EP1660607A1 - Use of a refrigerant mixture - Google Patents

Use of a refrigerant mixture

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Publication number
EP1660607A1
EP1660607A1 EP04763816A EP04763816A EP1660607A1 EP 1660607 A1 EP1660607 A1 EP 1660607A1 EP 04763816 A EP04763816 A EP 04763816A EP 04763816 A EP04763816 A EP 04763816A EP 1660607 A1 EP1660607 A1 EP 1660607A1
Authority
EP
European Patent Office
Prior art keywords
refrigerant
refrigerant mixture
mixture
air conditioning
mixture according
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Withdrawn
Application number
EP04763816A
Other languages
German (de)
French (fr)
Inventor
Felix Flohr
Christoph Meurer
Martin Schwiegel
Werner Krücke
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Solvay Fluor GmbH
Original Assignee
Solvay Fluor GmbH
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Priority claimed from DE102004032792A external-priority patent/DE102004032792A1/en
Application filed by Solvay Fluor GmbH filed Critical Solvay Fluor GmbH
Publication of EP1660607A1 publication Critical patent/EP1660607A1/en
Withdrawn legal-status Critical Current

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Classifications

    • 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
    • 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
    • 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
    • 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
    • C09K2205/106—Carbon dioxide
    • 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

Definitions

  • the invention relates to a refrigerant mixture, in particular a refrigerant for air conditioning systems in motor vehicles and commercial vehicles, preferably in car air conditioning systems.
  • halogenated hydrocarbons especially chlorofluorocarbons
  • GWP global warming potential
  • partially fluorinated hydrocarbons A large number of substances that have no ozone depletion potential are now available in the field of refrigeration technology.
  • DE 41 16 274 discloses a refrigerant mixture which contains CO2 and partially fluorinated hydrocarbons such as R 134a (CF3-CH2F) or R 152a (CHF2-CH3). These mixtures are to be used in particular as replacements for the refrigerants R 22 (CHCIF2) and R 502 (an azeotropic mixture of (CHCIF2) (R 22) and C2CIF5 (R 115)).
  • WO 00/39242 also describes a cold mixture as a substitute for R 22 (CHCIF2) or R 502 (mixture of CHCIF2 and C2CIF5). This mixture consists of fluoroethane (R 161) and trifluoroiodomethane (R 13 I 1).
  • the object of the invention is to provide a refrigerant mixture which can be used as a substitute for R 134a.
  • the refrigerant mixture should have a minimal global warming potential, be non-toxic and, if possible, non-flammable.
  • the refrigerant mixture according to the invention contains or consists of halogenated hydrocarbons with a GWPioo less than 150 and CO 2
  • Halogenated hydrocarbons with a GWP-J QO less than 150 are especially suitable as 1.1.-difluoroethane (R 152a), fluoroethane (R 161) and trifluoroiodomethane, which in combination with CO2 as a substitute for the refrigerant 1.1.1.2-tetrafluoroethane (R 134a) can be used.
  • Fluoroethane and difluoroethane are flammable as individual substances, but have a GWP-joo below 150 and are very volatile in the atmosphere. How to find a GWP-
  • Trifluoroiodomethane is not flammable, but it is also very unstable in the atmosphere. It was found that the disadvantageous properties of the individual substances can be compensated for by combining the individual substances with CO2 and the refrigerant mixture according to the invention can be used in particular for automotive air conditioning systems. These refrigerant mixtures are much cheaper than 1.1.1.2-tetrafluoromethane in terms of their direct greenhouse potential and can therefore be used as a substitute.
  • the composition of the refrigerant mixture can be varied depending on the pressure in the refrigerant system.
  • composition of the refrigerant mixture is selected so that the risk of flammability is reduced or severely restricted.
  • a mixture of 98-70 wt% R 152a and 2-30 wt% CO2 is used to replace R 134a.
  • R 152a behaves similar to R 134a in its thermophysical properties. However, due to the flammability of R 152a, it can be used in directly evaporating systems, e.g. in automobiles.
  • the explosion range of R 152a is between 4.5% by volume lower explosion limit and 21.8% by volume upper explosion limit. In the case of mixtures with a CO2 content of 30% by weight, the lower explosion limit increases to 13% by volume. (see Fig. 1). Increasing the lower explosion limit reduces the risk that flammable refrigerants generally have.
  • CO2 has very different thermophysical properties than R 134a and R 152a. CO2 is not flammable. CO2 has a significantly higher pressure level than R 134a or R 152a.
  • the critical temperature of 31 ° C means that CO2 for the air conditioning of vehicles cannot be used in the classic subcritical compression refrigeration process, but has to go through a transcritical process.
  • the transcritical process leads to significantly higher process pressures (> 100 bar) and a significant deterioration in the theoretically achievable maximum efficiency.
  • the mixture was found to have a high volumetric refrigeration capacity. This high cooling capacity leads to a reduction in the required stroke volume of the compressor and thus to a reduction in the compressor size (see example 1).
  • Mixtures of R 152a and CO2 with a CO2 content> 2% by weight have a higher pressure level than R 134a. Higher pressure levels improve heat transfer and reduce friction pressure losses. Both effects have a positive effect on the energy efficiency of the overall system. Mixtures of R 152a and CO2 have a large temperature glide. This has a positive effect if cooling and heating are required at sliding temperatures. The sliding heat transfer is present in all heat transfers in which there is no phase change on the secondary side and thus also in the air cooling or air heating.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Combustion & Propulsion (AREA)
  • Thermal Sciences (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Air-Conditioning For Vehicles (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Lubricants (AREA)

