METHOD FOR CIRCULATING SELECTED HEAT TRANSFER FLUIDS THROUGH A CLOSED LOOP CYCLE

The present invention relates to the use of flexible hoses capable of handling high pressure fluids and providing a barrier against permeation loss in air conditioning and refrigeration systems. Such hoses are particularly suitable in air conditioning and refrigeration in which new, low global warming potential refrigerant alternatives are used.

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Description
BACKGROUND OF THE INVENTION

1. Field of the Invention

The present invention relates to the use of flexible hoses capable of handling high pressure fluids and providing a barrier against permeation loss in air conditioning and refrigeration systems. More particularly, the present invention relates to the use of such hoses in air conditioning and refrigeration systems, including mobile air conditioning systems, in which new, low global warming potential (GWP) refrigerant alternatives are used.

2. Description of Related Art

The refrigeration industry has been working for the past few decades to find replacement refrigerants for the ozone depleting chlorofluorocarbons (CFCs) and hydrochlorofluorocarbons (HCFCs) being phased out as a result of the Montreal Protocol. The solution for most refrigerant producers has been the commercialization of hydrofluorocarbon (HFC) refrigerants. The new HFC refrigerants, HFC-134a being the most widely used at this time, have zero ozone depletion potential and thus are not affected by the current regulatory phase out as a result of the Montreal Protocol.

Further environmental regulations may ultimately cause global phase out of certain HFC refrigerants. Currently, the automobile industry is facing regulations relating to global warming potential (GWP) for refrigerants used in mobile air-conditioning. Therefore, there is a great current need to identify new refrigerants with reduced global warming potential for the automobile air-conditioning market. Should the regulations be more broadly applied in the future, an even greater need will be felt for refrigerants that can be used in all areas of the refrigeration and air-conditioning industry.

Currently proposed replacement refrigerants for HFC-134a include HFC-152a, pure hydrocarbons such as butane or propane, or “natural” refrigerants such as CO2 or ammonia. Many of these suggested replacements are toxic, flammable, and/or have low energy efficiency. Therefore, new alternatives are constantly being sought.

As is widely understood by those having skill in the field, in a typical refrigeration or air conditioning system heat transfer fluids are circulated within a closed loop including a compressor, a condenser and an evaporator. Hoses are typically connected between the outlet of the compressor and the inlet of the condenser; between the outlet of the condenser and the inlet of the evaporator; and between the outlet of the evaporator and the inlet of the compressor. Such hoses must be able to withstand the high pressure of the fluids which are circulated through such systems.

Hoses used for these purposes need to be flexible for ease of installation and use, and often must be shaped into curves and bends for connecting components already installed into fixed positions. They must also be able to contain the fluid pressure. These hoses are often made of elastomeric materials such as natural or synthetic rubber or thermoplastic elastomers, and are typically reinforced with braiding to impart high pressure capability.

Moreover, it is essential that the hoses of such systems offer superior barrier resistance to permeation of the contained fluid through the wall of the hose construction. In addition, the hose wall must provide high barrier resistance to ingression of external fluids, such as air or moisture, into the contained fluid.

In order to meet barrier requirements, hoses are often provided with a suitable thermoplastic barrier layer on the inside. A typical high pressure barrier hose may thus consist of multiple layers—an inner thermoplastic barrier layer made of a polyamide, a polyester or a suitable thermoplastic material; an over-layer of an elastomeric material to provide flexibility; and a braid layer over the elastomeric layer to provide pressure capability and an outer protective cover layer of an elastomeric material.

Attempts to make flexible high pressure high barrier hoses often involve first making a corrugated metallic tube and coating the tube with an elastomeric polymer. Such constructions, however, require complex manufacturing processes, and are expensive for large scale uses. U.S. Pat. No. 7,055,553 describes a fluid transfer hose incorporating a metal barrier layer. The metal barrier layer is bonded using techniques that require use of aggressive chemicals. Also, expensive fluoropolymer layers are incorporated in the hose construction.

Moreover, while such hoses provide pressure capability and flexibility, their barrier properties can be improved. With the drive for reduced emissions, this becomes an issue in highly demanding applications such as refrigeration and air conditioning. As low GWP refrigerants are developed it is important to identify barrier hoses which are suitable for these refrigerants.

It would be desirable to provide a flexible hose for air conditioning or refrigeration systems which is suitable for use with new, high-pressure, low GWP refrigerants. Ideally, such a hose would not require the use of aggressive chemicals, would be economical to make, and would meet stringent barrier requirements.

BRIEF SUMMARY OF THE INVENTION

The present invention relates to transporting a heat transfer fluid within a refrigeration or air conditioning system through a hose, where the hose is able to withstand high-pressure refrigerants, and the hose has improved barrier properties. A further advantage of such hose is its simple and straightforward construction. In a particular embodiment, such hose is especially suitable for use with fluoroolefin compositions which are low GWP refrigerant alternatives. These and other objects, features and advantages of the present invention will become better understood upon having reference to the description of the invention herein.

Therefore, in accordance with the present invention, there is provided a method of providing transport of a heat transfer fluid composition within a refrigeration or air conditioning system, comprising circulating the heat transfer fluid through one or more hoses of said system, wherein said heat transfer fluid comprises a compound selected from the group consisting of: R32, R152a, CF3I, 1234yf, 1225ye and trans-1234ze.

In a particular embodiment, the composition comprises 1225ye and at least one additional compound selected from the group consisting of HFC-1234ze, HFC-1234yf, HFC-1234ye, HFC-1243zf, HFC-32, HFC-125, HFC-134, HFC-134a, HFC-143a, HFC-152a, HFC-161, HFC-227ea, HFC-236ea, HFC-236fa, HFC-245fa, HFC-365mfc, propane, n-butane, isobutane, 2-methylbutane, n-pentane, cyclopentane, dimethylether, CF3SCF3, CO2, NH3, and CF3I.

In another particular embodiment, the composition comprises HFC-1234ze and at least one additional compound selected from the group consisting of HFC-1234yf, HFC-1234ye, HFC-1243zf, HFC-32, HFC-125, HFC-134, HFC-134a, HFC-143a, HFC-152a, HFC-161, HFC-227ea, HFC-236ea, HFC-236fa, HFC-245fa, HFC-365mfc, propane, n-butane, isobutane, 2-methylbutane, n-pentane, cyclopentane, dimethylether, CF3SCF3, CO2 and CF3I.

In another particular embodiment, the composition comprises HFC-1234yf and at least one additional compound selected from the group consisting of HFC-1234ye, HFC-1243zf, HFC-32, HFC-125, HFC-134, HFC-134a, HFC-143a, HFC-152a, HFC-161, HFC-227ea, HFC-236ea, HFC-236fa, HFC-245fa, HFC-365mfc, propane, n-butane, isobutane, 2-methylbutane, n-pentane, cyclopentane, dimethylether, CF3SCF3, CO2, NH3, and CF3I.

In another particular embodiment, the composition comprises HFC-1243zf and at least one additional compound selected from the group consisting of HFC-1234ye, HFC-32, HFC-125, HFC-134, HFC-134a, HFC-143a, HFC-152a, HFC-161, HFC-227ea, HFC-236ea, HFC-236fa, HFC-245fa, HFC-365mfc, propane, n-butane, isobutane, 2-methylbutane, n-pentane, cyclopentane, dimethylether, CF3SCF3, CO2 and CF3I.

In another particular embodiment, the composition comprises HFC-1234ye and at least one additional compound selected from the group consisting of HFC-1243zf, HFC-32, HFC-125, HFC-134, HFC-134a, HFC-143a, HFC-152a, HFC-161, HFC-227ea, HFC-236ea, HFC-236fa, HFC-245fa, HFC-365mfc, propane, n-butane, isobutane, 2-methylbutane, n-pentane, cyclopentane, dimethylether, CF3SCF3, CO2 and CF3I.

In one particular embodiment of a hose configuration, the hose comprises an outer layer comprising a material selected from the group consisting of an elastomer and a polyamide and an inner layer comprising a material selected from the group consisting of an elastomer, a polyamide and a thermoplastic. The hose may further include (a) a tie layer positioned over said inner layer; (b) a metal-polymer laminate positioned over said tie layer and consisting of a layer of polymer compatible with or bondable to said outer surface of said veneer, a thin layer of metallic foil, and another layer of a polymer protecting the metallic foil; (c) a braid under-layer positioned over said metal-polymer laminate and consisting of an elastomeric material; and (d) a reinforcing braid layer positioned over said braid under-layer, wherein the outer layer is positioned on the outside of the reinforcing braid layer.

BRIEF DESCRIPTION OF THE DRAWINGS

The present invention may be better understood with reference to the following figure, wherein:

FIG. 1 is a schematic diagram of a refrigeration or air conditioning system including a plurality of hoses according to the present invention.

FIG. 2 is a cross-sectional view of a hose of the present invention.

 DETAILED DESCRIPTION OF THE INVENTION

According to the present invention, there is provided a refrigeration or air-conditioning system. Such a system, which is a vapor compression system, is shown in FIG. 1. A vapor-compression system is a closed loop system which re-uses refrigerant in multiple steps producing a cooling effect in one step and a heating effect in a different step. Such a system generally includes an evaporator, a compressor, a condenser and an expansion device, as will be described below in detail with respect to FIG. 1. With reference to FIG. 1, gaseous refrigerant from an evaporator (42) flows through a hose (63) to the inlet of a compressor (12), and is then discharged. Various types of compressors may be used with the present invention, including reciprocating, rotary, jet, centrifugal, scroll, screw or axial-flow, depending on the mechanical means to compress the fluid, or as positive-displacement (e.g., reciprocating, scroll or screw) or dynamic (e.g., centrifugal or jet).

The compressed refrigerant gas from the compressor flows through the compressor outlet and through a hose (61) to a condenser (41). A pressure regulating valve (51) in hose (61) may be used. This valve allows recycle of the refrigerant flow back to the compressor via a hose (63), thereby providing the ability to control the pressure of the refrigerant reaching the condenser (41) and if necessary to prevent compressor surge. The compressed refrigerant is condensed in the condenser, thus giving off heat. The liquid refrigerant flows through an expansion device (52) via a hose (62) to the evaporator (42), which is located in the passenger compartment. In the evaporator, the liquid refrigerant is vaporized, providing cooling and the cycle then repeats. The expansion device (52) may be an expansion valve, a capillary tube or an orifice tube.

The closed loop, vapor compression system of the present invention may be used in either stationary or mobile refrigeration or air-conditioning applications. Stationary refrigeration apparatus or stationary air-conditioning apparatus refer to the equipment used for cooling the air in a building, or cooling perishable goods such as foods, pharmaceutical materials, etc, in a conventional, non-mobile, non-vehicle mounted system. These systems may include chillers, ducted and ductless air conditioners and heat pumps, domestic refrigerators and freezers, commercial refrigerators and freezers, supermarket and industrial refrigeration systems.

Such stationary refrigeration or air conditioning systems may be associated with CHP (Combined Heat and Power) systems, wherein a stationary internal combustion engine is used to drive an electrical generator. The waste heat produced by the engine may be recovered and used to perform work, by such means as a Rankine Cycle (steam engine) or Organic Rankine cycle (ORC). In a Rankine cycle, the heat is used to vaporize a liquid (an organic liquid in the case of an ORC), which in turn drives a turbine. The mechanical energy of the turbine may be used to drive an electricity generator, which runs a refrigeration or air-conditioning system.

Mobile refrigeration apparatus or mobile air-conditioning apparatus refers to any refrigeration or air-conditioning apparatus incorporated into a mobile transportation unit for the road, rail, sea or air. In addition, apparatus, which are meant to provide refrigeration or air-conditioning for a system independent of any moving carrier, known as “intermodal” systems, are included in the present invention. Such intermodal systems include “containers” (combined sea/land transport) as well as “swap bodies” (combined road and rail transport). The present invention is particularly useful for road transport refrigerating or air-conditioning apparatus, such as automobile air-conditioning apparatus or refrigerated road transport equipment.

A body to be cooled may be any space, location or object requiring refrigeration or air-conditioning. In stationary applications the body may be the interior of a structure, i.e. residential or commercial, or a storage location for perishables, such as food or pharmaceuticals. Numerous mobile systems are described earlier in defining mobile refrigeration apparatus and mobile air-conditioning apparatus.

The refrigeration apparatus or air-conditioning apparatus of the present invention may additionally employ fin and tube heat exchangers, microchannel heat exchangers and vertical or horizontal single pass tube or plate type heat exchangers in the evaporator and/or the condenser.

In accordance with the present invention, there is provided a method of providing transport of a heat transfer fluid within a refrigeration or air conditioning system, comprising circulating a heat transfer fluid composition through one or more hoses of said system. In one embodiment of the present invention, the hose may comprise an outer layer comprising a material selected from the group consisting of an elastomer and a polyamide. The hose may further comprise an inner layer comprising a material selected from the group consisting of an elastomer, a polyamide and a thermoplastic. In particular, the inner layer may comprise a thermoplastic veneer, and the outer layer may comprise an elastomer.

In a particular configuration of the present invention, hoses are constructed in multiple layers such as described below from the innermost to the outermost surface, including:

    • an layer of a thermoplastic veneer;
    • a tie layer;
    • a metal-polymer laminate consisting of a layer of polymer compatible with the tie layer, a thin layer of metallic foil, and another layer of a polymer protecting the metallic foil;
    • a braid under-layer of a thermoplastic or thermosetting elastomer;
    • a braid layer providing reinforcement; and
    • an outer layer of an elastomeric material.

Reference is made to FIG. 2, in which this embodiment is shown. In FIG. 2, there is shown generally at 10 each of the layers of the invention, numbered and described from the innermost layer to the outermost layer. Hence, there is first depicted closest to the core (where the mandrel is inserted and then later withdrawn) an innermost layer of a thermoplastic veneer 12 having an inner surface 14 and an outer surface 16. The veneer may incorporate a tie layer 18 positioned at its outer surface 16. A metal-polymer laminate 20 is positioned over the tie layer and consisting of a layer 22 of polymer compatible with or bondable to the outer surface of the veneer, a thin layer 24 of metallic foil, and another layer 26 of a polymer protecting the metallic foil. Thereafter, a braid under-layer 28 is positioned over the metal-polymer laminate 20 and consisting of an elastomeric material. A reinforcing braid layer 30 is then positioned over the braid under-layer 28. Finally, an outer layer 32 of an elastomeric material positioned over the reinforcing braid layer 30.

The hose of this one embodiment of the present invention is manufactured in multiple steps, sequenced as provided below.

Step 1—First a mandrel or a solid rod or other suitable structure is provided that serves as a support through the subsequent manufacturing steps. Such mandrels are commonly used in the manufacture of hoses made out of thermosetting materials that need to be supported during the extrusion and curing steps. They are made of a variety of thermoplastic or thermosetting materials such as copolyester ethers, copolyamides, polyolefins, TPVs, EPDMs, synthetic rubbers etc. It is desirable to ensure that the mandrel has sufficient flexibility to be spoolable in long lengths.

Step 2—A thermoplastic veneer is extruded over the mandrel. The veneer can be in the form of a monolayer or a two layer tube depending on the type of metal foil and polymer laminate to be used in step 3 as explained below. It should not develop adhesion to the mandrel surface so that mandrel can be extracted at the end of hose fabrication. As appropriate, one of skill in the field can apply suitable release agents to the mandrel to facilitate the nonadhesive properties of the mandrel in relation to the inner layer of the veneer and lubricate its extraction at the end of hose fabrication.

A monolayer veneer or the inner layer of the two-layer veneer can be made of a polyamide, copolyamide, polyphthalamide, polyester or copolyester that provides chemical and thermal resistance to the contained fluid it is in contact with.

When a monolayer veneer is used, the laminate used in step 3 is provided with an adhesive that can bond to the surface of the veneer. Examples of such laminates are those where metallic foil is laminated with a pressure sensitive adhesive (PSA) that can adhere to the surface of the veneer. Such laminates are available commercially with variety of adhesives such as acrylics, rubber, silicones etc.

