -40 ° C to -20 ° C, more particularly preferably from -35 ° C to -25 ° C and for example around -30 ° C; and the temperature at the start of the condensation of the composition according to the invention (azeotropic or heat transfer composition) in the condenser is preferably from 25 ° C to 80 ° C, in particular from 30 ° C to 60 ° C, so more particularly preferred from 35 ° C to 55 ° C and for example about 40 ° C. In “moderate temperature cooling” processes, the temperature of entry of the composition according to the invention (azeotropic or heat transfer composition) to the evaporator is preferably from -20 ° C. to 10 ° C., in particular from -15 ° C to 5 ° C, more particularly preferably from -10 ° C to 0 ° C and for example around -5 ° C; and the temperature at the start of the condensation of the composition according to the invention (azeotropic or heat transfer composition) in the condenser is preferably from 25 ° C to 80 ° C, in particular from 30 ° C to 60 ° C, so more particularly preferred from 35 ° C to 55 ° C and for example about 50 ° C. These methods can be refrigeration or air conditioning methods. In “moderate temperature heating” processes, the temperature of entry of the composition according to the invention (azeotropic or heat transfer composition) to the evaporator is preferably from -20 ° C to 10 ° C, in particular from -15 ° C to 5 ° C, more particularly preferably from -10 ° C to 0 ° C and for example around -5 ° C; and the temperature at the start of the condensation of the composition according to the invention (azeotropic or heat transfer composition) in the condenser is preferably from 25 ° C to 80 ° C, in particular from 30 ° C to 60 ° C, so more particularly preferred from 35 ° C to 55 ° C and for example about 50 ° C. In “high temperature heating” processes, the temperature of entry of the composition according to the invention (azeotropic or heat transfer composition) to the evaporator is preferably from -20 ° C. to 90 ° C., in particular from 10 ° C to 90 ° C, more particularly preferably from 50 ° C to 90 ° C and for example around 80 ° C; and the temperature at the start of the condensation of the composition according to the invention (azeotropic or heat transfer composition) in the condenser is preferably from 70 ° C to 160 ° C, in particular from 90 ° C to 150 ° C, so more particularly preferred from 110 ° C. to 140 ° C. and for example approximately 135 ° C. The compositions according to the invention are particularly advantageous in refrigerated transport. Any movement of perishable products under refrigerated space is considered to be refrigerated transport. Food or pharmaceutical products represent an important part of perishable products. Refrigerated transport can be carried out by truck, rail or boat, possibly using multi-platform containers which can be adapted as well on trucks, rails or boats. In refrigerated transport, the temperature of the refrigerated spaces is between -30 ° C and 16 ° C. The refrigerant charge in transport by truck, rail or multi-platform containers varies between 4 kg and 8 kg of refrigerant. Installations in boats can contain between 100 and 500kg. The most widely used refrigerant to date is R404A. The operating temperatures of the refrigeration systems depend on the refrigeration temperature requirements and the outdoor climatic conditions. The same refrigeration installation must be able to cover a wide range of temperatures between -30 ° C and 16 ° C and operate in both cold and hot climates. The most restrictive condition in evaporation temperature is -30 ° C. The compositions according to the invention can be used to replace various heat transfer fluids in various heat transfer applications, such as 1,1,1,2tetrafluoroethane (R134a). Oil separator According to the invention, the vapor compression circuit can comprise an oil separator. According to one embodiment, the oil separator is located between the compressor and the condenser. According to the invention, the oil separator can be a reservoir or a cylinder comprising at least one deflector or screen for collecting the oil. According to one embodiment, the oil separator comprises a float / valve / needle mechanism. In this particular case, the oil, recovered in the separator, is stored in the lower part containing the float / valve / pointer mechanism. When the oil level is high enough to lift the float mechanism, the needle valve system opens and allows the oil to re-enter the crankcase (s) of the compressor (s). The oil return takes place in particular thanks to the pressure difference between that of the oil separator and that of the crankcase (s) of the compressor (s). The oil separator advantageously allows the release of the refrigerant towards the condenser, and the return of the separated lubricating oil, to the compressor. The