Abstract

The invention relates to a refrigerant mixture that is suitable as a substitute for the refrigerant 1.1.1.2-tetrafluorethane (R 134a), whereby said mixture comprises or is constituted of halogenated hydrocarbons having a GWP100 of not more than 150 and CO2. The refrigerant mixture is preferably suitable as refrigerant in air-conditioning systems especially for automotive air-conditioning systems.

Description

Verwendung eines Kältemittelgemisches Beschreibung Use of a refrigerant mixture description
Die Erfindung betrifft ein Kaltemittelgemisch, insbesondere ein Kältemittel für Klimaanlagen in Kraft- und Nutzfahrzeugen, vorzugsweise in Autoklimaanlagen.The invention relates to a refrigerant mixture, in particular a refrigerant for air conditioning systems in motor vehicles and commercial vehicles, preferably in car air conditioning systems.
Es ist bekannt, halogenierte Kohlenwasserstoffe oder deren Gemische als Kältemittel einzusetzen.It is known to use halogenated hydrocarbons or their mixtures as refrigerants.
Seit einiger Zeit sind insbesondere für Fahrzeugklimaanlagen so genannte natürliche Kältemittel in der Diskussion. Kohlendioxid ist ein möglicher Ersatzstoff, dessen direktes Treibhauspotential gegenüber dem bisher eingesetzten ozonfreundlichen 1.1.1.2- Tetrafluorethan (R 134a) vernachlässigbar klein ist. Kohlendioxid wurde bis ca. 1950 wegen seiner Unbrennbarkeit als Arbeitsstoff für Kältemaschinen verwendet. Wegen des ungünstigen Tripelpunktes und der ungünstigen Drucklage ist es jedoch mit Aufkommen der FCKW als Kältemittel bedeutungslos geworden.For some time now, so-called natural refrigerants have been under discussion, particularly for vehicle air conditioning systems. Carbon dioxide is a possible substitute whose direct greenhouse potential is negligibly small compared to the previously used ozone-friendly 1.1.1.2-tetrafluoroethane (R 134a). Carbon dioxide was used as a working material for chillers until around 1950 because of its non-flammability. However, due to the unfavorable triple point and the unfavorable pressure situation, CFCs have become meaningless as refrigerants.
Es ist bekannt, CO2 als Kältemittel allein oder im Gemisch mit halogenierten Kohlenwasserstoffen einzusetzen.It is known to use CO2 as a refrigerant alone or in a mixture with halogenated hydrocarbons.
Es ist weiterhin bekannt, dass von den halogenierten Kohlenwasserstoffen, insbesondere die Fluorchlorkohlenwasserstoffe ein sehr hohes Treibhauspotential (GWP) besitzen, dagegen ist der GWP-Wert für teilfluorierte Kohlenwasserstoffe deutlich niedriger. Im Bereich der Kältetechnik ist inzwischen eine Vielzahl von Substanzen verfügbar, die kein Ozon-Abbaupotential besitzen.It is also known that halogenated hydrocarbons, especially chlorofluorocarbons, have a very high global warming potential (GWP), whereas the GWP value for partially fluorinated hydrocarbons is significantly lower. A large number of substances that have no ozone depletion potential are now available in the field of refrigeration technology.
DE 41 16 274 offenbart ein Kaltemittelgemisch, welches CO2 und teilfluorierte Kohlenwasserstoffe wie z.B.- R 134a (CF3-CH2F) oder R 152a (CHF2-CH3) enthält. Diese Gemische sollen insbesondere als Ersatz für die Kältemittel R 22 (CHCIF2) und R 502 (ein azeotropes Gemisch aus (CHCIF2) (R 22) und C2CIF5 (R 115)) Verwendung finden. WO 00/39242 beschreibt ebenfalls eine Kältemischung als Substitut für R 22 (CHCIF2) oder R 502 (Mischung aus CHCIF2 und C2CIF5). Diese Mischung besteht aus Fluor- ethan (R 161) und Trifluorjodmethan (R 13 I 1).DE 41 16 274 discloses a refrigerant mixture which contains CO2 and partially fluorinated hydrocarbons such as R 134a (CF3-CH2F) or R 152a (CHF2-CH3). These mixtures are to be used in particular as replacements for the refrigerants R 22 (CHCIF2) and R 502 (an azeotropic mixture of (CHCIF2) (R 22) and C2CIF5 (R 115)). WO 00/39242 also describes a cold mixture as a substitute for R 22 (CHCIF2) or R 502 (mixture of CHCIF2 and C2CIF5). This mixture consists of fluoroethane (R 161) and trifluoroiodomethane (R 13 I 1).