In a two-layer veneer construction, the outer layer is made of a functionalized polymer to function as a tie layer between the inner thermoplastic veneer and the metal-polymer laminate to be provided over it. It can be made of a functionalized polyolefin or copolyolefin such as those made by grafting or copolymerizing functional monomers with olefins and copolyolefins. Some examples of functional monomers include those with acid, anhydride, acrylate, epoxy functionality.

When a two-layer veneer is used, the laminate used in step 3 does not need to have an adhesive surface. It is rather sufficient to have a polymeric layer at the surface that is compatible or otherwise bondable to the functionalized tie layer of the veneer.

Step 3—A metal foil and polymer laminate consisting of a first polymer layer compatible or bondable to the surface of the veneer, a thin metallic foil and a second polymer layer (which may be identical to or different from the first polymer layer) is then applied over the assembly prepared in step 2.

Adhesion can be further promoted by application of heat and/or pressure as warranted. Heating may not be necessary if the first polymer layer of the laminate is a room temperature pressure sensitive adhesive (PSA) type. When a two-layer veneer is used along with a functionalized polyolefin as the tie layer, application of both heat and pressure are needed. In one embodiment, the assembly of Step 2 is covered by the metal foil laminate and passed through a heated die designed to apply pressure on to the assembly to form the bonding. In another embodiment, the veneer supported by the mandrel is first passed through a heating tunnel so as to raise the surface temperature of the veneer. The metal foil laminate is then applied over the veneer, and the assembly is passed through another heated die designed to apply pressure and affect bonding.

The laminate is applied over the veneer lengthwise so that it circumferentially wraps around it. The two edges of the foil positioned lengthwise along the tube are bonded tightly together and any excess foil is then trimmed to provide a fully covered assembly. This form of wrapping is preferred over the so-called helical wrap formed by winding a tape over the veneer in a helical fashion at an angle to the axis of the hose because it results in only one seam running along the length of the hose. From barrier perspective, a seam can provide potential site for permeation leak. Hence, it is desirable to minimize it's occurrence in the construction. Lengthwise wrap described above is also easier to apply especially on a small diameter tubing such as that encountered in flexible high pressure hoses.

In cases where extremely high barrier is desired, it may be advantageous to provide multiple layers of the laminate in a manner that seams do not overlap thus providing higher level of permeation barrier.

Metallic foil is thin enough to provide flexibility while resist fracture during handling. For example, it can be aluminum foil, in 1-10 micron thickness range to provide very high level of barrier while retaining flexibility. Note that this approach provides a continuous layer of metal over the tube surface unlike vapor deposition techniques which leave gaps in metal coverage resulting in inferior barrier properties.

The second layer of polymer over the metallic foil is selected to protect the surface of the metal foil and provide compatibility with the braid under-layer to be provided over it. It can be a polyamide, polyester or a polyolefin, and is selected so as to be compatible with the type of braid underlayer to be used in the next step.

Step 4—A braid underlayer is extruded over the assembly of Step 3. The underlayer is an elastomeric material such as a natural or synthetic rubber or a thermoplastic elastomer such as thermoplastic olefin (TPO), thermoplastic ester elastomer (TEE) or a thermoplastic vulcanizate (such as ETPV or TPV, common selections in this field). Its purpose is to provide cushioning and protection against forces imposed during braiding.

It is preferable if this braid underlayer bonds to the surface of the laminate applied in step 3. This may be accomplished by several means such as ensuring that the braid underlayer material is compatible with the surface layer of the laminate, extruding a two-layer braid underlayer such that its inner layer acts as a tie layer to bond to the surface of the laminate or sequentially extruding a tie layer over the laminate first and then the braid underlayer.

A functionalized polymer such as that used for forming the tie layer of the two-layer veneer of step 2 may be used for this purpose, the functionalization chosen to be compatible with the two layers to be bonded.

Step 5—A braided reinforcement layer is provided over the assembly of Step 4. Depending on the desired pressure capability, braiding can be made of metallic or polymeric filaments or high performance filaments such as Kevlar® or Nomex®, both commercially available from E.I. du Pont de Nemours and Company of Wilmington, Del. Braid density is determined according to desired pressure capability and filament material selection. Multiple layers of braid and hybrid braids of multiple types of filaments are often used in practice to maximize the degree of reinforcement while optimizing the cost.

Step 6—An outer protective layer is extruded over the braided reinforcement layer. This layer can again be made of an elastomeric material such as TPO, TEE or a thermoplastic vulcanizate (ETPV or TPV).

Step 7—If any of the layers in the hose construction are made of a thermosetting material, then the assembly of Step 6 needs to cure. If all the layers are made of thermoplastic materials, then curing is not necessary. Note that one or more outer protective layers can be added at this time as well.

Step 8—Finally, the mandrel is extracted from the assembly of Step 6 or Step 7 to produce the finished hose. The mandrel can be extracted by applying hydraulic pressure to one end of the hose or by mechanical means.

Hose made this way can be cut to desired length and fittings can be applied as desired. The hose made this way provides flexibility, high pressure capability and very high barrier capability.

It is readily apparent to those having skill in the art to which this invention pertains that in addition to the materials mentioned herein, a variety of other materials are suitable for each layer as is well known and understood. Likewise, representative thicknesses of each layer and techniques for braiding are already well appreciated by those having skill in the field, and are selected according to the intended application.

In accordance with the method of the present invention, the heat transfer fluid composition comprises a compound selected from the group consisting of: R32, R152a, CF3I, 1234yf, 1225ye and trans-1234ze.

In certain embodiments of the invention, hereinafter referred to as the fluorolefin embodiment, the heat transfer fluid composition comprises at least one fluoroolefin. The heat transfer fluid compositions of the present invention may further comprise at least one additional component that may be a second fluoroolefin, hydrofluorocarbon (HFC), hydrocarbon, dimethyl ether, bis(trifluoromethyl)sulfide, CF3I, or CO2.

According to a particular aspect of the fluoroolefin embodiment, the heat transfer fluid composition comprises 1225ye and at least one additional compound selected from the group consisting of HFC-1234ze, HFC-1234yf, HFC-1234ye, HFC-1243zf, HFC-32, HFC-125, HFC-134, HFC-134a, HFC-143a, HFC-152a, HFC-161, HFC-227ea, HFC-236ea, HFC-236fa, HFC-245fa, HFC-365mfc, propane, n-butane, isobutane, 2-methylbutane, n-pentane, cyclopentane, dimethylether, CF3SCF3, CO2, NH3, and CF3I.

According to another particular aspect of the fluoroolefin embodiment, the heat transfer fluid composition comprises HFC-1234ze and at least one additional compound selected from the group consisting of HFC-1234yf, HFC-1234ye, HFC-1243zf, HFC-32, HFC-125, HFC-134, HFC-134a, HFC-143a, HFC-152a, HFC-161, HFC-227ea, HFC-236ea, HFC-236fa, HFC-245fa, HFC-365mfc, propane, n-butane, isobutane, 2-methylbutane, n-pentane, cyclopentane, dimethylether, CF3SCF3, CO2 and CF3I.

In another particular aspect of the fluoroolefin embodiment, the heat transfer fluid composition comprises HFC-1234yf and at least one additional compound selected from the group consisting of HFC-1234ye, HFC-1243zf, HFC-32, HFC-125, HFC-134, HFC-134a, HFC-143a, HFC-152a, HFC-161, HFC-227ea, HFC-236ea, HFC-236fa, HFC-245fa, HFC-365mfc, propane, n-butane, isobutane, 2-methylbutane, n-pentane, cyclopentane, dimethylether, CF3sCF3, CO2, NH3, and CF3I.

According to another particular aspect of the fluoroolefin embodiment, the heat transfer fluid composition comprises HFC-1243zf and at least one additional compound selected from the group consisting of HFC-1234ye, HFC-32, HFC-125, HFC-134, HFC-134a, HFC-143a, HFC-152a, HFC-161, HFC-227ea, HFC-236ea, HFC-236fa, HFC-245fa, HFC-365mfc, propane, n-butane, isobutane, 2-methylbutane, n-pentane, cyclopentane, dimethylether, CF3SCF3, CO2 and CF3I.

In another particular aspect of the fluoroolefin embodiment, the heat transfer fluid composition comprises HFC-1234ye and at least one additional compound selected from the group consisting of HFC-1243zf, HFC-32, HFC-125, HFC-134, HFC-134a, HFC-143a, HFC-152a, HFC-161, HFC-227ea, HFC-236ea, HFC-236fa, HFC-245fa, HFC-365mfc, propane, n-butane, isobutane, 2-methylbutane, n-pentane, cyclopentane, dimethylether, CF3SCF3, CO2 and CF3I.

For these particular embodiments, the fluoroolefin and the other components of the heat transfer fluid compositions of the present invention are listed in Table 1.

TABLE 1 Compound Chemical name Chemical formula HFC-1225ye 1,2,3,3,3-pentafluoropropene CF3CF═CHF HFC-1234ze 1,3,3,3-tetrafluoropropene CF3CH═CHF HFC-1234yf 2,3,3,3-tetrafluoropropene CF3CF═CH2 HFC-1234ye 1,2,3,3-tetrafluoropropene CHF2CF═CHF HFC-1243zf 3,3,3-trifluoropropene CF3CH═CH2 HFC-32 difluoromethane CH2F2 HFC-125 pentafluoroethane CF3CHF2 HFC-134 1,1,2,2-tetrafluoroethane CHF2CHF2 HFC-134a 1,1,1,2-tetrafluoroethane CH2FCF3 HFC-143a 1,1,1-trifluoroethane CH3CF3 HFC-152a 1,1-difluoroethane CHF2CH3 HFC-161 fluoroethane CH3CH2F HFC-227ea 1,1,1,2,3,3,3- CF3CHFCF3 heptafluoropropane HFC-236ea 1,1,1,2,3,3-hexafluoropropane CF3CHFCHF2 HFC-236fa 1,1,1,3,3,3-hexafluoroethane CF3CH2CF3 HFC-245fa 1,1,1,3,3-pentafluoropropane CF3CH2CHF2 HFC-365mfc 1,1,1,3,3-pentafluorobutane CF3CH2CH2CHF2 Propane CH3CH2CH3 n-butane CH3CH2CH2CH3 i-butane isobutane CH3CH(CH3)CH3 2-methylbutane CH3CH(CH3)CH2CH3 n-pentane CH3CH2CH2CH2CH3 cyclopentane cyclo-(CH2)5— DME dimethylether CH3OCH3 CO2 carbon dioxide CO2 CF3SCF3 bis(trifluoromethyl)sulfide CF3SCF3 iodotrifluoromethane CF3I R717 Ammonia NH3

The individual components listed in Table 1 may be prepared by methods known in the art.

The fluoroolefin compounds used in the compositions of the present invention, HFC-1225ye, HFC-1234ze, and HFC-1234ye, may exist as different configurational isomers or stereoisomers. The present invention is intended to include all single configurational isomers, single stereoisomers or any combination or mixture thereof. For instance, 1,3,3,3-tetra-fluoropropene (HFC-1234ze) is meant to represent the cis-isomer, trans-isomer, or any combination or mixture of both isomers in any ratio. Another example is HFC-1225ye, by which is represented the cis-isomer, trans-isomer, or any combination or mixture of both isomers in any ratio. The compositions of the present invention contain primarily the cis or Z isomer of HFC-1225ye.

The heat transfer fluid compositions of the present invention may be generally useful when the fluoroolefin is present at about 1 weight percent to about 99 weight percent, preferably about 20 weight percent to about 99 weight percent, more preferably about 40 weight percent to about 99 weight percent and still more preferably 50 weight percent to about 99 weight percent.

The present invention further provides compositions as listed in Table 2.

