EP2922930A1 - Refrigerant composition - Google Patents
Refrigerant compositionInfo
- Publication number
- EP2922930A1 EP2922930A1 EP13801627.4A EP13801627A EP2922930A1 EP 2922930 A1 EP2922930 A1 EP 2922930A1 EP 13801627 A EP13801627 A EP 13801627A EP 2922930 A1 EP2922930 A1 EP 2922930A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- hfc
- weight
- composition
- composition according
- pentafluoroethane
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Withdrawn
Links
Classifications
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K5/00—Heat-transfer, heat-exchange or heat-storage materials, e.g. refrigerants; Materials for the production of heat or cold by chemical reactions other than by combustion
- C09K5/02—Materials undergoing a change of physical state when used
- C09K5/04—Materials undergoing a change of physical state when used the change of state being from liquid to vapour or vice versa
- C09K5/041—Materials undergoing a change of physical state when used the change of state being from liquid to vapour or vice versa for compression-type refrigeration systems
- C09K5/044—Materials undergoing a change of physical state when used the change of state being from liquid to vapour or vice versa for compression-type refrigeration systems comprising halogenated compounds
- C09K5/045—Materials undergoing a change of physical state when used the change of state being from liquid to vapour or vice versa for compression-type refrigeration systems comprising halogenated compounds containing only fluorine as halogen
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B1/00—Compression machines, plants or systems with non-reversible cycle
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K2205/00—Aspects relating to compounds used in compression type refrigeration systems
- C09K2205/10—Components
- C09K2205/12—Hydrocarbons
- C09K2205/122—Halogenated hydrocarbons
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K2205/00—Aspects relating to compounds used in compression type refrigeration systems
- C09K2205/22—All components of a mixture being fluoro compounds
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K2205/00—Aspects relating to compounds used in compression type refrigeration systems
- C09K2205/40—Replacement mixtures
Definitions
- ODP ozone depletion potential
- 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.
- GWP Global Warming Potential
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Combustion & Propulsion (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Lubricants (AREA)
Abstract
The invention relates to refrigerant fluids that can be used in different types of compression systems. The invention more specifically relates to a composition comprising between 36 and 39 wt. % of difluromethane (HFC-32), between 28 and 32 wt. % of pentafluoroethane (HFC-125), and between 31 and 35 wt. % of tetrafluoroethane (HFC-134a), as a replacement for the R-404A.
Description
Composition réfrigérante Refrigerant composition
La présente invention concerne des fluides frigorigènes aptes à être utilisés dans différents types de systèmes à compression en remplacement du réfrigérant R-404A. The present invention relates to refrigerants suitable for use in various types of compression systems as a replacement for R-404A refrigerant.
L'utilisation de fluide frigorigène dans des systèmes de réfrigération à compression est largement répandue dans les domaines de la réfrigération industrielle, commerciale et à usage domestique. The use of refrigerant in compression refrigeration systems is widespread in the fields of industrial, commercial and domestic refrigeration.
Les problèmes posés par les substances appauvrissant la couche d'ozone atmosphérique (ODP : ozone depletion potential) ont été traités à Montréal où a été signé le protocole imposant une réduction de la production et de l'utilisation des chlorofluorocarbures (CFC). Ce protocole a fait l'objet d'amendements qui ont imposé l'abandon des CFC et étendu la réglementation à d'autres produits, dont les hydrochlorofluorocarbones (HCFC). The problems posed by ozone depletion potential (ODP) have been addressed in Montreal, where the protocol for reducing the production and use of chlorofluorocarbons (CFCs) has been signed. This protocol has been amended to remove CFCs and extend the regulation to include other products, including hydrochlorofluorocarbons (HCFCs).
L'industrie de la réfrigération et de la production d'air conditionné a beaucoup investi dans la substitution de ces fluides frigorigènes et c'est ainsi que les hydrofluorocarbures (HFC) ont été commercialisés. The refrigeration and air-conditioning industry has invested heavily in the substitution of these refrigerants and so hydrofluorocarbons (HFCs) have been marketed.
La contribution à l'effet de serre d'un fluide est quantifiée par un critère, le GWP (Global Warming Potential) qui résume le pouvoir de réchauffement en prenant une valeur de référence de 1 pour le dioxyde de carbone. 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.