Die Aufgabe der Erfindung besteht darin, ein Kaltemittelgemisch bereitzustellen, welches als Ersatz für R 134a Verwendung finden kann. Das Kaltemittelgemisch soll ein minimales Treibhauspotential aufweisen, nicht giftig und möglichst nicht brennbar sein.The object of the invention is to provide a refrigerant mixture which can be used as a substitute for R 134a. The refrigerant mixture should have a minimal global warming potential, be non-toxic and, if possible, non-flammable.
Die erfindungsgemäße Kältemittelmischung enthält oder besteht aus halogenierten Kohlenwasserstoffen mit einem GWPioo kleiner 150 und Cθ2-The refrigerant mixture according to the invention contains or consists of halogenated hydrocarbons with a GWPioo less than 150 and CO 2
Als halogenierte Kohlenwasserstoff mit einem GWP-J QO kleiner150 sind insbesondere 1.1.- Difluorethan (R 152a), Fluorethan (R 161) und Trifluorjodmethan als geeignete Verbindungen anzusehen, die in Kombination mit CO2 als Ersatzstoff für das Kältemittel 1.1.1.2-Tetrafluorethan (R 134a) Verwendung finden können.Halogenated hydrocarbons with a GWP-J QO less than 150 are especially suitable as 1.1.-difluoroethane (R 152a), fluoroethane (R 161) and trifluoroiodomethane, which in combination with CO2 as a substitute for the refrigerant 1.1.1.2-tetrafluoroethane (R 134a) can be used.
Fluorethan und Difluorethan sind als Einzelsubstanzen brennbar, haben jedoch einen GWP-joo unter 150 und sind in der Atmosphäre sehr unbeständig. So findet man für Fluorethan einen GWP-| QO von 12 und für Difluorethan einen GWPηQO von 0.Fluoroethane and difluoroethane are flammable as individual substances, but have a GWP-joo below 150 and are very volatile in the atmosphere. How to find a GWP- | for fluoroethane QO of 12 and for difluoroethane a GWPηQO of 0.
Trifluorjodmethan ist nicht brennbar, dafür aber in der Atmosphäre ebenfalls sehr unbeständig. Es wurde gefunden, dass durch Kombination der Einzelsubstanzen mit CO2 die nachteiligen Eigenschaften der Einzelsubstanzen kompensiert werden können und die erfindungsgemäße Kältemittelmischung insbesondere für Autoklimaanlagen Verwendung finden kann. Diese Kältemittelgemische sind hinsichtlich ihres direkten Treibhauspotentials wesentlich günstiger als 1.1.1.2-Tetrafluormethan und können deshalb als Ersatzstoff eingesetzt werden. Die Zusammensetzung der Kältemittelmischung kann in Abhängigkeit vom Druck im Kältemittelsystem variiert werden.Trifluoroiodomethane is not flammable, but it is also very unstable in the atmosphere. It was found that the disadvantageous properties of the individual substances can be compensated for by combining the individual substances with CO2 and the refrigerant mixture according to the invention can be used in particular for automotive air conditioning systems. These refrigerant mixtures are much cheaper than 1.1.1.2-tetrafluoromethane in terms of their direct greenhouse potential and can therefore be used as a substitute. The composition of the refrigerant mixture can be varied depending on the pressure in the refrigerant system.
Es ist ebenfalls im Sinne der Erfindung, dass die Zusammensetzung der Kältemittelmischung so gewählt wird, dass das Risiko der Brennbarkeit vermindert bzw. stark eingeschränkt wird. In einer Ausführungsform wird ein Gemisch aus 98 - 70 Gew.-% R 152a und 2 - 30 Gew.-% CO2 als Ersatz für R 134a verwendet.It is also within the scope of the invention that the composition of the refrigerant mixture is selected so that the risk of flammability is reduced or severely restricted. In one embodiment, a mixture of 98-70 wt% R 152a and 2-30 wt% CO2 is used to replace R 134a.