TABLE 2 Concentration ranges (wt %) Components Preferred More preferred Most preferred HFC-1225ye/HFC-32 1-99/99-1 30-99/70-1 90-99/10-1; 95/5/97/3 HFC-1225ye/HFC-134a 1-99/99-1 40-99/60-1 90/10 HFC-1225ye/CO2 0.1-99.9/99.9-0.1 70-99.7/30-0.3 99/1 HFC-1225ye/ammonia 0.1-99.9/0.1-99.9 40-99.9/0.1-60 90/10, 85/15, 80/ 20, 95/5 HFC-1225ye/HFC-1234yf 1-99/99-1 51-99/49-1 and 60-90/ 60/40, 51/49 40-10 HFC-1225ye/HFC-152a/HFC-32 1-98/1-98/1-98 50-98/1-40/1-40 85/10/5 81/15/4 82/15/3 HFC-1225ye/HFC-152a/CO2 1-98/1-98/0.1-98 50-98/1-40/0.3-30 84/15/1 84/15.5/0.5 HFC-1225ye/HFC-152a/propane 1-98/1-98/1-98 50-98/1-40/1-20 85/13/2 HFC-1225ye/HFC-152a/i-butane 1-98/1-98/1-98 50-98/1-40/1-20 85/13/2 HFC-1225ye/HFC-152a/DME 1-98/1-98/1-98 50-98/1-40/1-20 85/13/2 HFC-1225ye/HFC-152a/CF3I 1-98/1-98/1-98 20-90/1-50/1-60 HFC-1225ye/HFC-134a/HFC- 1-98/1-98/1-98 40-98/1-50/1-40 76/9/15 152a HFC-1225ye/HFC-134a/HFC-32 1-98/1-98/1-98 1-80/1-80/1-80 88/9/3 HFC-1225ye/HFC-134a/HFC-161 1-98/1-98/1-98 40-98/1-50/1-20 86/10/4 HFC-1225ye/HFC-134a/CO2 1-98/1-98/0.1-98 40-98/1-50/0.3-30 88.5/11/0.5 HFC-1225ye/HFC-134a/propane 1-98/1-98/1-98 40-98/1-50/1-20 87/10/3 HFC-1225ye/HFC-134a/i-butane 1-98/1-98/1-98 40-98/1-50/1-20 87/10/3 HFC-1225ye/HFC-134a/DME 1-98/1-98/1-98 40-98/1-50/1-20 87/10/3 HFC-1225ye/HFC-134/HFC-32 1-98/1-98/1-98 40-98/1-50/1-40 88/9/3 trans-HFC-1234ze/HFC-134a 1-99/99-1 30-99/70-1 90/10 trans-HFC-1234ze/HFC-32 1-99/99-1 40-99/60-1 95/5 trans-HFC-1234ze/HFC-32/CF3I 1-98/1-98/1-98 20-90/0.1-60/1-70 trans-HFC-1234ze/HFC-152a 1-99/99-1 40-99/60-1 80/20 trans-HFC-1234ze/HFC-125 1-99/99-1 30-99/70-1 HFC-1234yf/HFC-134a 1-99/99-1 30-99/70-1 90/10 HFC-1234yf/HFC-32 1-99/99-1 40-99/60-1 95/5 HFC-1234yf/HFC-125 0.1-99/99-0.1 52-99/48-1 HFC-1234yf/HFC-152a 1-99/99-1 40-99/60-1 80/20 HFC-1225ye/HFC-134a/HFC- 1-97/1-97/1-97/ 20-97/1-80/1-50/ 74/8/17/1 152a/HFC-32 0.1-97 0.1-50 HFC-1225ye/HFC-1234yf/HFC- 1-98/1-98/0.1-98 10-90/10-90/0.1-50 70/20/10 and 134a 20/70/10 HFC-1225ye/HFC-1234yf/HFC-32 1-98/1-98/0.1-98 10-90/5-90/0.1-50 25/73/2, 75/23/2, 49/49/2, 85/10/5, 90/5/5 HFC-1225ye/HFC-1234yf/HFC- 1-97/1-97/0.1-97/ 10-80/10-80/1-60/1-60 32/CF3I 1-97 HFC-1225ye/HFC-1234yf/HFC- 1-98/1-98/0.1-98 10-90/10-90/0.1-50 70/25/5 and 152a 25/70/5 HFC-1225ye/HFC-1234yf/HFC- 1-98/1-98/0.1-98 10-90/10-90/0.1-50 25/71/4, 125 75/21/4, 75/24/1 and 25/74/1 HFC-1225ye/HFC-1234yf/CF3I 1-98/1-98/1-98 9-90/9-90/1-60 40/40/20 and 45/45/10 HFC-32/HFC-125/HFC-1225ye 0.1-98/0.1-98/ 5-70/5-70/5-70 30/30/40 and 0.1-98 23/25/52 HFC-32/HFC-125/trans-HFC- 0.1-98/0.1-98/ 5-70/5-70/5-70 30/50/20 and 1234ze 0.1-98 23/25/52 HFC-32/HFC-125/HFC-1234yf 0.1-98/0.1-98/ 5-70/5-70/5-70 40/50/10, 0.1-98 23/25/52, 15/45/40, and 10/60/30 HFC-32/HFC-134a/HFC- 1-97/1-97/1-97/ 1-60/1-60/1-60/1-60 1225ye/CF3I 1-97 HFC-32/HFC-134a/HFC- 1-96/1-96/1-96/ 1-50/1-50/1-50/1-50/ 1225ye/HFC-1234yf/CF3I 1-96/1-96 1-50 HFC-32/HFC-125/HFC- 1-96/1-96/1-96/ 1-50/1-50/1-50/1-50/ 134a/HFC-1225ye/CF3I 1-96/1-96 1-50 HFC-125/HFC-1225ye/n-butane 0.1-98/0.1-98/ 5-70/5-70/1-20 65/32/3 and 0.1-98 85.1/11.5/3.4 HFC-32/NH3/HFC-1225ye 1-98/1-98/1-98 1-60/10-60/10-90 HFC-32/NH3/HFC-1225ye/CF3I 1-97/1-97/1-97/ 1-60/1-60/10-80/1-60 1-97 HFC-32/NH3/HFC-1234yf/CF3I 1-97/1-97/1-97/ 1-60/1-60/10-80/5-80 1-97 HFC-125/trans-HFC-1234ze/n- 0.1-98/0.1-98/ 5-70/5-70/1-20 66/32/2 and butane 0.1-98 86.1/11.5/2.4 HFC-125/HFC-1234yf/n-butane 0.1-98/0.1-98/ 5-70/5-70/1-20 67/32/1 and 0.1-98 87.1/11.5/1.4 HFC-125/HFC-1225ye/isobutane 0.1-98/0.1-98/ 5-70/5-70/1-20 85.1/11.5/3.4 0.1-98 and 65/32/3 HFC-1225ye/HFC-125/ammonia 0.1-98/0.1-98/ 20-98/1-60/0.1-40 0.1-98 HFC-1225ye/HFC-32/HFC- 0.1-97/0.1-97/ 20-97/1-60/1-60/ 125/ammonia 0.1-97/0.1-97 0.1-40 HFC-125/trans-HFC- 0.1-98/0.1-98/ 5-70/5-70/1-20 86.1/11.5/2.4 1234ze/isobutane 0.1-98 and 66/32/2 HFC-125/HFC-1234yf/isobutane 0.1-98/0.1-98/ 5-70/5-70/1-20 and 87.1/11.5/1.4 0.1-98 80-98/1-19/1-10 and 67/32/1 HFC-1234yf/HFC-32/HFC-143a 1-50/1-98/1-98 15-50/20-80/5-60 HFC-1234yf/HFC-32/isobutane 1-40/59-98/1-30 10-40/59-90/1-10 HFC-1234yf/HFC-125/HFC-143a 1-60/1-98/1-98 10-60/20-70/20-70 HFC-1234yf/HFC-125/isobutane 1-40/59-98/1-20 10-40/59-90/1-10 HFC-1234yf/HFC-125/CF3I 1-98/0.1-98/1-98 10-80/1-60/1-60 HFC-1234yf/HFC-134/propane 1-80/1-70/19-90 20-80/10-70/19-50 HFC-1234yf/HFC-134/DME 1-70/1-98/29-98 20-70/10-70/29-50 HFC-1234yf/HFC-134a/propane 1-80/1-80/19-98 10-80/10-80/19-50 HFC-1234yf/HFC-134a/n-butane 1-98/1-98/1-30 10-80/10-80/1-20 HFC-1234yf/HFC-134a/isobutane 1-98/1-98/1-30 10-80/10-80/1-20 HFC-1234yf/HFC-134a/DME 1-98/1-98/1-40 10-80/10-80/1-20 HFC-1234yf/HFC-134a/CF3I 1-98/1-98/1-98 10-80/1-60/1-60 HFC-1234yf/HFC-143a/propane 1-80/1-98/1-98 10-80/10-80/1-50 HFC-1234yf/HFC-143a/DME 1-40/59-98/1-20 5-40/59-90/1-10 HFC-1234yf/HFC-152a/n-butane 1-98/1-98/1-30 10-80/10-80/1-20 HFC-1234yf/HFC-152a/isobutane 1-98/1-90/1-40 10-80/10-80/1-20 HFC-1234yf/HFC-152a/DME 1-70/1-98/1-98 10-70/10-80/1-20 HFC-1234yf/HFC-152a/CF3I 1-98/1-98/1-98 10-80/1-60/1-60 HFC-1234yf/HFC-227ea/propane 1-80/1-70/29-98 10-60/10-60/29-50 HFC-1234yf/HFC-227ea/n-butane 40-98/1-59/1-20 50-98/10-49/1-10 HFC-1234yf/HFC- 30-98/1-69/1-30 50-98/10-49/1-10 227ea/isobutane HFC-1234yf/HFC-227ea/DME 1-98/1-80/1-98 10-80/10-80/1-20 HFC-1234yf/n-butane/DME 1-98/1-40/1-98 10-80/10-40/1-20 HFC-1234yf/isobutane/DME 1-98/1-50/1-98 10-90/1-40/1-20 HFC-1234yf/DME/CF3I 1-98/1-98/1-98 10-80/1-20/10-80 HFC-1234yf/DME/CF3SCF3 1-98/1-40/1-98 10-80/1-20/10-70 HFC-1225ye/trans-HFC- 1-98/1-98/1-98 10-80/10-80/10-80 1234ze/HFC-134 HFC-1225ye/trans-HFC- 1-98/1-98/1-98 10-80/10-80/10-80 1234ze/HFC-227ea HFC-1225ye/trans-HFC- 1-60/1-60/39-98 10-60/10-60/39-80 1234ze/propane HFC-1225ye/trans-HFC- 1-98/1-98/1-30 10-80/10-80/1-20 1234ze/n-butane HFC-1225ye/trans-HFC- 1-98/1-98/1-98 10-80/10-80/1-30 1234ze/DME HFC-1225ye/trans-HFC-1234ze/ 1-98/1-98/1-98 10-80/10-80/10-80 CF3SCF3 HFC-1225ye/HFC-1243zf/HFC- 1-98/1-98/1-98 10-80/10-80/10-80 134 HFC-1225ye/HFC-1243zf/n- 1-98/1-98/1-30 10-80/10-80/1-20 butane HFC-1225ye/HFC- 1-98/1-98/1-40 10-80/10-80/1-30 1243zf/isobutane HFC-1225ye/HFC-1243zf/DME 1-98/1-98/1-98 10-80/10-80/1-30 HFC-1225ye/HFC-1243zf/CF3I 1-98/1-98/1-98 10-80/10-80/10-80 HFC-1225ye/HFC-134/HFC-152a 1-98/1-98/1-98 10-80/10-80/1-50 HFC-1225ye/HFC-134/HFC- 1-98/1-98/1-98 10-80/10-80/10-80 227ea HFC-1225ye/HFC-134/n-butane 1-98/1-90/1-40 10-80/10-80/1-30 HFC-1225ye/HFC-134/isobutane 1-98/1-90/1-40 10-80/10-80/1-30 HFC-1225ye/HFC-134/DME 1-98/1-98/1-40 10-80/10-80/1-30 HFC-1225ye/HFC-227ea/DME 40-98/1-59/1-30 50-98/1-49/1-20 HFC-1225ye/n-butane/DME 1-98/1-30/1-98 60-98/1-20/1-20 HFC-1225ye/n-butane/CF3SCF3 1-98/1-20/1-98 10-80/1-10/10-80 HFC-1225ye/isobutane/DME 1-98/1-60/1-98 40-90/1-30/1-30 HFC-1225ye/isobutane/CF3I 1-98/1-40/1-98 10-80/1-30/10-80 trans-HFC-1234ze/HFC- 1-98/1-98/1-98 10-80/10-80/10-80 1243zf/HFC-227ea trans-HFC-1234ze/HFC-1243zf/n- 1-98/1-98/1-30 10-80/10-80/1-20 butane trans-HFC-1234ze/HFC- 1-98/1-98/1-40 10-80/10-80/1-30 1243zf/isobutane trans-HFC-1234ze/HFC- 1-98/1-98/1-98 10-80/10-80/1-40 1243zf/DME trans-HFC-1234ze/HFC-32/CF3I 1-98/1-98/1-98 10-80/1-70/1-80 trans-HFC-1234ze/HFC- 1-98/1-98/1-98 10-80/10-80/1-50 134/HFC-152a trans-HFC-1234ze/HFC- 1-98/1-98/1-98 10-80/10-80/10-80 134/HFC-227ea trans-HFC-1234ze/HFC-134/DME 1-98/1-98/1-40 10-80/10-80/1-30 trans-HFC-1234ze/HFC- 1-98/1-98/1-98 10-80/10-80/1-50 134a/HFC-152a trans-HFC-1234ze/HFC-152a/n- 1-98/1-98/1-50 10-80/10-80/1-30 butane trans-HFC-1234ze/HFC- 1-98/1-98/1-98 20-90/1-50/1-30 152a/DME trans-HFC-1234ze/HFC-227ea/n- 1-98/1-98/1-40 10-80/10-80/1-30 butane trans-HFC-1234ze/n-butane/DME 1-98/1-40/1-98 10-90/1-30/1-30 trans-HFC-1234ze/n-butane/CF3I 1-98/1-30/1-98 10-80/1-20/10-80 trans-HFC- 1-98/1-60/1-98 10-90/1-30/1-30 1234ze/isobutane/DME trans-HFC-1234ze/isobutane/ 1-98/1-40/1-98 10-80/1-20/10-80 CF3I trans-HFC-1234ze/isobutane/ 1-98/1-40/1-98 10-80/1-20/10-80 CF3SCF3 HFC-1243zf/HFC-134/HFC- 1-98/1-98/1-98 10-80/10-80/10-80 227ea HFC-1243zf/HFC-134/n-butane 1-98/1-98/1-40 10-80/10-80/1-30 HFC-1243zf/HFC-134/DME 1-98/1-98/1-98 10-80/10-80/1-30 HFC-1243zf/HFC-134/CF3I 1-98/1-98/1-98 10-80/10-80/10-80 HFC-1243zf/HFC-134a/HFC- 1-98/1-98/1-98 10-80/10-80/1-50 152a HFC-1243zf/HFC-134a/n-butane 1-98/1-98/1-40 10-80/10-80/1-30 HFC-1243zf/HFC-152a/propane 1-70/1-70/29-98 10-70/1-50/29-40 HFC-1243zf/HFC-152a/n-butane 1-98/1-98/1-30 10-80/1-80/1-20 HFC-1243zf/HFC-152a/isobutane 1-98/1-98/1-40 10-80/1-80/1-30 HFC-1243zf/HFC-152a/DME 1-98/1-98/1-98 10-80/1-80/1-30 HFC-1243zf/HFC-227ea/n-butane 1-98/1-98/1-40 10-80/1-80/1-30 HFC-1243zf/HFC- 1-98/1-90/1-50 10-80/1-80/1-30 227ea/isobutane HFC-1243zf/HFC-227ea/DME 1-98/1-80/1-90 10-80/1-80/1-30 HFC-1243zf/n-butane/DME 1-98/1-40/1-98 10-90/1-30/1-30 HFC-1243zf/isobutane/DME 1-98/1-60/1-98 10-90/1-30/1-30 HFC-1243zf/isobutane/CF3I 1-98/1-40/1-98 10-80/1-30/10-80 HFC-1243zf/DME/CF3SCF3 1-98/1-40/1-90 10-80/1-30/10-80 HFC-1225ye/HFC-32/CF3I 1-98/1-98/1-98 5-80/1-70/1-80 HFC-1225ye/HFC-1234yf/HFC- 1-97/1-97/1-97/ 1-80/1-70/5-70/5-70 32/HFC-125 1-97 HFC-1225ye/HFC-1234yf/HFC- 1-97/1-97/1-97/ 5-80/5-70/5-70/5-70 32/HFC-134a 1-97 HFC-1225ye/HFC-1234yf/HFC- 1-96/1-96/1-96/ 1-70/1-60/1-70/1-60/ 32/HFC-125/CF3I 1-96/1-96 1-60 HFC-1225ye/HFC-32/HFC- 1-97/1-97/1-97/ 10-80/5-70/5-70/5-70 125/HFC-152a 1-97 HFC-1225ye/HFC-32/HFC- 1-97/1-97/1-97/ 5-70/5-70/5-70/1-30 125/isobutane 1-97 HFC-1225ye/HFC-32/HFC- 1-97/1-97/1-97/ 5-70/5-70/5-70/1-30 125/propane 1-50 HFC-1225ye/HFC-32/HFC- 1-97/1-97/1-97/ 5-70/5-70/5-70/1-30 125/DME 1-50 HFC-1225ye/HFC-32/CF3I/DME 1-97/1-97/1-97/ 5-70/5-70/5-70/1-30 1-50 HFC-1225ye/HFC-32/HFC- 1-97/1-97/1-97/ 10-80/5-70/5-70/1-80 125/CF3I 1-97 HFC-1234yf/HFC-32/CF3I 1-98/1-98/1-98 10-80/1-70/1-80 HFC-1234yf/HFC-32/HFC- 1-97/1-97/1-97/ 5-70/5-80/1-70/5-70 134a/CF3I 1-97 HFC-1234yf/HFC-32/HFC-125 1-98/1-98/1-98 10-80/5-80/10-80 HFC-1234yf/HFC-32/HFC- 1-97/1-97/1-97/ 10-80/5-70/10-80/5-80 125/CF3I 1-97

The most preferred compositions of the present invention listed in Table 2 are generally expected to maintain the desired properties and functionality when the components are present in the concentrations as listed +/−2 weight percent. The compositions containing CO2 would be expected to maintain the desired properties and functionality when the CO2 was present at the listed concentration +/−0.2 weight percent.

The compositions of the present invention may be azeotropic or near-azeotropic compositions. By azeotropic composition is meant a constant-boiling mixture of two or more substances that behave as a single substance. One way to characterize an azeotropic composition is that the vapor produced by partial evaporation or distillation of the liquid has the same composition as the liquid from which it is evaporated or distilled, i.e., the mixture distills/refluxes without compositional change. Constant-boiling compositions are characterized as azeotropic because they exhibit either a maximum or minimum boiling point, as compared with that of the non-azeotropic mixture of the same compounds. An azeotropic composition will not fractionate within a refrigeration or air conditioning system during operation, which may reduce efficiency of the system. Additionally, an azeotropic composition will not fractionate upon leakage from a refrigeration or air conditioning system. In the situation where one component of a mixture is flammable, fractionation during leakage could lead to a flammable composition either within the system or outside of the system.

A near-azeotropic composition (also commonly referred to as an “azeotrope-like composition”) is a substantially constant boiling liquid admixture of two or more substances that behaves essentially as a single substance. One way to characterize a near-azeotropic composition is that the vapor produced by partial evaporation or distillation of the liquid has substantially the same composition as the liquid from which it was evaporated or distilled, that is, the admixture distills/refluxes without substantial composition change. Another way to characterize a near-azeotropic composition is that the bubble point vapor pressure and the dew point vapor pressure of the composition at a particular temperature are substantially the same. Herein, a composition is near-azeotropic if, after 50 weight percent of the composition is removed, such as by evaporation or boiling off, the difference in vapor pressure between the original composition and the composition remaining after 50 weight percent of the original composition has been removed is less than about 10 percent.

Azeotropic compositions of the present invention at a specified temperature are shown in Table 3.

