AZEOTROPIC COMPOSITION OF 1,1,1,2-TETRAFLUOROETHANE AND DIMETHYL ETHER

Abstract: The azeotrope of 1,1,1,2-tetrafluoroethane and dimethyl ether and its use as a refrigerant, aerosol propellant and polymer foam blowing agent are disclosed.

Description: AZEOTROPIC COMPOSITION OF 1,1,1,2-TETRAFLUOROETHANE AND DIMETHYL ETHER Background of the Invention This invention relates to mixtures of 1,1,1,2- tetrafluoroethane (HFC-134a) and dimethyl ether (DME) . Such mixtures are useful as refrigerants, heat transfer media, gaseous dielectrics, foam expansion agents, aerosol propellants and power cycle working fluids. These mixtures are potentially environmentally safe substitutes for dichlorodifluoromethane (CFC-12) , which is a large volume commercial refrigerant. Closed-cell polyurethane foams are widely used for insulation purposes in building construction and in the manufacture of energy efficient electrical appliances. In the construction industry, polyurethane (polyiso- cyanurate) board stock is used in roofing and siding for its insulation and load-carrying capabilities. Poured and sprayed polyurethane foams are also used in construction. Sprayed polyurethane foams are widely used for insulating large structures such as storage tanks, etc. Pour-in-place polyurethane foams are used, for example, in appliances such as refrigerators and freezers plus they are used in making refrigerated trucks and railcars. All of these various types of polyurethane foams require expansion agents (blowing agents) for their manufacture. Insulating foams depend on the use of halocarbon blowing agents, not only to foam the poly¬ mer, but primarily for their low vapor thermal conductivity, a very important characteristic for insulation value. Historically, polyurethane foams are made with CFC-11 (CFCl ) as the primary blowing agent. A second important type of insulating foam is phenolic foam. These foams, which have very attractive flammability characteristics, are generally made with CFC-11 and CFC-113 (1,1,2-trichloro-l,2,2-trifluoro- ethane) blowing agents. A third type of insulating foam is thermoplastic foam, primarily polystyrene foam. Polyolefin foams (polyethylene and polypropylene) are widely used in packaging. These thermoplastic foams are generally made with CFC-12. Many refrigeration applications, e.g., refrigera- tors and auto air conditioners presently use CFC-12 as the refrigerant. HFC-134a is a fluorocarbon compound identified as a potential replacement for CFC-12, having properties near those of CFC-12, and being nonflammable with a zero ozone depletion potential. However, HFC-134a has a lower refrigeration coefficient of performance than that of CFC-12, which can result in increased energy consumption for refrigeration applica¬ tions if HFC-134a is substituted for CFC-12. Many products designed for household, personal or industrial use are available as aerosol products. Typical examples of such products and ones in which the propellant system of the present invention can be used include personal products such as hair sprays, deodor¬ ants and colognes; household products such as waxes, polishes, pan sprays, room fresheners and household insecticides; industrial products such as cleaners, lubricants, and mold release agents; and automotive products such as cleaners and polishes. All such products utilize the pressure of a propellant gas or a mixture of propellant gases (i.e., a propellant gas system) to expel the active ingredients from the container. For this purpose, most aerosols employ liquified gases which vaporize and provide the pressure to propel the active ingredients when the valve on the aerosol container is pressed open. An important physical property associated with the dispensing of aerosol products is the vapor pressure of the propellant. Vapor pressure from the viewpoint of this invention is the pressure exerted when a liquified propellant gas is in equilibrium with its vapor in a closed container, such as an aerosol can. Vapor pressure can be measured by connecting a pressure gauge to the valve on an aerosol can or gas cylinder contain¬ ing the vapor/liquid mixture. A standard of measure¬ ment of vapor pressure in the U.S. aerosol industry is pounds per square inch gauge (psig) with the gas/liquid mixture at constant temperature, most commonly at 70 β F (21 β C) . The vapor pressures of liquified gases most widely