compression circuit according to the invention may include an oil return line between the oil separator and the inlet of the compressor. In particular, the oil separator comprises an inlet valve (allowing in particular the entry of the composition of the invention), an outlet valve in the upper part of the separator (in particular making it possible to recover part of the refrigerant which will go to the condenser), and an outlet valve in the lower part of the separator (allowing in particular the outlet of the oil for its return to the compressor). Typically, oil separators can use at least one of the following techniques: coalescence: phenomenon by which two identical but dispersed substances tend to come together; centrifugation: this technique uses centrifugal force to separate fluids of different densities; speed reduction: this technique allows the heaviest molecules to continue their trajectory, thanks to their inertia, while the lightest molecules disperse in the internal volume of the oil separator; change of direction: this technique combined with the previous one increases the separation efficiency of the oil droplets (heavy molecules) present in the vapor (light molecules). The oil droplets notably retain their initial trajectory, under the effect of their mass and their initial speed, while the steam is directed towards the outlet of the separator. Coalescence can be achieved using wire screens or coaslescent cartridges. Centrifugation can be carried out using turbulators, helical systems or special arrangements of separators (cyclone). An oil separator can in particular implement several of the above-mentioned techniques. Among the oil separators useful according to the invention, there may be mentioned for example the TURBOIL range from Carly, OUB from Danfoss, OS from Emerson, series 5520 and 5540 from Castel, the Temprite separators and the AC&R separators, the OAS separators from Bitzer for screw compressors. The vapor compression circuit may further include an oil cooling system, and optionally an oil pump and / or an oil distribution system, located between the oil separator and the inlet. compressor. The oil pump can be used to remedy pressure losses and / or to allow the oil to reach a pressure higher than the compressor discharge pressure. The oil cooling system can be used to cool the oil from the compressor and the oil separator. Flammability The compositions according to the present invention also have the advantage of having a flame propagation speed of less than 10 cm / s, preferably less than 8 cm / s, or even 7 cm / s or even 3 cm / s depending on the measurement method developed by Jabbour T - 2004. Some compositions are even non-flammable. The experimental device uses the vertical glass tube method (number of tubes 2, length 150 cm, diameter 40 cm). The use of two tubes makes it possible to make two tests with the same concentration at the same time. The tubes are fitted with tungsten electrodes, which are placed at the bottom of each tube, 6.35mm (1/4 inch) apart and are connected to a 15kV and 30mA generator. The test method is developed in the thesis of T. Jabbour, “Classification of the flammability of refrigerants based on the fundamental flame speed” under the supervision of Denis Clodic. Thesis, Paris, 2004. For example, the flame propagation speed for the composition HFO1234yf / R134a / R152a: 78.9 / 7.0 / 14.1% by mass is 4.75 cm / s and that of the composition HFO-1234yf / R134a / R152a: 74.2 / 7.7 / 18.1% by mass is 6 cm / s. All of the embodiments described above can be combined with each other. Thus, each preferred azeotropic composition can be combined with each additive and in particular with each preferred polyol ester (esters A, B, C or D), in the various proportions mentioned. The various preferred compositions can be used in the various applications described above. FIGURE 1: Figure 1 is a diagram of the R134a / Triton SE 55 oil mixture representing the temperature (in ° C) on the abscissa and the pressure (bar) on the ordinate, produced under the operating conditions of the example below . At 0% oil, we have 100% R134a, while at 70% oil, we have a mixture comprising 30% R134a. This diagram shows that at constant pressure, the concentration of the refrigerant in the oil decreases when the temperature of the mixture Ts increases. The following examples illustrate the invention without, however, limiting it. EXAMPLES POE Triton SE 55 d oil supplier: FUCHS In an oil separator integrated into a screw compressor, the oil is collected in the lower part of the separator. In this example, the amounts of refrigerant trapped by the oil in the separator are analyzed. The refrigerant / oil mixture in the separator is at a temperature Ts (which is also the temperature of the refrigerant at the outlet of the