Als Reinstoffe weisen beide Einzelkomponenten des erfindungsgemäßen Gemisches für eine Verwendung als Kältemittel Nachteile auf.As pure substances, both individual components of the mixture according to the invention have disadvantages for use as refrigerants.
R 152a verhält sich von seinen thermophysikalischen Eigenschaften ähnlich wie R 134a. Aufgrund der Brennbarkeit von R 152a wird jedoch die Einsatzfähigkeit in direkt verdampfenden Systemen, wie z.B. in Automobilen, eingeschränkt. Der Explosionsbereich von R 152a liegt zwischen 4,5 Vol. % unterer Explosionsgrenze und 21 ,8 Vol. % oberer Explosionsgrenze. Bei Mischungen mit einem CO2 Anteil von 30 Gew.-% erhöht sich die untere Explosionsgrenze auf 13 Vol. %. (siehe Fig. 1). Die Erhöhung der unteren Explosionsgrenze reduziert das Risiko, welches generell bei brennbaren Kältemitteln besteht.R 152a behaves similar to R 134a in its thermophysical properties. However, due to the flammability of R 152a, it can be used in directly evaporating systems, e.g. in automobiles. The explosion range of R 152a is between 4.5% by volume lower explosion limit and 21.8% by volume upper explosion limit. In the case of mixtures with a CO2 content of 30% by weight, the lower explosion limit increases to 13% by volume. (see Fig. 1). Increasing the lower explosion limit reduces the risk that flammable refrigerants generally have.
CO2 ist in seinen thermophysikalischen Eigenschaften gegenüber denen von R 134a und R 152a sehr verschieden. CO2 ist nicht brennbar. CO2 besitzt eine wesentlich höhere Drucklage als R 134a oder R 152a.CO2 has very different thermophysical properties than R 134a and R 152a. CO2 is not flammable. CO2 has a significantly higher pressure level than R 134a or R 152a.
Die kritische Temperatur von 31 °C hat zur Folge, dass CO2 für die Klimatisierung von Fahrzeugen nicht im klassischen unterkritischen Kompressionskälteprozess einsetzbar ist, sondern einen transkritischen Prozess durchlaufen muss. Der transkritische Pro- zess führt zu wesentlich höheren Prozessdrücken (>100 bar) und zu einer deutlichen Verschlechterung des theoretisch erreichbaren maximalen Wirkungsgrades.The critical temperature of 31 ° C means that CO2 for the air conditioning of vehicles cannot be used in the classic subcritical compression refrigeration process, but has to go through a transcritical process. The transcritical process leads to significantly higher process pressures (> 100 bar) and a significant deterioration in the theoretically achievable maximum efficiency.
CO2 hat, obwohl es vom menschlichen Körper produziert wird, ab Konzentrationen von 4 Vol. % eine toxische Wirkung, die bei längerem Einatmen zu Bewusstlosigkeit führen und über 8 Vol. % zum Tode führen kann. In Mischung mit R 152a wird dieser Toxizi- tätseffekt aufgehoben. R 134a besitzt mit einem GWPΠ QO von 1300 einen relativ hohen Beitrag zum Treibhauseffekt, wenn es in die Atmosphäre gelangt. Mit einem GWPioo von 140 für R 152a und einem GWP-I QQ von 1 für CO2 haben die erfindungsgemäß verwendeten Komponenten einen wesentlich niedrigeren GWP-J OO a's R 134a. Aufgrund der unterschiedlichen spezifischen Dichten von R 152a und CO2 gegenüber R 134a kann die für Autoklimaanlagen benötigte Füllmenge, wesentlich verringert werden, (siehe Tabelle 1)CO2, although it is produced by the human body, has a toxic effect from concentrations of 4% by volume, which can lead to unconsciousness if inhaled for longer and over 8% by volume can lead to death. When mixed with R 152a, this toxicity effect is eliminated. With a GWP Π QO of 1300, R 134a makes a relatively high contribution to the greenhouse effect if it gets into the atmosphere. With a GWPioo of 140 for R 152a and a GWP I QQ of 1 for CO2, the components used in the invention a significantly lower GWP J OO a 's R 134a. Due to the different specific densities of R 152a and CO2 compared to R 134a, the filling quantity required for car air conditioning systems can be significantly reduced (see Table 1)