employed as aerosol propellants will vary over the range of about 20 to 90 psig (138 to 621 kPa) at 70"F (21 β ). The propellant systems of the present invention have vapor pressures in this range. In the early 1970's, concern began to be expressed that the stratospheric ozone layer (which provides protection against penetration of the earth's atmosphere by ultraviolet radiation) was being depleted by chlorine atoms introduced to the atmosphere from the release of fully halogenated chlorofluorocarbons. These chlorofluorocarbons are used as propellants in aerosols, as blowing agents for foams, as refrigerants and as cleaning/drying solvent systems. Because of the great chemical stability of fully halogenated chloro¬ fluorocarbons, according to the ozone depletion theory, these compounds do not decompose in the earth's atmosphere but reach the stratosphere where they slowly degrade liberating chlorine atoms which in turn react with the ozone. Concern reached such a level that in 1978 the U.S. Environmental Protection Agency (EPA) placed a ban on nonessential uses of fully halogenated chlorofluoro¬ carbons as aerosol propellants. This ban resulted in a dramatic shift in the U.S. away from chlorofluorocarbon propellants (except for exempted uses) to primarily hydrocarbon propellants. However, since the rest of the world did not join the U.S. in this aerosol ban, the net result has been to shift the uses of chloro¬ fluorocarbons in aerosols out of the U.S., but not to permanently reduce the world-wide total chlorofluoro- carbon production, as sought. In fact, in the last few years the total amount of chlorofluorocarbons manufac¬ tured worldwide has exceeded the level produced in 1978 (before the U.S. ban) . During the period of 1978-1987, much research was conducted to study the ozone depletion theory. Because of the complexity of atmospheric chemistry, many questions relating to this theory remained unanswered. However, assuming the theory to be valid, the health risks which would result from depletion of the ozone layer are significant. This, coupled with the fact that world-wide production of chlorofluorocarbons has increased, has resulted in international efforts to reduce chlorofluorocarbon use. Particularly, in September, 1987, the United Nations through its Envi- ronment Programme (UNEP) issued a tentative proposal calling for a 50 percent reduction in world-wide production of fully halogenated chlorofluorocarbons by the year 1998. This proposal was ratified January 1, 1989 and became effective on July 1, 1989. Because of this proposed reduction in availability of fully halogenated chJerofluorocarbons such as CFC-11, CFC-12 and CFC-113, alternative, more environ¬ mentally acceptable, products are urgently needed. As early as the 1970's with the initial emergence of the ozone depletion theory, it was known that the introduction of hydrogen into previously fully halo¬ genated chlorofluorocarbons markedly reduced the chemical stability of these compounds. Hence, these now destabilized compounds would be expected to degrade in the atmosphere and not reach the stratosphere and the ozone layer. The accompanying Table lists the ozone depletion potential for a variety of fully and partially halogenated halocarbons. Halocarbon Global Warming Potential data (potential for reflecting infrared radiation (heat) back to earth and thereby raising the earth's surface temperature) are also shown. OZONE DEPLETION AND HALOCARBON GLOBAL WARMING POTENTIALS Halocarbon Global Ozone Depletion Warming Blowing Agent Potential Potential CFC-11 (CFC1 3 ) 1.0 1.0 CFC-12 (CF 2 C1 2 ) 1.0 2.8 HCFC-22 (CHF 2 C1) 0.05 0.3 HCFC-123 (CF 3 CHC1 2 ) 0.02 0.02 HCFC-124 (CF 3 CHFC1) 0.02 0.09 HFC-134a (CF 3 CH 2 F) 0 0.3 HCFC-141b (CFC1 CH ) 0.1 0.09 HCFC-142b (CF 2 C1CH 3 ) 0.06 0.3 HFC-152a (CHF 2 CH 3 ) 0 0.03 CFC-113 (CF 2 C1-CFC1 2 ) 0.8-0 .9 1.4 Halocarbons such as HFC-134a have zero ozone depletion potential. Dimethyl ether, having no halogen content, is also a zero czone depleter. Although 1,1,1,2-tetrafluoroethane has utility as a refrigerant, aerosol propellant or foam blowing agent, an azeotrope offers the possibility of producing more economical nonfractionating systems with improved properties such as polymer and refrigerant oil solubil¬ ity. Unfortunately, as recognized in the art, it is not possible to predict the formation of azeotropes. This