TABLE 3 Wt % Wt % T Component A Component B A B Psia kPa (C.) HFC-1234yf HFC-32 7.4 92.6 49.2 339 −25 HFC-1234yf HFC-125 10.9 89.1 40.7 281 −25 HFC-1234yf HFC-134a 70.4 29.6 18.4 127 −25 HFC-1234yf HFC-152a 91.0 9.0 17.9 123 −25 HFC-1234yf HFC-143a 17.3 82.7 39.5 272 −25 HFC-1234yf HFC-227ea 84.6 15.4 18.0 124 −25 HFC-1234yf propane 51.5 48.5 33.5 231 −25 HFC-1234yf n-butane 98.1 1.9 17.9 123 −25 HFC-1234yf isobutane 88.1 11.9 19.0 131 −25 HFC-1234yf DME 53.5 46.5 13.1 90 −25 HFC-1225ye trans-HFC- 63.0 37.0 11.7 81 −25 1234ze HFC-1225ye HFC-1243zf 40.0 60.0 13.6 94 −25 HFC-1225ye HFC-134 52.2 47.8 12.8 88 −25 HFC-1225ye HFC-152a 7.3 92.7 14.5 100 −25 HFC-1225ye propane 29.7 70.3 30.3 209 −25 HFC-1225ye n-butane 89.5 10.5 12.3 85 −25 HFC-1225ye isobutane 79.3 20.7 13.9 96 −25 HFC-1225ye DME 82.1 17.9 10.8 74 −25 HFC-1225ye CF3SCF3 37.0 63.0 12.4 85 −25 trans-HFC-1234ze HFC-1243zf 17.0 83.0 13.0 90 −25 trans-HFC-1234ze HFC-134 45.7 54.3 12.5 86 −25 trans-HFC-1234ze HFC-134a 9.5 90.5 15.5 107 −25 trans-HFC-1234ze HFC-152a 21.6 78.4 14.6 101 −25 trans-HFC-1234ze HFC-227ea 59.2 40.8 11.7 81 −25 trans-HFC-1234ze propane 28.5 71.5 30.3 209 −25 trans-HFC-1234ze n-butane 88.6 11.4 11.9 82 −25 trans-HFC-1234ze isobutane 77.9 22.1 12.9 89 −25 trans-HFC-1234ze DME 84.1 15.9 10.8 74 −25 trans-HFC-1234ze CF3SCF3 34.3 65.7 12.7 88 −25 HFC-1243zf HFC-134 63.0 37.0 13.5 93 −25 HFC-1243zf HFC-134A 25.1 74.9 15.9 110 −25 HFC-1243zf HFC-152A 40.7 59.3 15.2 104 −25 HFC-1243zf HFC-227ea 78.5 21.5 13.1 90 −25 HFC-1243zf propane 32.8 67.2 31.0 213 −25 HFC-1243zf n-butane 90.3 9.7 13.5 93 −25 HFC-1243zf isobutane 80.7 19.3 14.3 98 −25 HFC-1243zf DME 72.7 27.3 12.0 83 −25 cis-HFC-1234ze HFC-236ea 20.9 79.1 30.3 209 25 cis-HFC-1234ze HFC-245fa 76.2 23.8 26.1 180 25 cis-HFC-1234ze n-butane 51.4 48.6 6.08 42 −25 cis-HFC-1234ze isobutane 26.2 73.8 8.74 60 −25 cis-HFC-1234ze 2-methylbutane 86.6 13.4 27.2 188 25 cis-HFC-1234ze n-pentane 92.9 7.1 26.2 181 25 HFC-1234ye HFC-236ea 24.0 76.0 3.35 23.1 −25 HFC-1234ye HFC-245fa 42.5 57.5 22.8 157 25 HFC-1234ye n-butane 41.2 58.8 38.0 262 25 HFC-1234ye isobutane 16.4 83.6 50.9 351 25 HFC-1234ye 2-methylbutane 80.3 19.7 23.1 159 25 HFC-1234ye n-pentane 87.7 12.3 21.8 150 25

Additionally, ternary azeotropes composition have been found as listed in Table 4.

TABLE 4 Pres Pres Temp Component A Component B Component C Wt % A Wt % B Wt % C (psi) (kPa) (° C.) HFC-1234yf HFC-32 HFC-143A 3.9 74.3 21.8 50.02 345 −25 HFC-1234yf HFC-32 isobutane 1.1 92.1 6.8 50.05 345 −25 HFC-1234yf HFC-125 HFC-143A 14.4 43.5 42.1 38.62 266 −25 HFC-1234yf HFC-125 isobutane 9.7 89.1 1.2 40.81 281 −25 HFC-1234yf HFC-134 propane 4.3 39.1 56.7 34.30 236 −25 HFC-1234yf HFC-134 DME 15.2 67.0 17.8 10.38 71.6 −25 HFC-1234yf HFC-134a propane 24.5 31.1 44.5 34.01 234 −25 HFC-1234yf HFC-134a n-butane 60.3 35.2 4.5 18.58 128 −25 HFC-1234yf HFC-134a isobutane 48.6 37.2 14.3 19.86 137 −25 HFC-1234yf HFC-134a DME 24.0 67.9 8.1 17.21 119 −25 HFC-1234yf HFC-143a propane 17.7 71.0 11.3 40.42 279 −25 HFC-1234yf HFC-143a DME 5.7 93.0 1.3 39.08 269 −25 HFC-1234yf HFC-152a n-butane 86.6 10.8 2.7 17.97 124 −25 HFC-1234yf HFC-152a isobutane 75.3 11.8 12.9 19.12 132 −25 HFC-1234yf HFC-152a DME 24.6 43.3 32.1 11.78 81.2 −25 HFC-1234yf HFC-227ea propane 35.6 17.8 46.7 33.84 233 −25 HFC-1234yf HFC-227ea n-butane 81.9 16.0 2.1 18.07 125 −25 HFC-1234yf HFC-227ea isobutane 70.2 18.2 11.6 19.27 133 −25 HFC-1234yf HFC-227ea DME 28.3 55.6 16.1 15.02 104 −25 HFC-1234yf n-butane DME 48.9 4.6 46.4 13.15 90.7 −25 HFC-1234yf isobutane DME 31.2 26.2 42.6 14.19 97.8 −25 HFC-1234yf DME CF3I 16.3 10.0 73.7 15.65 108 −25 HFC-1234yf DME CF3SCF3 34.3 10.5 55.2 14.57 100 −25 HFC-1225ye trans-HFC- HFC-134 47.4 5.6 47.0 12.77 88.0 −25 1234ze HFC-1225ye trans-HFC- HFC-227ea 28.4 52.6 19.0 11.63 80.2 −25 1234ze HFC-1225ye trans-HFC- propane 20.9 9.1 70.0 30.36 209 −25 1234ze HFC-1225ye trans-HFC- n-butane 65.8 24.1 10.1 12.39 85.4 −25 1234ze HFC-1225ye trans-HFC- DME 41.0 40.1 18.9 10.98 75.7 −25 1234ze HFC-1225ye trans-HFC- CF3SCF3 1.0 33.7 65.2 12.66 87.3 −25 1234ze HFC-1225ye HFC-1243zf HFC-134 28.7 47.3 24.1 13.80 95.1 −25 HFC-1225ye HFC-1243zf n-butane 37.5 55.0 7.5 13.95 96.2 −25 HFC-1225ye HFC-1243zf isobutane 40.5 43.2 16.3 14.83 102 −25 HFC-1225ye HFC-1243zf DME 19.1 51.0 29.9 12.15 83.8 −25 HFC-1225ye HFC-1243zf CF3I 10.3 27.3 62.3 14.05 96.9 −25 HFC-1225ye HFC-134 HFC-152a 63.6 26.8 9.6 12.38 85.4 −25 HFC-1225ye HFC-134 HFC-227ea 1.3 52.3 46.4 12.32 84.9 −25 HFC-1225ye HFC-134 n-butane 18.1 67.1 14.9 14.54 100 −25 HFC-1225ye HFC-134 isobutane 0.7 74.0 25.3 16.68 115 −25 HFC-1225ye HFC-134 DME 29.8 52.5 17.8 9.78 67.4 −25 HFC-1225ye HFC-227ea DME 63.1 31.0 5.8 10.93 75.4 −25 HFC-1225ye n-butane DME 66.0 13.0 21.1 11.34 78.2 −25 HFC-1225ye n-butane CF3SCF3 71.3 5.6 23.0 12.25 84.5 −25 HFC-1225ye isobutane DME 49.9 29.7 20.4 12.83 88.5 −25 HFC-1225ye isobutane CF3I 27.7 2.2 70.1 13.19 90.9 −25 Trans-HFC- HFC-1243zf HFC-227ea 7.1 73.7 19.2 13.11 90.4 −25 1234ze Trans-HFC- HFC-1243zf n-butane 9.5 81.2 9.3 13.48 92.9 −25 1234ze Trans-HFC- HFC-1243zf isobutane 3.3 77.6 19.1 14.26 98.3 −25 1234ze Trans-HFC- HFC-1243zf DME 2.6 70.0 27.4 12.03 82.9 −25 1234ze Trans-HFC- HFC-134 HFC-152a 52.0 42.9 5.1 12.37 85.3 −25 1234ze Trans-HFC- HFC-134 HFC-227ea 30.0 43.2 26.8 12.61 86.9 −25 1234ze Trans-HFC- HFC-134 DME 27.7 54.7 17.7 9.76 67.3 −25 1234ze Trans-HFC- HFC-134a HFC-152a 14.4 34.7 51.0 14.42 99.4 −25 1234ze Trans-HFC- HFC-152a n-butane 5.4 80.5 14.1 15.41 106 −25 1234ze Trans-HFC- HFC-152a DME 59.1 16.4 24.5 10.80 74.5 −25 1234ze Trans-HFC- HFC-227ea n-butane 40.1 48.5 11.3 12.61 86.9 −25 1234ze Trans-HFC- n-butane DME 68.1 13.0 18.9 11.29 77.8 −25 1234ze Trans-HFC- n-butane CF3I 81.2 9.7 9.1 11.87 81.8 −25 1234ze Trans-HFC- isobutane DME 55.5 28.7 15.8 12.38 85.4 −25 1234ze Trans-HFC- isobutane CF3I 34.9 6.1 59.0 12.57 86.7 −25 1234ze Trans-HFC- isobutane CF3SCF3 37.7 1.1 61.7 12.66 87.3 −25 1234ze HFC-1243zf HFC-134 HFC-227ea 58.6 34.1 7.3 13.54 93.4 −25 HFC-1243zf HFC-134 n-butane 27.5 58.7 13.9 14.72 101 −25 HFC-1243zf HFC-134 DME 18.7 63.5 17.8 10.11 69.7 −25 HFC-1243zf HFC-134 CF3I 11.4 23.9 64.7 14.45 99.6 −25 HFC-1243zf HFC-134a HFC-152a 41.5 21.5 37.1 14.95 103 −25 HFC-1243zf HFC-134A n-butane 7.0 81.4 11.6 17.03 117 −25 HFC-1243zf HFC-152a propane 2.9 34.0 63.0 31.73 219 −25 HFC-1243zf HFC-152a n-butane 28.8 60.3 11.0 15.71 108 −25 HFC-1243zf HFC-152a isobutane 6.2 68.5 25.3 17.05 118 −25 HFC-1243zf HFC-152a DME 33.1 36.8 30.1 11.41 78.7 −25 HFC-1243zf HFC-227ea n-butane 62.0 28.4 9.6 13.67 94.3 −25 HFC-1243zf HFC-227ea isobutane 27.9 51.0 21.1 15.00 103 −25 HFC-1243zf HFC-227ea DME 48.1 44.8 7.2 12.78 88.1 −25 HFC-1243zf n-butane DME 60.3 10.1 29.6 12.28 84.7 −25 HFC-1243zf isobutane DME 47.1 26.9 25.9 13.16 90.7 −25 HFC-1243zf isobutane CF3I 32.8 1.1 66.1 13.97 96.3 −25 HFC-1243zf DME CF3SCF3 41.1 2.3 56.6 13.60 93.8 −25

The near-azeotropic compositions of the present invention at a specified temperature are listed in Table 5.

TABLE 5 Component A Component B (wt % A/wt % B) T (C.) HFC-1234yf HFC-32 1-57/99-43 −25 HFC-1234yf HFC-125 1-51/99-49 −25 HFC-1234yf HFC-134 1-99/99-1 −25 HFC-1234yf HFC-134a 1-99/99-1 −25 HFC-1234yf HFC-152a 1-99/99-1 −25 HFC-1234yf HFC-161 1-99/99-1 −25 HFC-1234yf HFC-143a 1-60/99-40 −25 HFC-1234yf HFC-227ea 29-99/71-1 −25 HFC-1234yf HFC-236fa 66-99/34-1 −25 HFC-1234yf HFC-1225ye 1-99/99-1 −25 HFC-1234yf trans-HFC-1234ze 1-99/99-1 −25 HFC-1234yf HFC-1243zf 1-99/99-1 −25 HFC-1234yf propane 1-80/99-20 −25 HFC-1234yf n-butane 71-99/29-1 −25 HFC-1234yf isobutane 60-99/40-1 −25 HFC-1234yf DME 1-99/99-1 −25 HFC-1225ye trans-HFC-1234ze 1-99/99-1 −25 HFC-1225ye HFC-1243zf 1-99/99-1 −25 HFC-1225ye HFC-134 1-99/99-1 −25 HFC-1225ye HFC-134a 1-99/99-1 −25 HFC-1225ye HFC-152a 1-99/99-1 −25 HFC-1225ye HFC-161 1-84/99-16, 90-99/ −25 10-1 HFC-1225ye HFC-227ea 1-99/99-1 −25 HFC-1225ye HFC-236ea 57-99/43-1 −25 HFC-1225ye HFC-236fa 48-99/52-1 −25 HFC-1225ye HFC-245fa 70-99/30-1 −25 HFC-1225ye propane 1-72/99-28 −25 HFC-1225ye n-butane 65-99/35-1 −25 HFC-1225ye isobutane 50-99/50-1 −25 HFC-1225ye DME 1-99/99-1 −25 HFC-1225ye CF3I 1-99/99-1 −25 HFC-1225ye CF3SCF3 1-99/99-1 −25 trans-HFC-1234ze cis-HFC-1234ze 73-99/27-1 −25 trans-HFC-1234ze HFC-1243zf 1-99/99-1 −25 trans-HFC-1234ze HFC-134 1-99/99-1 −25 trans-HFC-1234ze HFC-134a 1-99/99-1 −25 trans-HFC-1234ze HFC-152a 1-99/99-1 −25 trans-HFC-1234ze HFC-161 1-52/99-48, 87-99/ −25 13-1 trans-HFC-1234ze HFC-227ea 1-99/99-1 −25 trans-HFC-1234ze HFC-236ea 54-99/46-1 −25 trans-HFC-1234ze HFC-236fa 44-99/56-1 −25 trans-HFC-1234ze HFC-245fa 67-99/33-1 −25 trans-HFC-1234ze propane 1-71/99-29 −25 trans-HFC-1234ze n-butane 62-99/38-1 −25 trans-HFC-1234ze isobutane 39-99/61-1 −25 trans-HFC-1234ze DME 1-99/99-1 −25 trans-HFC-1234ze CF3SCF3 1-99/99-1 −25 trans-HFC-1234ze CF3I 1-99/99-1 −25 HFC-1243zf HFC-134 1-99/99-1 −25 HFC-1243zf HFC-134a 1-99/99-1 −25 HFC-1243zf HFC-152a 1-99/99-1 −25 HFC-1243zf HFC-161 1-99/99-1 −25 HFC-1243zf HFC-227ea 1-99/99-1 −25 HFC-1243zf HFC-236ea 53-99/47-1 −25 HFC-1243zf HFC-236fa 49-99/51-1 −25 HFC-1243zf HFC-245fa 66-99/34-1 −25 HFC-1243zf propane 1-71/99-29 −25 HFC-1243zf n-butane 62-99/38-1 −25 HFC-1243zf isobutane 45-99/55-1 −25 HFC-1243zf DME 1-99/99-1 −25 cis-HFC-1234ze HFC-236ea 1-99/99-1 25 cis-HFC-1234ze HFC-236fa 1-99/99-1 25 cis-HFC-1234ze HFC-245fa 1-99/99-1 25 cis-HFC-1234ze n-butane 1-80/99-20 −25 cis-HFC-1234ze isobutane 1-69/99-31 −25 cis-HFC-1234ze 2-methylbutane 60-99/40-1 25 cis-HFC-1234ze n-pentane 63-99/37-1 25 HFC-1234ye HFC-134 38-99/62-1 25 HFC-1234ye HFC-236ea 1-99/99-1 −25 HFC-1234ye HFC-236fa 1-99/99-1 25 HFC-1234ye HFC-245fa 1-99/99-1 25 HFC-1234ye Cis-HFC-1234ze 1-99/99-1 25 HFC-1234ye n-butane 1-78/99-22 25 HFC-1234ye cyclopentane 70-99/30-1 25 HFC-1234ye isobutane 1-68/99-32 25 HFC-1234ye 2-methylbutane 47-99/53-1 25 HFC-1234ye n-pentane 57-99/43-1 25

Ternary and higher order near-azeotrope compositions comprising fluoroolefins have also been identified as listed in Table 6.