compressor) and the pressure in the separator is equal to the vapor saturation pressure of the refrigerant at the inlet of the condenser ( Pcond). Therefore, this results in a system which works at a condensation temperature (Tcond), which is the saturation temperature of the refrigerant alone at the corresponding pressure Pcond. In general, the analysis of a typical refrigerant / oil diagram (as illustrated for example in FIG. 1 for R134a) shows that, at constant pressure (Pcond), the concentration of the refrigerant in the oil decreases when the temperature of the mixture (oil / refrigerant, Ts) increases and moves away from the saturation temperature of the refrigerant alone (Tcond), the difference between Ts and Tcond representing the overheating at the outlet of the compressor. The temperature Tcond, the pressure Pcond and the temperature Ts in the oil separator are defined by the operating requirements of the installation. The percentage of oil in the refrigerant will therefore be deduced from the corresponding refrigerant / oil diagram at the pressure Pcond and at the temperature Ts. This method makes it possible to compare refrigerants indirectly by looking at the overheating at the compressor outlet. Consider an air conditioning system that works under the following conditions in heating mode (heat pump): Condensation temperature Tcond = 70 ° C; Evaporation temperature: 0 ° C; Overheating in the evaporator: 0 ° C; Under cooling: 0 ° C; Compressor efficiency: 75%; - Reference case: R134a and POE Triton SE 55 oil; According to the diagram in Figure 1, for a temperature (Ts) in the separator of 87 ° C and a pressure of 21 bar abs, the superheat at the outlet of the compressor is 17 ° C, this gives a percentage d 'oil of 75% by mass (25% by mass of R134a in oil). For an HFO-1234yf / POE Triton SE 55 oil mixture, under the same operating conditions described above, the condenser pressure is approximately 20.5 bar abs and the superheat at the compressor outlet is approximately 4, 8 ° C. The HFO-1234yf has a saturation pressure very close to the R134a but a slight overheating. Consequently, the concentration of the refrigerant in the liquid phase of the oil separator will be greater than 30%, even 35%, by mass. Consequently, for the same circulation rate of the oil / coolant liquid, the increase in the percentage of coolant in the oil of the separator results in a decrease in the quantity of lubricating oil circulating in the compressor and also in a decrease in the viscosity of the oil / coolant mixture. Therefore, direct replacement of R134a with HFO-1234yf can damage the compressor (lubrication problem, low viscosity) and reduce performance. The table below gives the superheat value at the compressor output in relation to the condensing temperature under the same operating conditions, described above for R134a and HFO-1234yf, for different mixtures: Ratio A corresponds to the following ratio: [overheating at the compressor of the mixture - overheating at the compressor of 1234y / d A = r overheating at the compressor of 1234y / X 100 P (bar) Temperature (° C) condenser evaporator evaporator inlet compressor output condenser vapor saturation compressor overheating < HFO-1234yf 20.45 3.16 0.0 74.8 70.0 4.8 0 HFO-1234ze 16.11 2.17 0.0 77.2 70.0 7.2 50 R134a 21.17 2.93 0.0 87.6 70.0 17.6 266 R1234yf R134a R152a 81.5 6.5 12.0 20.90 3.18 0.0 79.1 70.0 9.0 88 80.5 7.5 12.0 20.92 3.18 0.0 79.2 70.0 9.2 90 79.5 8.5 12.0 20.95 3.18 0.0 79.3 70.0 9.3 93 78.5 9.5 12.0 20.97 3.18 0.0 79.4 70.0 9.4 95 77.5 10.5 12.0 21.00 3.18 0.0 79.6 70.0 9.5 98 79.5 6.5 14.0 20.90 3.18 0.0 79.6 70.0 9.6 100 78.5 7.5 14.0 20.93 3.18 0.0 79.8 70.0 9.7 102 77.5 8.5 14.0 20.95 3.18 0.0 79.9 70.0 9.9 105 76.5 9.5 14.0 20.97 3.18 0.0 80.0 70.0 10.0 108 75.5 10.5 14.0 20.99 3.18 0.0 80.1 70.0 10.1 110 77.5 6.5 16.0 20.90 3.17 0.0 80.2 70.0 10.2 112 76.5 7.5 16.0 20.92 3.17 0.0 80.4 70.0 10.3 115 75.5 8.5 16.0 20.94 3.17 0.0 80.5 70.0 10.5 117 74.5 9.5 16.0 20.96 3.17 0.0 80.6 70.0 10.6 120 73.5 10.5 16.0 20.98 3.17 0.0 80.7 70.0 10.7 122 The azeotropic compositions according to the invention advantageously have higher compressor overheating than HFO-1234yf alone, and in particular a coefficient A, as defined above, greater than 80%, or even even greater than 100%, relative to the HFO-1234yf alone. Thus, the mixtures according to the invention advantageously make it possible to reduce (and / or avoid) the amount of refrigerant trapped in the lubricating oil compared to HFO1234yf alone, and therefore to increase the efficiency of the installation by due to the higher refrigerant circulation in the system. In addition, with the mixtures of the invention, the quantity of lubricating oil recovered by the separator being higher than with the HFO-1234yf, better lubrication of the compressor is obtained.