Le fluide frigorigène R-404A est un mélange de fluoroéthanes, i.e., R- 143a, R-125 et R-134a ayant un GWP de 3922. Ce fluide a un GWP élevé majoritairement à cause de la présence du R-143a qui a un GWP de 4470. Un fluide ayant un GWP élevé nécessite d'être remplacé. Il existe donc un besoin important de développer un fluide de remplacement du R-404A, pouvant fonctionner dans les mêmes systèmes à compression.
Selon un premier aspect, l'invention concerne ainsi des compositions comprenant au moins de 36 à 39 % en poids de difluorométhane (HFC-32), de 28 à 32 % en poids de pentafluoroethane (HFC-125) et de 31 à 35 % en poids de tetrafluoroethane (HFC-134a). The refrigerant R-404A is a mixture of fluoroethanes, ie, R-143a, R-125 and R-134a having a GWP of 3922. This fluid has a high GWP mainly because of the presence of R-143a which has a GWP of 4470. A fluid with a high GWP needs to be replaced. There is therefore an important need to develop a replacement fluid for R-404A, which can operate in the same compression systems. According to a first aspect, the invention thus relates to compositions comprising at least 36 to 39% by weight of difluoromethane (HFC-32), from 28 to 32% by weight of pentafluoroethane (HFC-125) and from 31 to 35% by weight. by weight of tetrafluoroethane (HFC-134a).
De préférence, les compositions selon l'invention sont caractérisée en ce que la somme des poids des composés HFC-32, HFC-125 et HFC-134a est égale à 100 %. Preferably, the compositions according to the invention are characterized in that the sum of the weights of the compounds HFC-32, HFC-125 and HFC-134a is equal to 100%.
Dans un mode de réalisation selon l'invention, on préfère une composition consistant en 37 % en poids de difluorométhane (HFC-32), 30 % en poids de pentafluoroethane (HFC-125), et 33 % en poids de tetrafluoroethane (HFC-134a). In one embodiment according to the invention, a composition consisting of 37% by weight of difluoromethane (HFC-32), 30% by weight of pentafluoroethane (HFC-125), and 33% by weight of tetrafluoroethane (HFC-125) is preferred. 134a).
Une possibilité offerte par la présente invention est l'utilisation des compositions préalablement citées en tant que fluide réfrigérant. One possibility offered by the present invention is the use of the previously mentioned compositions as a coolant.
Dans un mode de réalisation préféré, les compositions selon l'invention sont utilisées en remplacement du R-404A. In a preferred embodiment, the compositions according to the invention are used instead of R-404A.
L'invention concerne également un procédé de réfrigération comprenant au moins une étape de condensation suivit d'une étape d'évaporation d'une composition décrite précédemment. The invention also relates to a refrigeration process comprising at least one condensation step followed by a step of evaporation of a composition described above.
Dans un mode de réalisation préféré, le procédé selon l'invention comprend une étape de condensation réalisée à une température supérieure à 13 °C, de préférence supérieure à 24 °C. Selon un mode de réalisation tout particulièrement préféré, le procédé selon l'invention, comprend une étape d'évaporation réalisée à une température inférieure ou égale à -10 °C.
L'invention a également pour objet un dispositif pour transfert de chaleur dans un cycle de compression renfermant une composition décrite précédemment. In a preferred embodiment, the process according to the invention comprises a condensation step carried out at a temperature above 13 ° C., preferably above 24 ° C. According to a very particularly preferred embodiment, the process according to the invention comprises an evaporation step carried out at a temperature of less than or equal to -10 ° C. The invention also relates to a device for heat transfer in a compression cycle containing a composition described above.