TABLE 6 Near-azeotrope range Temp Components (weight percent) (° C.) HFC-1225ye/HFC-134a/HFC-152a 1-98/1-98/1-98 25 HFC-1225ye/HFC-134a/HFC-161 1-98/1-98/1-98 25 HFC-1225ye/HFC-134a/isobutane 1-98/1-98/1-40 25 HFC-1225ye/HFC-134a/DME 1-98/1-98/1-20 25 HFC-1225ye/HFC-152a/isobutane 1-98/1-98/1-50 25 HFC-1225ye/HFC-152a/DME 1-98/1-98/1-98 25 HFC-1225ye/HFC-1234yf/HFC-134a 1-98/1-98/1-98 25 HFC-1225ye/HFC-1234yf/HFC-152a 1-98/1-98/1-98 25 HFC-1225ye/HFC-1234yf/HFC-125 1-98/1-98/1-20 25 HFC-1225ye/HFC-1234yf/CF3I 1-98/1-98/1-98 25 HFC-1225ye/HFC-134a/HFC- 1-97/1-97/1-97/1-10 25 152a/HFC-32 HFC-125/HFC-1225ye/isobutane 80-98/1-19/1-10 25 HFC-125/trans-HFC- 80-98/1-19/1-10 25 1234ze/isobutane HFC-125/HFC-1234yf/isobutane 80-98/1-19/1-10 25 HFC-32/HFC-125/HFC-1225ye 1-98/1-98/1-4 25 HFC-32/HFC-125/trans-HFC-1234ze 1-98/1-98/1-50 25 HFC-32/HFC-125/HFC-1234yf 1-98/1-98/1-55 25 HFC-125/trans-HFC-1234ze/n-butane 80-98/1-19/1-10 25 HFC-125/HFC-1234yf/n-butane 80-98/1-19/1-10 25 HFC-1234yf/HFC-32/HFC-143a 1-50/1-98/1-98 −25 HFC-1234yf/HFC-32/isobutane 1-40/59-98/1-30 −25 HFC-1234yf/HFC-125/HFC-143a 1-60/1-98/1-98 −25 HFC-1234yf/HFC-125/isobutane 1-40/59-98/1-20 −25 HFC-1234yf/HFC-134/propane 1-80/1-70/19-90 −25 HFC-1234yf/HFC-134/DME 1-70/1-98/29-98 −25 HFC-1234yf/HFC-134a/propane 1-80/1-80/19-98 −25 HFC-1234yf/HFC-134a/n-butane 1-98/1-98/1-30 −25 HFC-1234yf/HFC-134a/isobutane 1-98/1-98/1-30 −25 HFC-1234yf/HFC-134a/DME 1-98/1-98/1-40 −25 HFC-1234yf/HFC-143a/propane 1-80/1-98/1-98 −25 HFC-1234yf/HFC-143a/DME 1-40/59-98/1-20 −25 HFC-1234yf/HFC-152a/n-butane 1-98/1-98/1-30 −25 HFC-1234yf/HFC-152a/isobutane 1-98/1-90/1-40 −25 HFC-1234yf/HFC-152a/DME 1-70/1-98/1-98 −25 HFC-1234yf/HFC-227ea/propane 1-80/1-70/29-98 −25 HFC-1234yf/HFC-227ea/n-butane 40-98/1-59/1-20 −25 HFC-1234yf/HFC-227ea/isobutane 30-98/1-69/1-30 −25 HFC-1234yf/HFC-227ea/DME 1-98/1-80/1-98 −25 HFC-1234yf/n-butane/DME 1-98/1-40/1-98 −25 HFC-1234yf/isobutane/DME 1-98/1-50/1-98 −25 HFC-1234yf/DME/CF3I 1-98/1-98/1-98 −25 HFC-1234yf/DME/CF3SCF3 1-98/1-40/1-80 −25 HFC-1225ye/trans-HFC- 1-98/1-98/1-98 −25 1234ze/HFC-134 HFC-1225ye/trans-HFC- 1-98/1-98/1-98 −25 1234ze/HFC-227ea HFC-1225ye/trans-HFC- 1-60/1-60/1-98 −25 1234ze/propane HFC-1225ye/trans-HFC-1234ze/n- 1-98/1-98/1-30 −25 butane HFC-1225ye/trans-HFC-1234ze/DME 1-98/1-98/1-98 −25 HFC-1225ye/trans-HFC-1234ze/ 1-98/1-98/1-98 −25 CF3SCF3 HFC-1225ye/HFC-1243zf/HFC-134 1-98/1-98/1-98 −25 HFC-1225ye/HFC-1243zf/n-butane 1-98/1-98/1-30 −25 HFC-1225ye/HFC-1243zf/isobutane 1-98/1-98/1-40 −25 HFC-1225ye/HFC-1243zf/DME 1-98/1-98/1-98 −25 HFC-1225ye/HFC-1243zf/CF3I 1-98/1-98/1-98 −25 HFC-1225ye/HFC-134/HFC-152a 1-98/1-98/1-98 −25 HFC-1225ye/HFC-134/HFC-227ea 1-98/1-98/1-98 −25 HFC-1225ye/HFC-134/n-butane 1-98/1-90/1-40 −25 HFC-1225ye/HFC-134/isobutane 1-98/1-90/1-40 −25 HFC-1225ye/HFC-134/DME 1-98/1-98/1-40 −25 HFC-1225ye/HFC-227ea/DME 40-98/1-59/1-30 −25 HFC-1225ye/n-butane/DME 1-98/1-30/1-98 −25 HFC-1225ye/n-butane/CF3SCF3 1-98/1-20/1-98 −25 HFC-1225ye/isobutane/DME 1-98/1-60/1-98 −25 HFC-1225ye/isobutane/CF3I 1-98/1-40/1-98 −25 trans-HFC-1234ze/HFC-1243zf/HFC- 1-98/1-98/1-98 −25 227ea trans-HFC-1234ze/HFC-1243zf/n- 1-98/1-98/1-30 −25 butane trans-HFC-1234ze/HFC- 1-98/1-98/1-40 −25 1243zf/isobutane trans-HFC-1234ze/HFC-1243zf/DME 1-98/1-98/1-98 −25 trans-HFC-1234ze/HFC-134/HFC- 1-98/1-98/1-98 −25 152a trans-HFC-1234ze/HFC-134/HFC- 1-98/1-98/1-98 −25 227ea trans-HFC-1234ze/HFC-134/DME 1-98/1-98/1-40 −25 trans-HFC-1234ze/HFC-134a/HFC- 1-98/1-98/1-98 −25 152a trans-HFC-1234ze/HFC-152a/n- 1-98/1-98/1-50 −25 butane trans-HFC-1234ze/HFC-152a/DME 1-98/1-98/1-98 −25 trans-HFC-1234ze/HFC-227ea/n- 1-98/1-98/1-40 −25 butane trans-HFC-1234ze/n-butane/DME 1-98/1-40/1-98 −25 trans-HFC-1234ze/n-butane/CF3I 1-98/1-30/1-98 −25 trans-HFC-1234ze/isobutane/DME 1-98/1-60/1-98 −25 trans-HFC-1234ze/isobutane/CF3I 1-98/1-40/1-98 −25 trans-HFC-1234ze/isobutane/ 1-98/1-40/1-98 −25 CF3SCF3 HFC-1243zf/HFC-134/HFC-227ea 1-98/1-98/1-98 −25 HFC-1243zf/HFC-134/n-butane 1-98/1-98/1-40 −25 HFC-1243zf/HFC-134/DME 1-98/1-98/1-98 −25 HFC-1243zf/HFC-134/CF3I 1-98/1-98/1-98 −25 HFC-1243zf/HFC-134a/HFC-152a 1-98/1-98/1-98 −25 HFC-1243zf/HFC-134a/n-butane 1-98/1-98/1-40 −25 HFC-1243zf/HFC-152a/propane 1-70/1-70/29-98 −25 HFC-1243zf/HFC-152a/n-butane 1-98/1-98/1-30 −25 HFC-1243zf/HFC-152a/isobutane 1-98/1-98/1-40 −25 HFC-1243zf/HFC-152a/DME 1-98/1-98/1-98 −25 HFC-1243zf/HFC-227ea/n-butane 1-98/1-98/1-40 −25 HFC-1243zf/HFC-227ea/isobutane 1-98/1-90/1-50 −25 HFC-1243zf/HFC-227ea/DME 1-98/1-80/1-90 −25 HFC-1243zf/n-butane/DME 1-98/1-40/1-98 −25 HFC-1243zf/isobutane/DME 1-98/1-60/1-98 −25 HFC-1243zf/isobutane/CF3I 1-98/1-40/1-98 −25 HFC-1243zf/DME/CF3SCF3 1-98/1-40/1-90 −25

Certain of the compositions of the present invention are non-azeotropic compositions. Those compositions of the present invention falling within the preferred ranges of Table 2, but outside of the near-azeotropic ranges of Table 5 and Table 6 may be considered to be non-azeotropic.

A non-azeotropic composition may have certain advantages over azeotropic or near azeotropic mixtures. A non-azeotropic composition is a mixture of two or more substances that behaves as a mixture rather than a single substance. One way to characterize a non-azeotropic composition is that the vapor produced by partial evaporation or distillation of the liquid has a substantially different composition as the liquid from which it was evaporated or distilled, that is, the admixture distills/refluxes with substantial composition change. Another way to characterize a non-azeotropic composition is that the bubble point vapor pressure and the dew point vapor pressure of the composition at a particular temperature are substantially different. Herein, a composition is non-azeotropic if, after 50 weight percent of the composition is removed, such as by evaporation or boiling off, the difference in vapor pressure between the original composition and the composition remaining after 50 weight percent of the original composition has been removed is greater than about 10 percent.

The compositions of the present invention may be prepared by any convenient method to combine the desired amounts of the individual components. A preferred method is to weigh the desired component amounts and thereafter combine the components in an appropriate vessel. Agitation may be used, if desired.

An alternative means for making compositions of the present invention may be a method for making a refrigerant blend composition, wherein said refrigerant blend composition comprises a composition as disclosed herein, said method comprising (i) reclaiming a volume of one or more components of a refrigerant composition from at least one refrigerant container, (ii) removing impurities sufficiently to enable reuse of said one or more of the reclaimed components, (iii) and optionally, combining all or part of said reclaimed volume of components with at least one additional refrigerant composition or component.

A refrigerant container may be any container in which is stored a refrigerant blend composition that has been used in a refrigeration apparatus, air-conditioning apparatus or heat pump apparatus. Said refrigerant container may be the refrigeration apparatus, air-conditioning apparatus or heat pump apparatus in which the refrigerant blend was used. Additionally, the refrigerant container may be a storage container for collecting reclaimed refrigerant blend components, including but not limited to pressurized gas cylinders.

Residual refrigerant means any amount of refrigerant blend or refrigerant blend component that may be moved out of the refrigerant container by any method known for transferring refrigerant blends or refrigerant blend components.

Impurities may be any component that is in the refrigerant blend or refrigerant blend component due to its use in a refrigeration apparatus, air-conditioning apparatus or heat pump apparatus. Such impurities include but are not limited to refrigeration lubricants, being those described earlier herein, particulates including but not limited to metal, metal salt or elastomer particles, that may have come out of the refrigeration apparatus, air-conditioning apparatus or heat pump apparatus, and any other contaminants that may adversely effect the performance of the refrigerant blend composition.

Such impurities may be removed sufficiently to allow reuse of the refrigerant blend or refrigerant blend component without adversely effecting the performance or equipment within which the refrigerant blend or refrigerant blend component will be used.

It may be necessary to provide additional refrigerant blend or refrigerant blend component to the residual refrigerant blend or refrigerant blend component in order to produce a composition that meets the specifications required for a given product. For instance, if a refrigerant blend has 3 components in a particular weight percentage range, it may be necessary to add one or more of the components in a given amount in order to restore the composition to within the specification limits.

The heat transfer fluid compositions of the present invention will have global warming potential (GWP) that are less than many hydrofluorocarbon refrigerants currently in use. Preferably, such compositions will also have zero or low ozone depletion potential. One aspect of the present invention is to provide a refrigerant with a global warming potential of less than 1000, less than 500, less than 150, less than 100, or less than 50. Another aspect of the present invention is to reduce the net GWP of refrigerant mixtures by adding fluoroolefins to said mixtures.

The compositions of the present invention may be useful as low global warming potential (GWP) replacements for currently used refrigerants, including but not limited to R134a (or HFC-134a, 1,1,1,2-tetrafluoroethane), R22 (or HCFC-22, chlorodifluoromethane), R123 (or HFC-123, 2,2-dichloro-1,1,1-trifluoroethane), R11 (CFC-11, fluorotrichloromethane), R12 (CFC-12, dichlorodifluoromethane), R245fa (or HFC-245fa, 1,1,1,3,3-pentafluoropropane), R114 (or CFC-114, 1,2-dichloro-1,1,2,2-tetrafluoroethane), R236fa (or HFC-236fa, 1,1,1,3,3,3-hexafluoropropane), R124 (or HCFC-124, 2-chloro-1,1,1,2-tetrafluoroethane), R407c (ASHRAE designation for a blend of 52 weight percent R134a, 25 weight percent R125 (pentafluoroethane), and 23 weight percent R32 (difluoromethane), R410A (ASHRAE designation for a blend of 50 weight percent R125 and 50 weight percent R32), R417A, (ASHRAE designation for a blend of 46.6 weight percent R125, 50.0 weight percent R134a, and 3.4 weight percent n-butane), R422A, R422B, R422c and R422D, (ASHRAE designation for a blend of 85.1 weight percent R125, 11.5 weight percent R134a, and 3.4 weight percent isobutane), R404A, (ASHRAE designation for a blend of 44 weight percent R125, 52 weight percent R143a (1,1,1-trifluoroethane), and 4.0 weight percent R134a) and R507A (ASHRAE designation for a blend of 50 weight percent R125 and 50 weight percent R143a). Additionally, the compositions of the present invention may be useful as replacements for R12 (CFC-12, dichlorodifluoromethane) or R502 (ASHRAE designation for a blend of 51.2 weight percent CFC-115 (chloropentafluoroethane) and 48.8 weight percent HCFC-22).

Often replacement refrigerants are most useful if capable of being used in the original refrigeration equipment designed for a different refrigerant. The compositions of the present invention may be useful as replacements for the above-mentioned refrigerants in original equipment. Additionally, the compositions of the present invention may be useful as replacements for the above mentioned refrigerants in equipment designed to use the above-mentioned refrigerants.