Tabelle 1 : FüllmengenvergleichTable 1: Filling quantity comparison
Es wurde gefunden, dass das Gemisch eine hohe volumetrische Kälteleistung hat. Diese hohe Kälteleistung führt zu einer Verringerung des benötigten Hubvolumens des Verdichters und somit zu einer Verringerung der Verdichterbaugröße (siehe Beispiel 1).The mixture was found to have a high volumetric refrigeration capacity. This high cooling capacity leads to a reduction in the required stroke volume of the compressor and thus to a reduction in the compressor size (see example 1).
Bei Verwendung von Kompressoren, die für den Einsatz von R 134a vorgesehen sind, werden höhere Abkühlgeschwindigkeiten erreicht. Dies ist bei der Automobilklimatisierung von entscheidender Bedeutung, nicht zuletzt aus sicherheitstechnischen Gründen.When using compressors designed for the use of R 134a, higher cooling rates are achieved. This is of crucial importance in automotive air conditioning, not least for safety reasons.
Gemische aus R 152a und CO2 mit einem CO2 Anteil >2 Gew.-% weisen eine höhere Drucklage als R 134a auf. Höhere Drucklagen verbessern den Wärmeübergang und reduzieren Reibungsdruckverluste. Beide Effekte wirken sich positiv auf die Energieeffizienz des Gesamtsystems aus. Gemische aus R 152a und CO2 haben einen großen Temperaturgleit. Dies wirkt sich positiv aus, wenn Kühlen und Heizen bei gleitenden Temperaturen nötig ist. Der gleitende Wärmeübergang ist bei allen Wärmeübergängen vorhanden, bei denen kein Phasenwechsel auf Sekundärseite stattfindet und somit auch bei der Luftabkühlung bzw. Lufterwärmung vorhanden.Mixtures of R 152a and CO2 with a CO2 content> 2% by weight have a higher pressure level than R 134a. Higher pressure levels improve heat transfer and reduce friction pressure losses. Both effects have a positive effect on the energy efficiency of the overall system. Mixtures of R 152a and CO2 have a large temperature glide. This has a positive effect if cooling and heating are required at sliding temperatures. The sliding heat transfer is present in all heat transfers in which there is no phase change on the secondary side and thus also in the air cooling or air heating.
Beispiel: 1Example 1
In einer simulierten Autoklimaanlage wurde die Kältemittel bzw. Kältemittelmischungen unter den genannten Bedingungen miteinander verglichen.In a simulated car air conditioning system, the refrigerants or refrigerant mixtures were compared with one another under the conditions mentioned.
Kreislaufbedingunqen:Kreislaufbedingunqen:
Einfacher Kreislauf mit innerem WärmetauscherSimple circuit with an internal heat exchanger
Tu = 30 °CTu = 30 ° C
To = 0 °CTo = 0 ° C
Tc = 45 °CTc = 45 ° C
T überhitzt = 5KT overheated = 5K
T unterkühlt 2K isentroper Wirkungsgrad = 1 ;T supercooled 2K isentropic efficiency = 1;
ΔT1WT = 12KΔT 1WT = 12K
Abweichende Bedingungen für die zeotrope Mischungen von R 152a / CO2: Wärmeübergang in den Wärmetauscher findet statt bei einer mittleren Temperatur Tm = T"-(T"-T')/2 Abweichende Bedingung für die Mischung R 152a / 00979,32 / 20.68 Gew.-%:Different conditions for the zeotropic mixtures of R 152a / CO2: heat transfer into the heat exchanger takes place at an average temperature Tm = T "- (T" -T ') / 2 Different conditions for the mixture R 152a / 00979.32 / 20.68 Gew .-%:
Die Austrittstemperatur es Kältemittels wurde auf 35 °C, was zu einer mittleren Temperatur von Tm = 48,5 °C führt.The refrigerant outlet temperature was 35 ° C, resulting in an average temperature of T m = 48.5 ° C.
Abweichende Bedingungen für den transkritischen Cθ2-Prozess:Different conditions for the transcritical CO 2 process:
ΔTIWT = 5K ΔT IWT = 5K
Tab. 2: Vergleich der Leistungszahl (COP) und volumetrischer Kälteleistung verschiedener Kältemittel Tab. 2: Comparison of the coefficient of performance (COP) and volumetric cooling capacity of different refrigerants