权利要求:
Claims (17) [1" id="c-fr-0001] 1. Azeotropic composition comprising from 74 to 81.5% by weight of HFO-1324yf, from 6.5 to 10.5% by weight of HFC-134a, and from 12 to 16% by weight of HFC-152a, relative the total weight of the composition, said azeotropic composition having a boiling temperature between -40.00 ° C and 70.00 ° C, at a pressure between 0.5 and 21.0 bar abs (± 0.5 %). [2" id="c-fr-0002] 2. Composition according to claim 1 comprising from 75.5 to 79.5% by weight of HFO-1234yf, from 12 to 16% by weight of HFC-152a, and from 6.5 to 10.5% by weight of HFC -134a, relative to the total weight of the composition, said composition having a boiling temperature between -40.00 ° C and 70.00 ° C, at a pressure between 0.5 and 21.0 bar abs ( ± 0.5%). [3" id="c-fr-0003] 3. Composition according to any one of claims 1 or 2, comprising 77.5% (± 0.2%) by weight of HFO-1234yf, 14% (± 0.2%) by weight of HFC-152a and 8 , 5% (+ 0.2%) by weight of HFC-134a, relative to the total weight of the composition, said composition having a boiling temperature between -40.00 ° C and 70.00 ° C, at a pressure between 0.5 and 21.0 bar abs (± 0.5%). [4" id="c-fr-0004] 4. Composition according to any one of claims 1 to 3, comprising 77.5% (± 0.2%) by weight of HFO-1234yf, 14% (± 0.2%) by weight of HFC-152a and 8 , 5% (± 0.2%) by weight of HFC-134a, relative to the total weight of the composition, said composition having a boiling temperature of 26.97 ° C (± 0.50 ° C) at a pressure of 7.3 bar abs (± 0.5%). [5" id="c-fr-0005] 5. Composition according to any one of claims 1 or 2, comprising 77.5% by weight of HFO-1234yf, 16% by weight of HFC-152a and 6.5% by weight of HFC-134a, relative to the weight total of the composition, said composition having a boiling temperature between -40.00 ° C and 70.00 ° C, at a pressure between 0.5 and 21.0 bar abs (± 0.5%). [6" id="c-fr-0006] 6. Composition according to claim 5, comprising 77.5% by weight of HFO1234yf, 16% by weight of HFC-152a and 6.5% by weight of HFC-134a, relative to the total weight of the composition, said composition having a boiling point of 26.97 ° C (± 0.50 ° C) at a pressure of 7.3 bar abs (± 0.5%). [7" id="c-fr-0007] 7. Composition according to claim 1, comprising 81.5% by weight of HFO1234yf, 12% by weight of HFC-152a and 6.5% by weight of HFC-134a, relative to the total weight of the composition, said composition having a boiling temperature between -40.00 ° C and 70.00 ° C, at a pressure between 0.5 and 21.0 bar abs (± 0.5%). [8" id="c-fr-0008] 8. Composition according to claim 7, comprising 81.5% by weight of HFO1234yf, 12% by weight of HFC-152a and 6.5% by weight of HFC-134a, relative to the total weight of the composition, said composition having a boiling point of 26.97 ° C (± 0.50 ° C) at a pressure of 7.3 bar abs (± 0.5%). [9" id="c-fr-0009] 9. Composition according to any one of claims 1 or 2, comprising 75.5% (± 0.2%) by weight of HFO-1234yf, 14.5% (± 0.2%) by weight of HFC-152a and 10% (± 0.2%) by weight of HFC-134a, relative to the total weight of the composition, said composition having a boiling temperature between -40.00'C and 70.00'C, at a pressure between 0.5 and 21.0 bar abs (± 0.5%). [10" id="c-fr-0010] 10. Composition according to claim 9, comprising 75.5% (± 0.2%) by weight of HFO-1234yf, 14.5% (± 0.2%) by weight of HFC-152a and 10% (± 0 , 2%) by weight of HFC-134a, relative to the total weight of the composition, said composition having a boiling temperature of 26.97 ° C (± 0.50 ° C) at a pressure of 7.3 bar abs (± 0.5%). [11" id="c-fr-0011] 11. Composition according to any one of claims 1 or 2, comprising 77.5% by weight of HFO-1234yf, 12% by weight of HFC-152a and 10.5% by weight of HFC-134a, relative to the weight