fact obviously complicates the search for new azeotropes which have application in the field. Nevertheless, there is a constant effort in the art to discover new azeotropic compositions, which have desirable characteristics. Summary of the Invention In accordance with the present invention, azeo- tropic and other mixtures have been discovered, which consist essentially of 1,1,1,2-tetrafluoroethane (HFC-134a) and dimethyl ether (DME) . Included among the invention mixtures is an azeotrope with the compo¬ sition 50 weight percent HFC-134a and 50 weight percent DME at 22 β C (± 5 weight percent). Therefore, one azeotropic composition of the invention consists essentially of about 45-55 weight percent of 1,1,1,2- tetrafluoroethane and 55-45 weight percent of DME, at 22 β C. For the purpose of this discussion, azeotropic or constant boiling is intended to mean also essentially azeotropic or essentially constant boiling. In other words, included within the meaning of these terms are not only the true azeotrope described above, but also other compositions containing the same components in different proportions, which are true azeotropes at other temperatures and pressures, as well as those equivalent compositions which are part of the same azeotropic system and are azeotrope-like in their properties. As is well recognized in this art, there is a range of compositions which contain the same components as the azeotrope, which not only will exhibit essentially equivalent properties for refrig¬ eration and other applications, but which will also exhibit essentially equivalent properties to the true azeotropic composition in terms of constant boiling characteristics or tendency not to separate or frac¬ tionate on boiling. The azeotropic compositions of the invention are useful as refrigerants, expansion agents and as aerosol propellants, among other applications. They have zero ozone depletion potential opposite CFC-12, which is rated at 1.0. They are especially suitable as refrig¬ erants in that they exhibit vapor pressures near that of CFC-12, a commercial refrigerant, and have energy efficiency performance better than that of HFC-134a alone. Mixtures of HFC-l34a and DME may be formulated such that they are nonflammable. Therefore, also included among the compositions of this invention are nonflammable compositions containing 0.5 to 9.0 weight percent DME and 91.0 to 99.5 weight percent HFC-134a. Another aspect of the invention is a refrigeration method which comprises condensing a refrigerant composition of the invention (40.0-99.5 wt. % HFC-134a and 0.5-60.0 wt. % DME) and thereafter evaporating it in the vicinity of a body to be cooled. Similarly, still another aspect of the invention is a method for heating which comprises condensing the invention refrigerant in the vicinity of a body to be heated and thereafter evaporating the refrigerant. Preferably in the heating and cooling applica¬ tions, the nonflammable compositions will contain at least about 91.0 weight percent HFC-134a. These azeotropic compositions are useful as propellants for aerosol sprays, e.g. room fresheners. The azeotropes are particularly attractive as they do not separate or fractionate when used in aerosol packages equipped with vapor tap valves wherein the propellant is removed, at least partially, vapor phase. The invention therefore includes aerosol compositions comprising an active agent and an azeotropic composi¬ tion of the invention, and processes making such compositions by admixing said ingredients. The HFC-134a/DME azeotropic and constant boiling azeotrope-like compositions are excellent polymer blowing agents. The dimethyl ether component unex- g pectedly solubilizes the poorly soluble HFC-134a in polyurethane, phenolic and polystyrene foam, resulting in excellent insulating foams. Once solubilized in the foam, the HFC-134a insulating gas does not diffuse out of the foam. - 0 The novel azeotropic composition of the invention was discovered during a phase study wherein the compo¬ sitions were varied and vapor pressures measured. The azeotropic composition occurred at the minimum point of the vapor pressure-concentration plot, being at 50 15 weight percent HFC-134a and 50 weight percent DME at 22°C (± 5 weight percent). The azeotrope has an atmospheric pressure boiling point of -22.7"C, com¬ pared with -26.5*C for HFC-134a and -24.6 β C