Claims

Patentansprüche claims
1. Kältemittelmischung, verwendbar als Ersatz für das Kältemittel R 134a, enthaltend oder bestehend aus halogenierten Kohlenwasserstoffen mit einem GWP-J OO kleiner 150 und CO2.1. Refrigerant mixture, usable as a replacement for the refrigerant R 134a, containing or consisting of halogenated hydrocarbons with a GWP-J OO less than 150 and CO 2 .
2. Kältemittelmischung nach Anspruch 1, dadurch gekennzeichnet, dass als halo- genierter Kohlenwasserstoff insbesondere 1.1 -Difluorethan, Fluorethan und/oder Trifluorjodmethan enthalten sind.2. Refrigerant mixture according to claim 1, characterized in that in particular 1.1-difluoroethane, fluoroethane and / or trifluoroiodomethane are contained as the halogenated hydrocarbon.
3. Kältemittelmischung nach Anspruch 1 und 2, bestehend aus 98 - 70 Gew.-% 1.1- Difluorethan und 2 - 30 Gew.-% CO2.3. Refrigerant mixture according to claim 1 and 2, consisting of 98 - 70 wt .-% 1.1-difluoroethane and 2 - 30 wt .-% CO 2 .
4. Kältemittelmischung nach Anspruch 1 und 2 dadurch gekennzeichnet, dass die Kältemittelmischung Fluorethan und CO2 enthält oder daraus besteht.4. Refrigerant mixture according to claim 1 and 2, characterized in that the refrigerant mixture contains or consists of fluoroethane and CO 2 .
5. Verwendung einer Kältemittelmischung enthaltend oder bestehend aus halogenierten Kohlenwasserstoffen mit einem GWPioo kleiner 150 und C02 als Ersatz für das Kältemittel 1.1.1.2-Tetrafluorethan (R 134a) in Klimaanlagen für Kraft- und Nutzfahrzeuge, insbesondere für Autoklimaanlagen.5. Use of a refrigerant mixture containing or consisting of halogenated hydrocarbons with a GWPioo less than 150 and C0 2 as a replacement for the refrigerant 1.1.1.2-tetrafluoroethane (R 134a) in air conditioning systems for motor vehicles and commercial vehicles, in particular for car air conditioning systems.
6. Verwendung eines Kältemittelgemisches nach Anspruch 5 bestehend aus 98 -70 Gew.-% R 152a und 2 - 30 Gew.-% CO2 als Ersatz für das Kältemittel R 134a.6. Use of a refrigerant mixture according to claim 5 consisting of 98-70 wt .-% R 152a and 2-30 wt .-% CO 2 as a replacement for the refrigerant R 134a.
7. Verwendung eines Kältemittelgemisches nach Anspruch 5, dadurch gekennzeichnet, dass es Fluorethan und C02 enthält oder daraus besteht. 7. Use of a refrigerant mixture according to claim 5, characterized in that it contains or consists of fluoroethane and C0 2 .
EP04763816A 2003-08-27 2004-08-05 Use of a refrigerant mixture Withdrawn EP1660607A1 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
DE10339444 2003-08-27
DE102004032792A DE102004032792A1 (en) 2003-08-27 2004-07-07 Use of a refrigerant mixture
PCT/EP2004/008772 WO2005021675A1 (en) 2003-08-27 2004-08-05 Use of a refrigerant mixture