Les performances du mélange noté «Mélange 1 » constitué de 37 % en poids de difluorométhane (HFC-32), 30 % en poids de pentafluoroethane (HFC- 125), 33 % en poids de tetrafluoroethane (HFC-134a) sont comparées à celles du R-404A en simulant les performances avec le logiciel Cycle D, NIST- version 5.0 dans les conditions opératoires suivantes et sont présentées ci-après: The performance of the mixture noted "Mixture 1" consisting of 37% by weight of difluoromethane (HFC-32), 30% by weight of pentafluoroethane (HFC-125), 33% by weight of tetrafluoroethane (HFC-134a) are compared with those the R-404A by simulating performance with Cycle D software, NIST version 5.0 under the following operating conditions and are presented below:
Température d'évaporation : -32 °C Evaporation temperature: -32 ° C
Température de condensation : 43 °C Condensation temperature: 43 ° C
Sous-refroidissement : 5 °C Subcooling: 5 ° C
Surchauffe : 5 °C Overheating: 5 ° C
Puissance frigorifique : 10 kW Cooling capacity: 10 kW
Coefficient isentropique du compresseur : 0,7 Isentropic coefficient of the compressor: 0.7
Le GWP est calculé selon le 4ème rapport de l'IPCC (2007) The GWP is calculated according to the 4th report of the IPCC (2007)
Les performances du «Mélange 1 » à différentes températures de condensation et d'évaporation sont présentées ci-après et comparées à celles du R404A :
Réfrigérant R-404A Mélange 1 The performances of "Mixture 1" at different temperatures of condensation and evaporation are presented below and compared to those of R404A: Refrigerant R-404A Mixture 1
GWP 3922 1722 GWP 3922 1722
Température de condensation (°C) 13 24 35 43 13 24 35 43 Condensing temperature (° C) 13 24 35 43 13 24 35 43
Température d'évaporation (°C) -32 -32 -10 -20 -32 -10 -20 -32 -32 -32 -10 -20 -32 -10 -20 -32Evaporation temperature (° C) -32 -32 -10 -20 -32 -10 -20 -32 -32 -32 -10 -20 -32 -10 -20 -32
Pression d'évaporation (bar) 1.8 1.8 4.3 3.0 1.8 4.3 3.0 1.8 1.6 1.6 3.9 2.7 1.6 3.9 2.7 1.6Evaporation pressure (bar) 1.8 1.8 4.3 3.0 1.8 4.3 3.0 1.8 1.6 1.6 3.9 2.7 1.6 3.9 2.7 1.6
Pression de condensation (bar) 8.8 12.0 15.9 15.9 15.9 19.3 19.3 19.3 9.2 12.6 16.9 16.9 16.9 20.6 20.6 20.6Condensing pressure (bar) 8.8 12.0 15.9 15.9 15.9 19.3 19.3 19.3 9.2 12.6 16.9 16.9 16.9 20.6 20.6 20.6
Capacité frigorifique (kJ/mJ) 1343 1 191 2589 1738 1032 2318 1547 912 1308 1 199 2746 1838 1084 2541 1697 998Refrigeration capacity (kJ / m J ) 1343 1 191 2589 1738 1032 2318 1547 912 1308 1 199 2746 1838 1084 2541 1697 998
Coefficient de Performance 3.1 2.3 3.2 2.3 1.7 2.5 1.9 1.4 2.9 2.2 3.1 2.4 1.7 2.5 1.9 1.5Coefficient of Performance 3.1 2.3 3.2 2.3 1.7 2.5 1.9 1.4 2.9 2.2 3.1 2.4 1.7 2.5 1.9 1.5
Débit massique (kg/h) 254 287 296 310 331 330 349 375 178 194 201 207 215 217 224 233Mass flow (kg / h) 254 287 296 310 331 330 349 375 178 194 201 207 215 217 224 233
Capacité frigorifique par rapport au R-404A (%) - - - - - - - - 97 101 106 106 105 1 10 1 10 109Cooling capacity compared to R-404A (%) - - - - - - - - 97 101 106 106 105 1 10 1 10 109
COP par rapport au R-404A (%) - - - - - - - - 95 99 98 100 102 101 104 106
COP to R-404A (%) - - - - - - - - 95 99 98 100 102 101 104 106
Claims
1 . Composition comprenant : 1. Composition comprising:
a. 36 à 39 % en poids de difluorométhane (HFC-32) at. 36 to 39% by weight of difluoromethane (HFC-32)
b. 28 à 32 % en poids de pentafluoroethane (HFC-125) b. 28 to 32% by weight of pentafluoroethane (HFC-125)
c. 31 à 35 % en poids de tetrafluoroethane (HFC-134a) vs. 31 to 35% by weight of tetrafluoroethane (HFC-134a)
2. Composition selon la revendication 1 , dans laquelle la somme des poids des composés HFC-32, HFC-125, HFC-134a est égale à 100 %. 2. Composition according to claim 1, wherein the sum of the weights of the compounds HFC-32, HFC-125, HFC-134a is equal to 100%.
3. Composition selon la revendication 1 ou 2, consistant en : 3. Composition according to claim 1 or 2, consisting of:
a. 37 % en poids de difluorométhane (HFC-32) at. 37% by weight of difluoromethane (HFC-32)
b. 30 % en poids de pentafluoroethane (HFC-125) b. 30% by weight of pentafluoroethane (HFC-125)
c. 33 % en poids de tetrafluoroethane (HFC-134a) vs. 33% by weight of tetrafluoroethane (HFC-134a)
4. Utilisation de la composition selon l'une quelconque des revendications 1 à 3 comme réfrigérant. 4. Use of the composition according to any one of claims 1 to 3 as a refrigerant.