The compositions of the present invention may further comprise a lubricant. Lubricants of the present invention comprise refrigeration lubricants, i.e. those lubricants suitable for use with refrigeration, air-conditioning, or heat pump apparatus. Among these lubricants are those conventionally used in compression refrigeration apparatus utilizing chlorofluorocarbon refrigerants. Such lubricants and their properties are discussed in the 1990 ASHRAE Handbook, Refrigeration Systems and Applications, chapter 8, titled “Lubricants in Refrigeration Systems”, pages 8.1 through 8.21. Lubricants of the present invention may comprise those commonly known as “mineral oils” in the field of compression refrigeration lubrication. Mineral oils comprise paraffins (i.e. straight-chain and branched-carbon-chain, saturated hydrocarbons), naphthenes (i.e. cyclic paraffins) and aromatics (i.e. unsaturated, cyclic hydrocarbons containing one or more rings characterized by alternating double bonds). Lubricants of the present invention further comprise those commonly known as “synthetic oils” in the field of compression refrigeration lubrication. Synthetic oils comprise alkylaryls (i.e. linear and branched alkyl alkylbenzenes), synthetic paraffins and napthenes, and poly(alphaolefins). Representative conventional lubricants of the present invention are the commercially available BVM 100 N (paraffinic mineral oil sold by BVA Oils), Suniso® 3GS and Suniso® 5GS (naphthenic mineral oil sold by Crompton Co.), Sontex® 372LT (naphthenic mineral oil sold by Pennzoil), Calumet® RO-30 (naphthenic mineral oil sold by Calumet Lubricants), Zerol® 75, Zerol® 150 and Zerol® 500 (linear alkylbenzenes sold by Shrieve Chemicals) and HAB 22 (branched alkylbenzene sold by Nippon Oil).

Lubricants of the present invention further comprise those that have been designed for use with hydrofluorocarbon refrigerants and are miscible with refrigerants of the present invention under compression refrigeration, air-conditioning, or heat pump apparatus' operating conditions. Such lubricants and their properties are discussed in “Synthetic Lubricants and High-Performance Fluids”, R. L. Shubkin, editor, Marcel Dekker, 1993. Such lubricants include, but are not limited to, polyol esters (POEs) such as Castrol® 100 (Castrol, United Kingdom), polyalkylene glycols (PAGs) such as RL-488A from Dow (Dow Chemical, Midland, Mich.), and polyvinyl ethers (PVEs). These lubricants are readily available from various commercial sources.

Lubricants of the present invention are selected by considering a given compressor's requirements and the environment to which the lubricant will be exposed. Lubricants of the present invention preferably have a kinematic viscosity of at least about 5 cs (centistokes) at 40° C.

Commonly used refrigeration system additives may optionally be added, as desired, to compositions of the present invention in order to enhance lubricity and system stability. These additives are generally known within the field of refrigeration compressor lubrication, and include anti wear agents, extreme pressure lubricants, corrosion and oxidation inhibitors, metal surface deactivators, free radical scavengers, foaming and antifoam control agents, leak detectants and the like. In general, these additives are present only in small amounts relative to the overall lubricant composition. They are typically used at concentrations of from less than about 0.1% to as much as about 3% of each additive. These additives are selected on the basis of the individual system requirements. Some typical examples of such additives may include, but are not limited to, lubrication enhancing additives, such as alkyl or aryl esters of phosphoric acid and of thiophosphates. Additionally, the metal dialkyl dithiophosphates (e.g. zinc dialkyl dithiophosphate or ZDDP, Lubrizol 1375) and other members of this family of chemicals may be used in compositions of the present invention. Other antiwear additives include natural product oils and assymetrical polyhydroxyl lubrication additives such as Synergol TMS (International Lubricants). Similarly, stabilizers such as anti oxidants, free radical scavengers, and water scavengers may be employed. Compounds in this category can include, but are not limited to, butylated hydroxy toluene (BHT) and epoxides.

The compositions of the present invention may further comprise about 0.01 weight percent to about 5 weight percent of an additive such as, for example, a stabilizer, free radical scavenger and/or antioxidant. Such additives include but are not limited to, nitromethane, hindered phenols, hydroxylamines, thiols, phosphites, or lactones. Single additives or combinations may be used.

The compositions of the present invention may further comprise about 0.01 weight percent to about 5 weight percent of a water scavenger (drying compound). Such water scavengers may comprise ortho esters such as trimethyl-, triethyl-, or tripropylortho formate.

The compositions of the present invention may further comprise a tracer selected from the group consisting of hydrofluorocarbons (HFCs), deuterated hydrocarbons, deuterated hydrofluorocarbons, perfluorocarbons, fluoroethers, brominated compounds, iodated compounds, alcohols, aldehydes, ketones, nitrous oxide (N2O) and combinations thereof. The tracer compounds are added to the compositions in previously determined quantities to allow detection of any dilution, contamination or other alteration of the composition, as described in U.S. patent application Ser. No. 11/062,044, filed Feb. 18, 2005.

Typical tracer compounds for use in the present compositions are listed in Table 7.

TABLE 7 Compound Structure Deuterated hydrocarbons and hydrofluorocarbons Ethane-d6 CD3CD3 Propane-d8 CD3CD2CD3 HFC-32-d2 CD2F2 HFC-134a-d2 CD2FCF3 HFC-143a-d3 CD3CF3 HFC-125-d CDF2CF3 HFC-227ea-d CF3CDFCF3 HFC-227ca-d CF3CF2CDF2 HFC-134-d2 CDF2CDF2 HFC-236fa-d2 CF3CD2CF3 HFC-245cb-d3 CF3CF2CD3 HFC-263fb-d2* CF3CD2CH3 HFC-263fb-d3 CF2CH2CD3 Fluoroethers HFOC-125E CHF2OCF3 HFOC-134aE CH2FOCF3 HFOC-143aE CH3OCF3 HFOC-227eaE CF3OCHFCF3 HFOC-236faE CF3OCH2CF3 HFOC-245faEβγ or CHF2OCH2CF3 HFOC-245faEαβ (or CHF2CH2OCF3) HFOC-245cbEβγ or CH3OCF2CF3 HFOC-245cbαβ (or CH3CF2OCF3) HFE-42-11mcc (or Freon ® E1) CF3CF2CF2OCHFCF3 Freon ® E2 CF3CF2CF2OCF(CF3) CF2OCHFCF3 Hydrofluorocarbons HFC-23 CHF3 HFC-161 CH3CH2F HFC-152a CH3CHF2 HFC-134 CHF2CHF2 HFC-227ea CF3CHFCF3 HFC-227ca CHF2CF2CF3 HFC-236cb CH2FCF2CF3 HFC-236ea CF3CHFCHF2 HFC-236fa CF3CH2CF3 HFC-245cb CF3CF2CH3 HFC-245fa CHF2CH2CF3 HFC-254cb CHF2CF2CH3 HFC-254eb CF3CHFCH3 HFC-263fb CF3CH2CH3 HFC-272ca CH3CF2CH3 HFC-281ea CH3CHFCH3 HFC-281fa CH2FCH2CH3 HFC-329p CHF2CF2CF2CF3 HFC-329mmz (CH3)2CHCF3 HFC-338mf CF3CH2CF2CF3 HFC-338pcc CHF2CF2CF2CHF2 HFC-347s CH3CF2CF2CF3 HFC-43-10mee CF3CHFCHFCF2CF3 Perfluorocarbons PFC-116 CF3CF3 PFC-C216 Cyclo(—CF2CF2CF2—) PFC-218 CF3CF2CF3 PFC-C318 Cyclo(—CF2CF2CF2CF2—) PFC-31-10mc CF3CF2CF2CF3 PFC-31-10my (CF3)2CFCF3 PFC-C51-12mycm Cyclo(—CF(CF3)CF2CF(CF3)CF2—) PFC-C51-12mym, trans-cyclo(—CF2CF(CF3)CF(CF3)CF2—) PFC-C51-12mym, cis-cyclo(—CF2CF(CF3)CF(CF3)CF2—) Perfluoromethylcyclo-pentane Cyclo(—CF2CF2(CF3)CF2CF2CF2—) Perfluoromethylcyclo-hexane Cyclo(—CF2CF2(CF3)CF2CF2CF2CF2—) Perfluorodimethylcyclo-hexane Cyclo(—CF2CF2(CF3)CF2CF2(CF3)CF2—) (ortho, meta, or para) Perfluoroethylcyclohexane Cyclo(—CF2CF2(CF2CF3)CF2CF2CF2CF2—) Perfluoroindan C9F10 (see structure below) Perfluorotrimethylcyclo-hexane Cyclo(—CF2(CF3)CF2(CF3)CF2CF2(CF3)CF2—) (all possible isomers) Perfluoroisopropylcyclo-hexane Cyclo(—CF2CF2(CF2(CF3)2)CF2CF2CF2CF2—) Perfluorodecalin C10F18 (see structure below) (cis or trans, trans shown) Perfluoromethyldecalin (cis or trans C11F20 (see structure below) and all additional possible isomers) Brominated compounds Bromomethane CH3Br Bromofluoromethane CH2FBr Bromodifluoromethane CHF2Br Dibromofluoromethane CHFBr2 Tribromomethane CHBr3 Bromoethane CH3CH2Br Bromoethene CH2═CHBr 1,2-dibromoethane CH2BrCH2Br 1-bromo-1,2-difluoroethene CFBr═CHF Iodated compounds Iodotrifluoromethane CF3I Difluoroiodomethane CHF2I Fluoroiodomethane CH2FI 1,1,2-trifluoro-1-iodoethane CF2ICH2F 1,1,2,2-tetrafluoro-1-iodoethane CF2ICHF2 1,1,2,2-tetrafluoro-1,2-diiodoethane CF2ICF2I Iodopentafluorobenzene C6F5I Alcohols Ethanol CH3CH2OH n-propanol CH3CH2CH2OH Isopropanol CH3CH(OH)CH3 Aldehydes and Ketones Acetone (2-propanone) CH3C(O)CH3 n-propanal CH3CH2CHO n-butanal CH3CH2CH2CHO Methyl ethyl ketone (2-butanone) CH3C(O)CH2CH3 Other Nitrous oxide N2O

The compounds listed in Table 7 are available commercially (from chemical supply houses) or may be prepared by processes known in the art.

Single tracer compounds may be used in combination with the heat transfer fluid compositions of the present invention or multiple tracer compounds may be combined in any proportion to serve as a tracer blend. The tracer blend may contain multiple tracer compounds from the same class of compounds or multiple tracer compounds from different classes of compounds. For example, a tracer blend may contain 2 or more deuterated hydrofluorocarbons, or one deuterated hydrofluorocarbon in combination with one or more perfluorocarbons.

Additionally, some of the compounds in Table 7 exist as multiple isomers, structural or optical. Single isomers or multiple isomers of the same compound may be used in any proportion to prepare the tracer compound. Further, single or multiple isomers of a given compound may be combined in any proportion with any number of other compounds to serve as a tracer blend.

The tracer compound or tracer blend may be present in the compositions at a total concentration of about 50 parts per million by weight (ppm) to about 1000 ppm. Preferably, the tracer compound or tracer blend is present at a total concentration of about 50 ppm to about 500 ppm and most preferably, the tracer compound or tracer blend is present at a total concentration of about 100 ppm to about 300 ppm.

The compositions of the present invention may further comprise a compatibilizer selected from the group consisting of polyoxyalkylene glycol ethers, amides, nitriles, ketones, chlorocarbons, esters, lactones, aryl ethers, fluoroethers and 1,1,1-trifluoroalkanes. The compatibilizer is used to improve solubility of hydrofluorocarbon refrigerants in conventional refrigeration lubricants. Refrigeration lubricants are needed to lubricate the compressor of a refrigeration, air-conditioning or heat pump apparatus. The lubricant must move throughout the apparatus with the refrigerant in particular it must return from the non-compressor zones to the compressor to continue to function as lubricant and avoid compressor failure.

Hydrofluorocarbon refrigerants are generally not compatible with convention refrigeration lubricants such as mineral oils, alkylbenzenes, synthetic paraffins, synthetic napthenes and poly(alpha)olefins. Many replacement lubricants have been proposed, however, the polyalkylene glycols, polyol esters and polyvinyl ethers, suggested for use with hydrofluorocarbon refrigerants are expensive and absorb water readily. Water in a refrigeration, air-conditioning system or heat pump can lead to corrosion and the formation of particles that may plug the capillary tubes and other small orifices in the system, ultimately causing system failure. Additionally, in existing equipment, time-consuming and costly flushing procedures are required to change to a new lubricant. Therefore, it is desirable to continue to use the original lubricant if possible.

The compatibilizers of the present invention improve solubility of the hydrofluorocarbon refrigerants in conventional refrigeration lubricants and thus improve oil return to the compressor.

Polyoxyalkylene glycol ether compatibilizers of the present invention are represented by the formula R1[(OR2)xOR3]y, wherein: x is an integer from 1-3; y is an integer from 1-4; R1 is selected from hydrogen and aliphatic hydrocarbon radicals having 1 to 6 carbon atoms and y bonding sites; R2 is selected from aliphatic hydrocarbylene radicals having from 2 to 4 carbon atoms; R3 is selected from hydrogen and aliphatic and alicyclic hydrocarbon radicals having from 1 to 6 carbon atoms; at least one of R1 and R3 is said hydrocarbon radical; and wherein said polyoxyalkylene glycol ethers have a molecular weight of from about 100 to about 300 atomic mass units. As used herein, bonding sites mean radical sites available to form covalent bonds with other radicals. Hydrocarbylene radicals mean divalent hydrocarbon radicals. In the present invention, preferred polyoxyalkylene glycol ether compatibilizers are represented by R1[(OR2)xOR3]y: x is preferably 1-2; y is preferably 1; R1 and R3 are preferably independently selected from hydrogen and aliphatic hydrocarbon radicals having 1 to 4 carbon atoms; R2 is preferably selected from aliphatic hydrocarbylene radicals having from 2 or 3 carbon atoms, most preferably 3 carbon atoms; the polyoxyalkylene glycol ether molecular weight is preferably from about 100 to about 250 atomic mass units, most preferably from about 125 to about 250 atomic mass units. The R1 and R3 hydrocarbon radicals having 1 to 6 carbon atoms may be linear, branched or cyclic. Representative R1 and R3 hydrocarbon radicals include methyl, ethyl, propyl, isopropyl, butyl, isobutyl, sec-butyl, tert-butyl, pentyl, isopentyl, neopentyl, tert-pentyl, cyclopentyl, and cyclohexyl. Where free hydroxyl radicals on the present polyoxyalkylene glycol ether compatibilizers may be incompatible with certain compression refrigeration apparatus materials of construction (e.g. Mylar®), R1 and R3 are preferably aliphatic hydrocarbon radicals having 1 to 4 carbon atoms, most preferably 1 carbon atom. The R2 aliphatic hydrocarbylene radicals having from 2 to 4 carbon atoms form repeating oxyalkylene radicals —(OR2)x— that include oxyethylene radicals, oxypropylene radicals, and oxybutylene radicals. The oxyalkylene radical comprising R2 in one polyoxyalkylene glycol ether compatibilizer molecule may be the same, or one molecule may contain different R2oxyalkylene groups. The present polyoxyalkylene glycol ether compatibilizers preferably comprise at least one oxypropylene radical. Where R1 is an aliphatic or alicyclic hydrocarbon radical having 1 to 6 carbon atoms and y bonding sites, the radical may be linear, branched or cyclic. Representative R1 aliphatic hydrocarbon radicals having two bonding sites include, for example, an ethylene radical, a propylene radical, a butylene radical, a pentylene radical, a hexylene radical, a cyclopentylene radical and a cyclohexylene radical. Representative R1 aliphatic hydrocarbon radicals having three or four bonding sites include residues derived from polyalcohols, such as trimethylolpropane, glycerin, pentaerythritol, 1,2,3-trihydroxycyclohexane and 1,3,5-trihydroxycyclohexane, by removing their hydroxyl radicals.