Publications (1)

Publication Number Publication Date
EP1660607A1 true EP1660607A1 (en) 2006-05-31

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EP04763816A Withdrawn EP1660607A1 (en) 2003-08-27 2004-08-05 Use of a refrigerant mixture

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US (1) US20060202154A1 (en)
EP (1) EP1660607A1 (en)
JP (1) JP2007503486A (en)
KR (1) KR20060071405A (en)
BR (1) BRPI0413895A (en)
WO (1) WO2005021675A1 (en)

Families Citing this family (4)

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Publication number Priority date Publication date Assignee Title
US7413674B2 (en) * 2004-04-16 2008-08-19 Honeywell International Inc. Azeotrope-like trifluoroiodomethane compositions
FR2910016B1 (en) * 2006-12-19 2009-02-20 Arkema France COMPOSITIONS USEFUL AS REFRIGERANT FLUID
CA2682076C (en) 2007-03-27 2015-05-26 Dow Global Technologies Inc. Quality polymer foam from fluorinated alkene blowing agents
JP2011097497A (en) * 2009-11-02 2011-05-12 Sony Corp Data transfer device

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE4116274C2 (en) * 1991-05-17 1998-03-19 Forschungszentrum Fuer Kaeltet Refrigerant
EP0649453B1 (en) * 1992-07-10 1997-05-14 E.I. Du Pont De Nemours And Company Azeotropic compositions of perfluoroethane and trifluoromethane
EP0766713B2 (en) * 1994-11-02 2003-10-22 Solvay Fluor und Derivate GmbH Foaming agents containing liquid carbon dioxide
GB9618207D0 (en) * 1996-08-30 1996-10-09 Ici Plc Refrigerant compositions
ES2248648T5 (en) * 1998-05-22 2016-09-16 Solvay Fluor Gmbh Composition of expanding agent for the production of foamed thermoplastic synthetic materials
JP4153590B2 (en) * 1998-06-26 2008-09-24 株式会社三愛 Working fluid
GB9828737D0 (en) * 1998-12-29 1999-02-17 Star Refrigeration Vaporisable composition

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* Cited by examiner, † Cited by third party
Title
See references of WO2005021675A1 *

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WO2005021675A1 (en) 2005-03-10
BRPI0413895A (en) 2006-10-24
JP2007503486A (en) 2007-02-22
US20060202154A1 (en) 2006-09-14
KR20060071405A (en) 2006-06-26

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