5. Utilisation selon la revendication 4, en remplacement du R-404A. 5. Use according to claim 4, replacing R-404A.
6. Procédé de réfrigération comprenant les étapes suivantes : 6. Refrigeration process comprising the following steps:
a. Condensation d'une composition selon l'une quelconque des revendications 1 à 3 ; at. Condensation of a composition according to any one of claims 1 to 3;
b. Evaporation de la dite composition. b. Evaporation of the said composition.
7. Procédé selon la revendication 6, dans lequel l'étape de condensation est réalisée à une température supérieure à 13 °C, de préférence supérieure à 24 °C.
7. The method of claim 6, wherein the condensation step is carried out at a temperature above 13 ° C, preferably above 24 ° C.
8. Procédé selon l'une quelconque des revendications 6 ou 7, dans lequel l'étape d'évaporation est réalisée à une température inférieure ou égale à -10 °C. The process according to any one of claims 6 or 7, wherein the evaporation step is carried out at a temperature of less than or equal to -10 ° C.
9. Dispositif pour transfert de chaleur dans un cycle de compression renfermant la composition selon l'une quelconque des revendications 1 à 3.
9. Device for heat transfer in a compression cycle containing the composition according to any one of claims 1 to 3.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR1261033A FR2998302B1 (en) | 2012-11-20 | 2012-11-20 | REFRIGERANT COMPOSITION |
PCT/FR2013/052594 WO2014080104A1 (en) | 2012-11-20 | 2013-10-30 | Refrigerant composition |
Publications (1)
Publication Number | Publication Date |
---|---|
EP2922930A1 true EP2922930A1 (en) | 2015-09-30 |
Family
ID=47754677
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP13801627.4A Withdrawn EP2922930A1 (en) | 2012-11-20 | 2013-10-30 | Refrigerant composition |
Country Status (7)
Country | Link |
---|---|
US (1) | US9752069B2 (en) |
EP (1) | EP2922930A1 (en) |
JP (1) | JP6487330B2 (en) |
KR (1) | KR102108598B1 (en) |
CN (1) | CN104797678B (en) |
FR (1) | FR2998302B1 (en) |
WO (1) | WO2014080104A1 (en) |
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FR3010415B1 (en) | 2013-09-11 | 2015-08-21 | Arkema France | HEAT TRANSFER FLUIDS COMPRISING DIFLUOROMETHANE, PENTAFLUOROETHANE, TETRAFLUOROPROPENE AND POSSIBLY PROPANE |
FR3064275B1 (en) | 2017-03-21 | 2019-06-07 | Arkema France | METHOD FOR HEATING AND / OR AIR CONDITIONING A VEHICLE |
FR3064264B1 (en) | 2017-03-21 | 2019-04-05 | Arkema France | COMPOSITION BASED ON TETRAFLUOROPROPENE |
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2012
- 2012-11-20 FR FR1261033A patent/FR2998302B1/en not_active Expired - Fee Related
-
2013
- 2013-10-30 EP EP13801627.4A patent/EP2922930A1/en not_active Withdrawn
- 2013-10-30 JP JP2015542327A patent/JP6487330B2/en not_active Expired - Fee Related
- 2013-10-30 CN CN201380059300.0A patent/CN104797678B/en not_active Expired - Fee Related
- 2013-10-30 KR KR1020157012965A patent/KR102108598B1/en active IP Right Grant
- 2013-10-30 WO PCT/FR2013/052594 patent/WO2014080104A1/en active Application Filing
- 2013-10-30 US US14/442,855 patent/US9752069B2/en not_active Expired - Fee Related
Non-Patent Citations (2)
Title |
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None * |
See also references of WO2014080104A1 * |
Also Published As
Publication number | Publication date |
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US20150291869A1 (en) | 2015-10-15 |
US9752069B2 (en) | 2017-09-05 |
WO2014080104A1 (en) | 2014-05-30 |
JP2016502582A (en) | 2016-01-28 |
KR20150087239A (en) | 2015-07-29 |
CN104797678B (en) | 2019-04-09 |
FR2998302A1 (en) | 2014-05-23 |
JP6487330B2 (en) | 2019-03-20 |
KR102108598B1 (en) | 2020-05-07 |
CN104797678A (en) | 2015-07-22 |
FR2998302B1 (en) | 2015-01-23 |
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