Representative polyoxyalkylene glycol ether compatibilizers include but are not limited to: CH3OCH2CH(CH3)O(H or CH3) (propylene glycol methyl (or dimethyl)ether), CH3O[CH2CH(CH3)O]2(H or CH3) (dipropylene glycol methyl (or dimethyl)ether), CH3O[CH2CH(CH3)O]3(H or CH3) (tripropylene glycol methyl (or dimethyl)ether), C2H5OCH2CH(CH3)O(H or C2H5) (propylene glycol ethyl (or diethyl)ether), C2H5O[CH2CH(CH3)O]2(H or C2H5) (dipropylene glycol ethyl (or diethyl)ether), C2H5O[CH2CH(CH3)O]3(H or C2H5) (tripropylene glycol ethyl (or diethyl)ether), C3H7OCH2CH(CH3)O(H or C3H7) (propylene glycol n-propyl (or di-n-propyl)ether), C3H7O[CH2CH(CH3)O]2(H or C3H7) (dipropylene glycol n-propyl (or di-n-propyl)ether), C3H7O[CH2CH(CH3)O]3(H or C3H7) (tripropylene glycol n-propyl (or di-n-propyl)ether), C4H9OCH2CH(CH3)OH (propylene glycol n-butyl ether), C4H9O[CH2CH(CH3)O]2(H or C4H9) (dipropylene glycol n-butyl (or di-n-butyl)ether), C4H9O[CH2CH(CH3)O]3(H or C4H9) (tripropylene glycol n-butyl (or di-n-butyl)ether), (CH3)3COCH2CH(CH3)OH (propylene glycol t-butyl ether), (CH3)3CO[CH2CH(CH3)O]2(H or (CH3)3) (dipropylene glycol t-butyl (or di-t-butyl)ether), (CH3)3CO[CH2CH(CH3)O]3(H or (CH3)3) (tripropylene glycol t-butyl (or di-t-butyl)ether), C5H11OCH2CH(CH3)OH (propylene glycol n-pentyl ether), C4H9OCH2CH(C2H5)OH (butylene glycol n-butyl ether), C4H9O[CH2CH(C2H5)O]2H (dibutylene glycol n-butyl ether), trimethylolpropane tri-n-butyl ether (C2H5C(CH2—O—(CH2)3CH3)3) and trimethylolpropane di-n-butyl ether (C2H5C(CH2OC(CH2)3CH3)2CH2OH).

Amide compatibilizers of the present invention comprise those represented by the formulae R1C(O)NR2R3 and cyclo-[R4C(O)N(R5)], wherein R1, R2, R3 and R5 are independently selected from aliphatic and alicyclic hydrocarbon radicals having from 1 to 12 carbon atoms; R4 is selected from aliphatic hydrocarbylene radicals having from 3 to 12 carbon atoms; and wherein said amides have a molecular weight of from about 100 to about 300 atomic mass units. The molecular weight of said amides is preferably from about 160 to about 250 atomic mass units. R1, R2, R3 and R5 may optionally include substituted hydrocarbon radicals, that is, radicals containing non-hydrocarbon substituents selected from halogens (e.g., fluorine, chlorine) and alkoxides (e.g. methoxy). R1, R2, R3 and R5 may optionally include heteroatom-substituted hydrocarbon radicals, that is, radicals, which contain the atoms nitrogen (aza-), oxygen (oxa-) or sulfur (thia-) in a radical chain otherwise composed of carbon atoms. In general, no more than three non-hydrocarbon substituents and heteroatoms, and preferably no more than one, will be present for each 10 carbon atoms in R1-3, and the presence of any such non-hydrocarbon substituents and heteroatoms must be considered in applying the aforementioned molecular weight limitations. Preferred amide compatibilizers consist of carbon, hydrogen, nitrogen and oxygen. Representative R1, R2, R3 and R5 aliphatic and alicyclic hydrocarbon radicals include methyl, ethyl, propyl, isopropyl, butyl, isobutyl, sec-butyl, tert-butyl, pentyl, isopentyl, neopentyl, tert-pentyl, cyclopentyl, cyclohexyl, heptyl, octyl, nonyl, decyl, undecyl, dodecyl and their configurational isomers. A preferred embodiment of amide compatibilizers are those wherein R4 in the aforementioned formula cyclo-[R4C(O)N(R5)—] may be represented by the hydrocarbylene radical (CR6R7)n, in other words, the formula: cyclo-[(CR6R7)nC(O)N(R5)—] wherein: the previously-stated values for molecular weight apply; n is an integer from 3 to 5; R5 is a saturated hydrocarbon radical containing 1 to 12 carbon atoms; R6 and R7 are independently selected (for each n) by the rules previously offered defining R1-3. In the lactams represented by the formula: cyclo-[(CR6R7)nC(O)N(R5)—], all R6 and R7 are preferably hydrogen, or contain a single saturated hydrocarbon radical among the n methylene units, and R5 is a saturated hydrocarbon radical containing 3 to 12 carbon atoms. For example, 1-(saturated hydrocarbon radical)-5-methylpyrrolidin-2-ones.

Representative amide compatibilizers include but are not limited to: 1-octyl pyrrolidin-2-one, 1-decylpyrrolidin-2-one, 1-octyl-5-methylpyrrolidin-2-one, 1-butylcaprolactam, 1-cyclohexylpyrrolidin-2-one, 1-butyl-5-methylpiperid-2-one, 1-pentyl-5-methylpiperid-2-one, 1-hexylcaprolactam, 1-hexyl-5-methylpyrrolidin-2-one, 5-methyl-1-pentylpiperid-2-one, 1,3-dimethylpiperid-2-one, 1-methylcaprolactam, 1-butyl-pyrrolidin-2-one, 1,5-dimethylpiperid-2-one, 1-decyl-5-methylpyrrolidin-2-one, 1-dodecylpyrrolid-2-one, N,N-dibutylformamide and N,N-diisopropylacetamide.

Ketone compatibilizers of the present invention comprise ketones represented by the formula R1C(O)R2, wherein R1 and R2 are independently selected from aliphatic, alicyclic and aryl hydrocarbon radicals having from 1 to 12 carbon atoms, and wherein said ketones have a molecular weight of from about 70 to about 300 atomic mass units. R1 and R2 in said ketones are preferably independently selected from aliphatic and alicyclic hydrocarbon radicals having 1 to 9 carbon atoms. The molecular weight of said ketones is preferably from about 100 to 200 atomic mass units. R1 and R2 may together form a hydrocarbylene radical connected and forming a five, six, or seven-membered ring cyclic ketone, for example, cyclopentanone, cyclohexanone, and cycloheptanone. R1 and R2 may optionally include substituted hydrocarbon radicals, that is, radicals containing non-hydrocarbon substituents selected from halogens (e.g., fluorine, chlorine) and alkoxides (e.g. methoxy). R1 and R2 may optionally include heteroatom-substituted hydrocarbon radicals, that is, radicals, which contain the atoms nitrogen (aza-), oxygen (keto-, oxa-) or sulfur (thia-) in a radical chain otherwise composed of carbon atoms. In general, no more than three non-hydrocarbon substituents and heteroatoms, and preferably no more than one, will be present for each 10 carbon atoms in R1 and R2, and the presence of any such non-hydrocarbon substituents and heteroatoms must be considered in applying the aforementioned molecular weight limitations. Representative R1 and R2 aliphatic, alicyclic and aryl hydrocarbon radicals in the general formula R1C(O)R2 include methyl, ethyl, propyl, isopropyl, butyl, isobutyl, sec-butyl, tert-butyl, pentyl, isopentyl, neopentyl, tert-pentyl, cyclopentyl, cyclohexyl, heptyl, octyl, nonyl, decyl, undecyl, dodecyl and their configurational isomers, as well as phenyl, benzyl, cumenyl, mesityl, tolyl, xylyl and phenethyl.

Representative ketone compatibilizers include but are not limited to: 2-butanone, 2-pentanone, acetophenone, butyrophenone, hexanophenone, cyclohexanone, cycloheptanone, 2-heptanone, 3-heptanone, 5-methyl-2-hexanone, 2-octanone, 3-octanone, diisobutyl ketone, 4-ethylcyclohexanone, 2-nonanone, 5-nonanone, 2-decanone, 4-decanone, 2-decalone, 2-tridecanone, dihexyl ketone and dicyclohexyl ketone.

Nitrile compatibilizers of the present invention comprise nitriles represented by the formula R1CN, wherein R1 is selected from aliphatic, alicyclic or aryl hydrocarbon radicals having from 5 to 12 carbon atoms, and wherein said nitriles have a molecular weight of from about 90 to about 200 atomic mass units. R1 in said nitrile compatibilizers is preferably selected from aliphatic and alicyclic hydrocarbon radicals having 8 to 10 carbon atoms. The molecular weight of said nitrile compatibilizers is preferably from about 120 to about 140 atomic mass units. R1 may optionally include substituted hydrocarbon radicals, that is, radicals containing non-hydrocarbon substituents selected from halogens (e.g., fluorine, chlorine) and alkoxides (e.g. methoxy). R1 may optionally include heteroatom-substituted hydrocarbon radicals, that is, radicals, which contain the atoms nitrogen (aza-), oxygen (keto-, oxa-) or sulfur (thia-) in a radical chain otherwise composed of carbon atoms. In general, no more than three non-hydrocarbon substituents and heteroatoms, and preferably no more than one, will be present for each 10 carbon atoms in R1, and the presence of any such non-hydrocarbon substituents and heteroatoms must be considered in applying the aforementioned molecular weight limitations. Representative R1 aliphatic, alicyclic and aryl hydrocarbon radicals in the general formula R1CN include pentyl, isopentyl, neopentyl, tert-pentyl, cyclopentyl, cyclohexyl, heptyl, octyl, nonyl, decyl, undecyl, dodecyl and their configurational isomers, as well as phenyl, benzyl, cumenyl, mesityl, tolyl, xylyl and phenethyl.

Representative nitrile compatibilizers include but are not limited to: 1-cyanopentane, 2,2-dimethyl-4-cyanopentane, 1-cyanohexane, 1-cyanoheptane, 1-cyanooctane, 2-cyanooctane, 1-cyanononane, 1-cyanodecane, 2-cyanodecane, 1-cyanoundecane and 1-cyanododecane.

Chlorocarbon compatibilizers of the present invention comprise chlorocarbons represented by the formula RClx, wherein; x is selected from the integers 1 or 2; R is selected from aliphatic and alicyclic hydrocarbon radicals having 1 to 12 carbon atoms; and wherein said chlorocarbons have a molecular weight of from about 100 to about 200 atomic mass units. The molecular weight of said chlorocarbon compatibilizers is preferably from about 120 to 150 atomic mass units. Representative R aliphatic and alicyclic hydrocarbon radicals in the general formula RClx include methyl, ethyl, propyl, isopropyl, butyl, isobutyl, sec-butyl, tert-butyl, pentyl, isopentyl, neopentyl, tert-pentyl, cyclopentyl, cyclohexyl, heptyl, octyl, nonyl, decyl, undecyl, dodecyl and their configurational isomers.

Representative chlorocarbon compatibilizers include but are not limited to: 3-(chloromethyl)pentane, 3-chloro-3-methylpentane, 1-chlorohexane, 1,6-dichlorohexane, 1-chloroheptane, 1-chlorooctane, 1-chlorononane, 1-chlorodecane, and 1,1,1-trichlorodecane.

Ester compatibilizers of the present invention comprise esters represented by the general formula R1CO2R2, wherein R1 and R2 are independently selected from linear and cyclic, saturated and unsaturated, alkyl and aryl radicals. Preferred esters consist essentially of the elements C, H and O, have a molecular weight of from about 80 to about 550 atomic mass units.

Representative esters include but are not limited to: (CH3)2CHCH2OOC(CH2)2-4OCOCH2CH(CH3)2 (diisobutyl dibasic ester), ethyl hexanoate, ethyl heptanoate, n-butyl propionate, n-propyl propionate, ethyl benzoate, di-n-propyl phthalate, benzoic acid ethoxyethyl ester, dipropyl carbonate, “Exxate 700” (a commercial C7 alkyl acetate), “Exxate 800” (a commercial C8 alkyl acetate), dibutyl phthalate, and tert-butyl acetate.

Lactone compatibilizers of the present invention comprise lactones represented by structures [A], [B], and [C]:

These lactones contain the functional group —CO2— in a ring of six (A), or preferably five atoms (B), wherein for structures [A] and [B], R1 through R8 are independently selected from hydrogen or linear, branched, cyclic, bicyclic, saturated and unsaturated hydrocarbyl radicals. Each R1 though R8 may be connected forming a ring with another R1 through R8. The lactone may have an exocyclic alkylidene group as in structure [C], wherein R1 through R6 are independently selected from hydrogen or linear, branched, cyclic, bicyclic, saturated and unsaturated hydrocarbyl radicals. Each R1 though R6 may be connected forming a ring with another R1 through R6. The lactone compatibilizers have a molecular weight range of from about 100 to about 300 atomic mass units, preferred from about 100 to about 200 atomic mass units.

Representative lactone compatibilizers include but are not limited to the compounds listed in Table 8.

TABLE 8 Molecular Molecular Weight Additive Molecular Structure Formula (amu) (E,Z)-3-ethylidene-5- methyl-dihydro-furan-2- one C7H10O2 126 (E,Z)-3-propylidene-5- methyl-dihydro-furan-2- one C8H12O2 140 (E,Z)-3-butylidene-5- methyl-dihydro-furan-2- one C9H14O2 154 (E,Z)-3-pentylidene-5- methyl-dihydro-furan-2- one C10H16O2 168 (E,Z)-3-Hexylidene-5- methyl-dihydro-furan-2- one C11H18O2 182 (E,Z)-3-Heptylidene-5- methyl-dihydro-furan-2- one C12H20O2 196 (E,Z)-3-octylidene-5- methyl-dihydro-furan-2- one C13H22O2 210 (E,Z)-3-nonylidene-5- methyl-dihydro-furan-2- one C14H24O2 224 (E,Z)-3-decylidene-5- methyl-dihydro-furan-2- one C15H26O2 238 (E,Z)-3-(3,5,5- trimethylhexylidene)-5- methyl-dihydrofuran-2- one C14H24O2 224 (E,Z)-3- cyclohexylmethylidene- 5-methyl-dihydrofuran- 2-one C12H18O2 194 gamma-octalactone C8H14O2 142 gamma-nonalactone C9H16O2 156 gamma-decalactone C10H18O2 170 gamma-undecalactone C11H20O2 184 gamma-dodecalactone C12H22O2 198 3-hexyldihydro-furan-2- one C10H18O2 170 3-heptyldihydro-furan- 2-one C11H20O2 184 cis-3-ethyl-5-methyl- dihydro-furan-2-one C7H12O2 128 cis-(3-propyl-5-methyl)- dihydro-furan-2-one C8H14O2 142 cis-(3-butyl-5-methyl)- dihydro-furan-2-one C9H16O2 156 cis-(3-pentyl-5-methyl)- dihydro-furan-2-one C10H18O2 170 cis-3-hexyl-5-methyl- dihydro-furan-2-one C11H20O2 184 cis-3-heptyl-5-methyl- dihydro-furan-2-one C12H22O2 198 cis-3-octyl-5-methyl- dihydro-furan-2-one C13H24O2 212 cis-3-(3,5,5- trimethylhexyl)-5- methyl-dihydro-furan-2- one C14H26O2 226 cis-3-cyclohexylmethyl- 5-methyl-dihydro-furan- 2-one C12H20O2 196 5-methyl-5-hexyl- dihydro-furan-2-one C11H20O2 184 5-methyl-5-octyl- dihydro-furan-2-one C13H24O2 212 Hexahydro- isobenzofuran-1-one C8H12O2 140 delta-decalactone C10H18O2 170 delta-undecalactone C11H20O2 184 delta-dodecalactone C12H22O2 198 mixture of 4-hexyl- dihydrofuran-2-one and 3-hexyl-dihydro-furan- 2-one C10H18O2 170

Lactone compatibilizers generally have a kinematic viscosity of less than about 7 centistokes at 40° C. For instance, gamma-undecalactone has kinematic viscosity of 5.4 centistokes and cis-(3-hexyl-5-methyl)dihydrofuran-2-one has viscosity of 4.5 centistokes both at 40° C. Lactone compatibilizers may be available commercially or prepared by methods as described in U.S. patent application Ser. No. 10/910,495 filed Aug. 3, 2004, incorporated herein by reference.