total of the composition, said composition having a boiling temperature between -40.00 ° C and 70.00 ° C, at a pressure between 0.5 and 21.0 bar abs (± 0.5%), and preferably between 0.61 and 21.00 bar abs (+ 0.5%). [12" id="c-fr-0012] 12. Composition according to claim 11, comprising 77.5% by weight of HFO1234yf, 12% by weight of HFC-152a and 10.5% by weight of HFC-134a, relative to the total weight of the composition, said composition having a boiling point of 26.97 ° C (± 0.50 ° C) at pressure of 7.3 (± 0.5%). [13" id="c-fr-0013] 13. A heat transfer composition comprising the azeotropic composition according to any one of claims 1 to 12, and at least one additive in particular chosen from nanoparticles, stabilizers, surfactants, tracer agents, fluorescent agents, odorous agents , lubricants, preferably based on polyol esters, and solubilizers. [14" id="c-fr-0014] 14. Use of an azeotropic composition according to any one of claims 1 to 12, or of a heat transfer composition according to claim 13, in a heat transfer system containing a vapor compression circuit, said circuit preferably comprising an oil separator. [15" id="c-fr-0015] 15. Heat transfer installation comprising a vapor compression circuit containing the azeotropic composition according to any one of claims 1 to 12 or the heat transfer composition according to claim 13, said circuit preferably containing an oil separator , and in particular a screw compressor. [16" id="c-fr-0016] 16. Installation according to claim 15, chosen from mobile or stationary installations for heating by heat pump, air conditioning, refrigeration, freezing and heat engines. [17" id="c-fr-0017] 17. A method of heating or cooling a fluid or a body by means of a vapor compression circuit containing a heat transfer fluid or a heat transfer composition, said method successively comprising the evaporation of the fluid or heat transfer composition, compression of the fluid or heat transfer composition, condensation of the fluid or heat transfer composition, and expansion of the fluid or heat transfer composition, wherein the heat transfer fluid is the azeotropic composition according to any of claims 1 to 12, and the heat transfer composition is that according to claim 13, said compression circuit preferably comprising an oil separator. 1/1 R134a / TrifonSE55 PRESSURE (BAR) -20 -10 0 10 20 30 40 50 60 70 80 90 100 110 120 TEMPERATURE (“C)
类似技术:
公开号 | 公开日 | 专利标题 FR3057271A1|2018-04-13|USE OF TETRAFLUOROPROPENE COMPOSITIONS EP3523389B1|2022-03-16|Tetrafluoropropene-based azeotropic compositions EP3571259A1|2019-11-27|Composition comprising 2,3,3,3-tetrafluoropropene EP3516007B1|2022-01-05|Composition comprising 1-chloro-3,3,3-trifluoropropene WO2018134530A1|2018-07-26|Composition comprising 2,3,3,3-tetrafluoropropene EP3630909A1|2020-04-08|Trifluoroethylene-based compositions and uses thereof EP3752573A1|2020-12-23|Heat transfer compositions as replacement for r-134a WO2019158857A1|2019-08-22|Vehicle heating and/or air-conditioning system WO2018162865A1|2018-09-13|Quasi-azeotropic composition comprising 2,3,3,3-tetrafluoropropene and trans-1,3,3,3-tetrafluoropropene EP3601468B1|2021-10-20|Tetrafluoropropene-based composition
同族专利:
公开号 | 公开日 MX2019004099A|2019-08-05| CN109844055A|2019-06-04| US20200048518A1|2020-02-13| EP3523389A1|2019-08-14| EP3523389B1|2022-03-16| CN109844055B|2021-05-04| WO2018069620A1|2018-04-19| JP2019536884A|2019-12-19| KR20190060816A|2019-06-03| FR3057272B1|2020-05-08|
引用文献:
公开号 | 申请日 | 公开日 | 申请人 | 专利标题 US20110089366A1|2008-06-11|2011-04-21|Arkema France|Hydrofluoroolefin compositions| US20100122545A1|2008-11-19|2010-05-20|E. I. Du Pont De Nemours And Company|Tetrafluoropropene compositions and uses thereof| KR20110029417A|2009-09-15|2011-03-23|인하대학교 산학협력단|Ternary refrigerant mixture composed of r1234yf, r152a and r134a| US5065990A|1986-12-15|1991-11-19|Susan M. Durfee|Vise jaw accessory system for attaching and releasing vise accessories while maintaining positional accuracy of the accessories| BE1005222A3|1991-01-18|1993-06-01|Solvay|Compositions comprising 1,1,1,2-tetrafluoroethane and uses thereof.| US5363674A|1993-05-04|1994-11-15|Ecoair Corp.|Zero superheat refrigeration compression system| TR201908011T4|2002-10-25|2019-06-21|Honeywell Int Inc|Compositions containing fluorine-substituted olefins.| US7279451B2|2002-10-25|2007-10-09|Honeywell International Inc.|Compositions containing fluorine substituted olefins| JP4110388B2|2003-01-10|2008-07-02|荒川化学工業株式会社|Cleaning agent and rinsing agent for gold-plated parts, cleaning method and rinsing method| US20060243944A1|2005-03-04|2006-11-02|Minor Barbara H|Compositions comprising a fluoroolefin| EP2367601B1|2008-11-19|2015-10-28|E. I. du Pont de Nemours and Company|Tetrafluoropropene compositions and uses thereof| FR2957083B1|2010-03-02|2015-12-11|Arkema France|HEAT TRANSFER FLUID FOR CENTRIFUGAL COMPRESSOR| FR2971512B1|2011-02-10|2013-01-18|Arkema France|BINARY COMPOSITIONS OF 2,3,3,3-TETRAFLUOROPROPENE AND AMMONIA| FR2974812B1|2011-05-04|2014-08-08|Arkema France|HEAT TRANSFER COMPOSITIONS HAVING IMPROVED MISCIBILITY WITH LUBRICATING OIL| US9187682B2|2011-06-24|2015-11-17|Emerson Climate Technologies, Inc.|Refrigeration compressor lubricant| CN105038711A|2015-07-30|2015-11-11|天津大学|Mixed refrigerant containing 1,1-difluoroethane| CN105199674A|2015-10-30|2015-12-30|山东华安新材料有限公司|Refrigerant composition|FR2936806B1|2008-10-08|2012-08-31|Arkema France|REFRIGERANT FLUID| FR2937328B1|2008-10-16|2010-11-12|Arkema France|HEAT TRANSFER METHOD| US20170080773A1|2008-11-03|2017-03-23|Arkema France|Vehicle Heating and/or Air Conditioning Method| FR3055014B1|2016-08-10|2020-03-13|Arkema France|AZEOTROPE OR QUASI-AZEOTROPE COMPOSITION COMPRISING 1,1,1,2,2-PENTAFLUOROPROPANE AND TRANS-1,3,3,3-TETRAFLUOROPROPENE| FR3057271B1|2016-10-10|2020-01-17|Arkema France|USE OF TETRAFLUOROPROPENE COMPOSITIONS| FR3077572B1|2018-02-05|2021-10-08|Arkema France|TERNARY AZEOTROPIC OR QUASI-AZEOTROPIC COMPOSITION COMPRISING HF, 2,3,3,3-TETRAFLUOROPROPENE AND 1,1,1,2,2, -PENTAFLUOROPROPANE.|
法律状态:
2017-09-18| PLFP| Fee payment|Year of fee payment: 2 | 2018-04-13| PLSC| Search report ready|Effective date: 20180413 | 2018-09-13| PLFP| Fee payment|Year of fee payment: 3 | 2019-09-13| PLFP| Fee payment|Year of fee payment: 4 | 2020-09-14| PLFP| Fee payment|Year of fee payment: 5 | 2021-09-13| PLFP| Fee payment|Year of fee payment: 6 |
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申请号 | 申请日 | 专利标题 FR1659749|2016-10-10| FR1659749A|FR3057272B1|2016-10-10|2016-10-10|AZEOTROPIC COMPOSITIONS BASED ON TETRAFLUOROPROPENE|FR1659749A| FR3057272B1|2016-10-10|2016-10-10|AZEOTROPIC COMPOSITIONS BASED ON TETRAFLUOROPROPENE| MX2019004099A| MX2019004099A|2016-10-10|2017-10-09|Tetrafluoropropene-based azeotropic compositions.| JP2019540709A| JP2019536884A|2016-10-10|2017-10-09|Azeotropic compositions based on tetrafluoropropene| EP17787238.9A| EP3523389B1|2016-10-10|2017-10-09|Tetrafluoropropene-based azeotropic compositions| US16/339,903| US20200048518A1|2016-10-10|2017-10-09|Tetrafluoropropene-based azeotropic compositions| KR1020197012594A| KR20190060816A|2016-10-10|2017-10-09|The tetrafluoropropene-based < RTI ID = 0.0 > azeotropic composition| PCT/FR2017/052764| WO2018069620A1|2016-10-10|2017-10-09|Tetrafluoropropene-based azeotropic compositions| CN201780062362.5A| CN109844055B|2016-10-10|2017-10-09|Azeotrope compositions based on tetrafluoropropene| 相关专利
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