Aryl ether compatibilizers of the present invention further comprise aryl ethers represented by the formula R1OR2, wherein: R1 is selected from aryl hydrocarbon radicals having from 6 to 12 carbon atoms; R2 is selected from aliphatic hydrocarbon radicals having from 1 to 4 carbon atoms; and wherein said aryl ethers have a molecular weight of from about 100 to about 150 atomic mass units. Representative R1 aryl radicals in the general formula R1OR2 include phenyl, biphenyl, cumenyl, mesityl, tolyl, xylyl, naphthyl and pyridyl. Representative R2 aliphatic hydrocarbon radicals in the general formula R1OR2 include methyl, ethyl, propyl, isopropyl, butyl, isobutyl, sec-butyl and tert-butyl. Representative aromatic ether compatibilizers include but are not limited to: methyl phenyl ether (anisole), 1,3-dimethyoxybenzene, ethyl phenyl ether and butyl phenyl ether.

Fluoroether compatibilizers of the present invention comprise those represented by the general formula R1OCF2CF2H, wherein R1 is selected from aliphatic, alicyclic, and aromatic hydrocarbon radicals having from about 5 to about 15 carbon atoms, preferably primary, linear, saturated, alkyl radicals. Representative fluoroether compatibilizers include but are not limited to: C8H17OCF2CF2H and C6H13OCF2CF2H. It should be noted that if the refrigerant is a fluoroether, then the compatibilizer may not be the same fluoroether.

Fluoroether compatibilizers may further comprise ethers derived from fluoroolefins and polyols. The fluoroolefins may be of the type CF2═CXY, wherein X is hydrogen, chlorine or fluorine, and Y is chlorine, fluorine, CF3 or ORf, wherein Rf is CF3, C2F5, or C3F7. Representative fluoroolefins are tetrafluoroethylene, chlorotrifluoroethylene, hexafluoropropylene, and perfluoromethylvinyl ether. The polyols may be linear or branched. Linear polyols may be of the type HOCH2(CHOH)x(CRR′)yCH2OH, wherein R and R′ are hydrogen, or CH3, or C2H5 and wherein x is an integer from 0-4, and y is an integer from 0-4. Branched polyols may be of the type C(OH)t(R)u(CH2OH)v[(CH2)mCH2OH]w, wherein R may be hydrogen, CH3 or C2H5, m may be an integer from 0 to 3, t and u may be 0 or 1, v and w are integers from 0 to 4, and also wherein t+u+v+w=4. Representative polyols are trimethylol propane, pentaerythritol, butanediol, and ethylene glycol.

1,1,1-trifluoroalkane compatibilizers of the present invention comprise 1,1,1-trifluoroalkanes represented by the general formula CF3R1, wherein R1 is selected from aliphatic and alicyclic hydrocarbon radicals having from about 5 to about 15 carbon atoms, preferably primary, linear, saturated, alkyl radicals. Representative 1,1,1-trifluoroalkane compatibilizers include but are not limited to: 1,1,1-trifluorohexane and 1,1,1-trifluorododecane.

By effective amount of compatibilizer is meant that amount of compatibilizer that leads to efficient solubilizing of the lubricant in the composition and thus provides adequate oil return to optimize operation of the refrigeration, air-conditioning or heat pump apparatus.

The compositions of the present invention will typically contain from 0.1 to about 40 weight percent, preferably from about 0.2 to about 20 weight percent, and most preferably from about 0.3 to about 10 weight percent compatibilizer in the compositions of the present invention.

The heat transfer fluid of the present invention may be solubilized in a refrigeration lubricant selected from the group consisting of mineral oils, alkylbenzenes, synthetic paraffins, synthetic napthenes, and poly(alpha)olefins, wherein said method comprises contacting said lubricant with said composition in the presence of an effective amount of a compatibilizer, wherein said compatibilizer is selected from the group consisting of polyoxyalkylene glycol ethers, amides, nitriles, ketones, chlorocarbons, esters, lactones, aryl ethers, fluoroethers and 1,1,1-trifluoroalkanes.

The compositions of the present invention may further comprise an ultra-violet (UV) dye and optionally a solubilizing agent. The UV dye is a useful component for detecting leaks of the composition by permitting one to observe the fluorescence of the dye in the composition at a leak point or in the vicinity of refrigeration, air-conditioning, or heat pump apparatus. One may observe the fluoroscence of the dye under an ultra-violet light. Solubilizing agents may be needed due to poor solubility of such UV dyes in some compositions.

By “ultra-violet” dye is meant a UV fluorescent composition that absorbs light in the ultra-violet or “near” ultra-violet region of the electromagnetic spectrum. The fluorescence produced by the UV fluorescent dye under illumination by a UV light that emits radiation with wavelength anywhere from 10 nanometer to 750 nanometer may be detected. Therefore, if a composition containing such a UV fluorescent dye is leaking from a given point in a refrigeration, air-conditioning, or heat pump apparatus, the fluorescence can be detected at the leak point. Such UV fluorescent dyes include but are not limited to naphthalimides, perylenes, coumarins, anthracenes, phenanthracenes, xanthenes, thioxanthenes, naphthoxanthenes, fluoresceins, and derivatives or combinations thereof.

Solubilizing agents of the present invention comprise at least one compound selected from the group consisting of hydrocarbons, hydrocarbon ethers, dimethylether, polyoxyalkylene glycol ethers, amides, nitriles, ketones, chlorocarbons, esters, lactones, aryl ethers, fluoroethers and 1,1,1-trifluoroalkanes. The polyoxyalkylene glycol ethers, amides, nitriles, ketones, chlorocarbons, esters, lactones, aryl ethers, fluoroethers and 1,1,1-trifluoroalkanes solubilizing agents have been defined previously herein as being compatibilizers for use with conventional refrigeration lubricants.

Hydrocarbon solubilizing agents of the present invention comprise hydrocarbons including straight chained, branched chain or cyclic alkanes or alkenes containing 5 or fewer carbon atoms and only hydrogen with no other functional groups. Representative hydrocarbon solubilizing agents comprise propane, propylene, cyclopropane, n-butane, isobutane, 2-methylbutane and n-pentane. It should be noted that if the composition contains a hydrocarbon, then the solubilizing agent may not be the same hydrocarbon.

Hydrocarbon ether solubilizing agents of the present invention comprise ethers containing only carbon, hydrogen and oxygen, such as dimethyl ether (DME).

Solubilizing agents of the present invention may be present as a single compound, or may be present as a mixture of more than one solubilizing agent. Mixtures of solubilizing agents may contain two solubilizing agents from the same class of compounds, say two lactones, or two solubilizing agents from two different classes, such as a lactone and a polyoxyalkylene glycol ether.

In the present compositions comprising refrigerant and UV fluorescent dye, or comprising heat transfer fluid and UV fluorescent dye, from about 0.001 weight percent to about 1.0 weight percent of the composition is UV dye, preferably from about 0.005 weight percent to about 0.5 weight percent, and most preferably from 0.01 weight percent to about 0.25 weight percent.

Solubilizing agents such as ketones may have an objectionable odor, which can be masked by addition of an odor masking agent or fragrance. Typical examples of odor masking agents or fragrances may include Evergreen, Fresh Lemon, Cherry, Cinnamon, Peppermint, Floral or Orange Peel all commercially available, as well as d-limonene and pinene. Such odor masking agents may be used at concentrations of from about 0.001% to as much as about 15% by weight based on the combined weight of odor masking agent and solubilizing agent.

Solubility of these UV fluorescent dyes in the compositions of the present invention may be poor. Therefore, methods for introducing these dyes into the refrigeration, air-conditioning, or heat pump apparatus have been awkward, costly and time consuming. U.S. Pat. No. RE 36,951 describes a method, which utilizes a dye powder, solid pellet or slurry of dye that may be inserted into a component of the refrigeration, air-conditioning, or heat pump apparatus. As refrigerant and lubricant are circulated through the apparatus, the dye is dissolved or dispersed and carried throughout the apparatus. Numerous other methods for introducing dye into a refrigeration or air conditioning apparatus are described in the literature.

Ideally, the UV fluorescent dye could be dissolved in the refrigerant itself thereby not requiring any specialized method for introduction to the refrigeration, air conditioning apparatus, or heat pump. The present invention relates to compositions including UV fluorescent dye, which may be introduced into the system as a solution in the refrigerant. The inventive compositions will allow the storage and transport of dye-containing compositions even at low temperatures while maintaining the dye in solution.

In the present compositions comprising refrigerant, UV fluorescent dye and solubilizing agent, or comprising heat transfer fluid and UV fluorescent dye and solubilizing agent, from about 1 to about 50 weight percent, preferably from about 2 to about 25 weight percent, and most preferably from about 5 to about 15 weight percent of the combined composition is solubilizing agent. In the compositions of the present invention the UV fluorescent dye is present in a concentration from about 0.001 weight percent to about 1.0 weight percent, preferably from 0.005 weight percent to about 0.5 weight percent, and most preferably from 0.01 weight percent to about 0.25 weight percent.

EXAMPLES Example 1

A hose is constructed according to one embodiment of the invention in the following manner. A mandrel is first made in the form of a solid rod with a diameter of 6.4 mm. A veneer consisting of an inner layer of 0.65 mm thick Zytel® 42 (a high MWA 66 commercially available from E.I. du Pont de Nemours and Company) and 0.1 mm thick outer tie layer of Bynel® 4206 (a maleic anhydride grafted polyethylene commercially available from E.I. du Pont de Nemours and Company) is extruded over the mandrel. The assembly is then laminated with a metal-polymer laminate available as BFW 46 and obtained from James Dawson Enterprises Ltd of Lachine, Quebec, Canada. The laminate consists of an inner layer of low density polyethylene, a tie layer of EEA, an aluminum foil (10 micron thick) and an outer layer of polyethylene terephthalate (PET) with a total thickness of 0.1 mm. Lamination is carried out using a heated die with a passage way of appropriate size to pass the assembly through. The assembly of the previous step is uncoiled from a spool and a strip of metal-polymer laminate is wrapped around it such that two long edges of the strip mat against each other. The assembly is passed through the die heated to 140 C to affect the bonding. Excess laminate edge is trimmed off carefully so as not to damage the seal and avoid exposing underlying layer. A layer of TPV is extruded over the assembly. Following that, a braid of PET filaments is applied, and outer protective layer of ETPV is extruded over the top. The mandrel is subsequently extracted to prepare the multi-layer hose.

Example 2

Samples of hoses as described Example 1 were tested for hose permeation following the procedure outlined in Standard SAE J2064. Lengths of hose were cut and fitted at the ends to contain refrigerant. Hoses were charged with refrigerant to 70% by volume. Hoses were then placed in an oven and held at 80 C for 28 days. Hoses were periodically removed and weighed to determine refrigerant loss. An overall loss or permeation rate was then determined in kg/m2/yr. Results are shown in Table 9.

TABLE 9 Hose Permeation Rate Refrigerant Composition (kg/m2/yr) R134a 0.44 1225ye/R32 (95/5 wt %) 0.45 1225ye/1234yf/134a (45/45/10 wt %) 0.07

Results show hoses permeation for fluoroolefin compositions are at least equivalent to R134a. Since R32 is a small molecule, it contributes the most to hose permeation. The composition containing primarily fluoroolefins and a small amount of R134a had significantly lower permeation than R134a alone indicating, indicating fluoroolefins have overall lower permeation rates.

Claims

1. A method of providing transport of a heat transfer fluid composition within a refrigeration or air conditioning system, comprising circulating a heat transfer fluid through one or more hoses of said system, wherein said heat transfer fluid composition comprises a compound selected from the group consisting of: R32, R152a, CF3I, 1234yf, 1225ye and trans-1234ze.

2. The method of claim 1, wherein the method comprises the steps of circulating the heat transfer fluid composition from a hose connected between the outlet of a compressor and the inlet of a condenser.

3. The method of claim 2, further comprising the step of circulating the heat transfer fluid composition through a hose connected between an outlet of the condenser and an inlet of an evaporator.

4. The method of claim 3, further comprising the step of circulating the heat transfer fluid composition through a hose connected between an outlet of the evaporator and an inlet of the compressor.

5. The method of claim 3, wherein the hose comprises an outer layer comprising a material selected from the group consisting of an elastomer and a polyamide and an inner layer comprising a material selected from the group consisting of an elastomer, a polyamide and a thermoplastic.

6. The method of claim 5, wherein the inner layer comprises a thermoplastic veneer and the outer layer comprises an elastomer.

7. The method of claim 6, further including:

(a) a tie layer positioned over said inner layer;
(b) a metal-polymer laminate positioned over said tie layer and consisting of a layer of polymer compatible with or bondable to said outer surface of said veneer, a thin layer of metallic foil, and another layer of a polymer protecting the metallic foil;
(c) a braid under-layer positioned over said metal-polymer laminate and consisting of an elastomeric material; and
(d) a reinforcing braid layer positioned over said braid under-layer, wherein the outer layer is positioned on the outside of the reinforcing braid layer.

8. The method of claim 7, further comprising one or more additional reinforcing braid layers (d) and/or one or more additional outer layers.

9. The method of claim 1, wherein the heat transfer fluid composition comprises HFC-1225ye and at least one additional compound selected from the group consisting of HFC-1234ze, HFC-1234yf, HFC-1234ye, HFC-1243zf, HFC-32, HFC-125, HFC-134, HFC-134a, HFC-143a, HFC-152a, HFC-161, HFC-227ea, HFC-236ea, HFC-236fa, HFC-245fa, HFC-365mfc, propane, n-butane, isobutane, 2-methylbutane, n-pentane, cyclopentane, dimethylether, CF3SCF3, CO2, NH3, and CF3I.

10. The method of claim 1, wherein the heat transfer fluid composition comprises HFC-1234ze and at least one additional compound selected from the group consisting of HFC-1234yf, HFC-1234ye, HFC-1243zf, HFC-32, HFC-125, HFC-134, HFC-134a, HFC-143a, HFC-152a, HFC-161, HFC-227ea, HFC-236ea, HFC-236fa, HFC-245fa, HFC-365mfc, propane, n-butane, isobutane, 2-methylbutane, n-pentane, cyclopentane, dimethylether, CF3SCF3, CO2 and CF3I.

11. The method of claim 1, wherein the heat transfer fluid composition comprises HFC-1234yf and at least one additional compound selected from the group consisting of HFC-1234ye, HFC-1243zf, HFC-32, HFC-125, HFC-134, HFC-134a, HFC-143a, HFC-152a, HFC-161, HFC-227ea, HFC-236ea, HFC-236fa, HFC-245fa, HFC-365mfc, propane, n-butane, isobutane, 2-methylbutane, n-pentane, cyclopentane, dimethylether, CF3SCF3, CO2, NH3, and CF3I.

12. The method of claim 1, wherein the heat transfer fluid composition comprises HFC-1243zf and at least one additional compound selected from the group consisting of HFC-1234ye, HFC-32, HFC-125, HFC-134, HFC-134a, HFC-143a, HFC-152a, HFC-161, HFC-227ea, HFC-236ea, HFC-236fa, HFC-245fa, HFC-365mfc, propane, n-butane, isobutane, 2-methylbutane, n-pentane, cyclopentane, dimethylether, CF3SCF3, CO2 and CF3I.

13. The method of claim 1, wherein the heat transfer fluid composition comprises HFC-1234ye and at least one additional compound selected from the group consisting of HFC-1243zf, HFC-32, HFC-125, HFC-134, HFC-134a, HFC-143a, HFC-152a, HFC-161, HFC-227ea, HFC-236ea, HFC-236fa, HFC-245fa, HFC-365mfc, propane, n-butane, isobutane, 2-methylbutane, n-pentane, cyclopentane, dimethylether, CF3SCF3, CO2 and CF3I.

Patent History
Publication number: 20090314015
Type: Application
Filed: Aug 31, 2007
Publication Date: Dec 24, 2009
Applicant: E. I. DU PONT DE NEMOURS AND COMPANY (Wilmington, DE)
Inventors: Barbara Haviland Minor (Elkton, MD), Donald Bernard Bivens (Kennett Square, PA), Shailesh Ratilal Doshi (Kingston), Velliyur Nott Mallikarjuna Rao (Wilmington, DE), Enrico Simonato (Torino)
Application Number: 12/377,686
Classifications
Current U.S. Class: Compressing, Condensing And Evaporating (62/115)
International Classification: F25B 1/00 (20060101);