for DME. The language // an azeotropic composition consisting 2 0 essentially of..." is intended to include mixtures which contain all the components of the azeotrope of this invention (in any amounts) and which, when fractionally distilled, would produce an azeotrope containing all the components of this invention in at 25 least one fraction, alone or in combination with another compound, e.g. , one which distills at substantially the same temperature as said fraction. The nonflammable mixtures of this invention consist essentially of effective amounts of HFC-134a 30 and DME within the range of about 91.0 to 99.5 weight percent of HFC-134a and 0.5 to 9.0 weight percent of DME. More usually, for purposes of the invention, the mixtures will contain from about 40.0 to 99.5 weight percent of HFC-134a, the remainder being DME. 35 The compositions of this invention have vapor pressures and refrigeration energy efficiency values near that of CFC-12, hence are useful as refrigerants in refrigeration processes. They also show zero ozone depletion potential and the amount of dimethyl ether can be chosen such that the composition is nonflam¬ mable. By vapor pressure substantially equal to the vapor pressure of dichloro-difluoromethane (CFC-12) is meant a vapor pressure which is within twenty percent of the vapor pressure of CFC-12 at the same temperature. The vapor pressure of CFC-12 is described in "Handbook of Chemistry and Physics", 50th Edition, page D-163. The binary refrigerant compositions of the inven¬ tion can be used in existing refrigeration equipment, e.g., designed to use CFC-12. They are useful in compression cycle applications including air condi¬ tioner and heat pump systems for producing both cooling and heating. The new refrigerant mixtures can be used in refrigeration applications such as described in U.S. Patent No. 4,482,465 to Gray. As stated above, the preferred binary 1,1,1,2- tetrafluoroethane/DME compositions are essentially nonflammable. By nonflammable is meant a gas mixture which in air will not burn when subjected to a spark igniter as described in "Limits of Flammability of Gases and Vapors", Bulletin 503, H. F. Coward, et.al., Washington, U.S. Bureau of Mines, 1952. The HFC-134a/dimethyl ether azeotrope of the invention has a vapor pressure at 70°F (21 β C) of about 58 psig (400 kPa) . This vapor pressure range makes the azeotrope attractive and useful as an aerosol propel¬ lant. The HFC-134a/dimethyl ether azeotrope has been determined to be a good solvent for polystyrene. Thus the azeotrope and, more particularly, the nonflammable mixtures of HFC-134a and dimethyl ether are excellent blowing agents for polystyrene and will make it pos¬ sible to solubilize HFC-134a in polystyrene. Additionally, the HFC-134a/dimethyl ether azeo¬ trope is soluble in polyurethane polyols; whereas, HFC-134a alone has quite poor solubility. The compositions of the instant invention can be prepared by any convenient method including mixing or combining, by other suitable methods, the desired amounts of the components, using techniques well-known to the art. Without further elaboration, it is believed that one skilled in the art can, using the preceding de¬ scription, utilize the present invention to its fullest extent. The following preferred specific embodiments are, therefore, to be construed as merely illustrative, and not limitative of the remainder of the disclosure in any way whatsoever. In the foregoing and in the following examples, all temperatures are set forth uncorrected in degrees Celsius and unless otherwise indicated, all parts and percentages are by weight. The entire disclosure of all applications, patents and publications, cited above and below, are hereby incorporated by reference. EXAMPLES Example 1 A phase study is made on 1,1,1,2-tetrafluoroethane and dimethyl ether wherein the composition is varied and the vapor pressures measured, at a temperature of 22 β C. An azeotropic composition is obtained as evi¬ denced by the minimum vapor pressure observed and is identified as 50.0 weight percent 1,1,1,2-tetrafluoro- ethane and 50.0 weight percent dimethyl ether. (+ 5 weight percent) . Example 2 An evaluation of the refrigeration properties of the mixtures of the invention versus dichlorodifluoro- methane (CFC-12) and 1,1,1,2-tetrafluoroethane (HFC-134a) , respectively, are shown in the following Table. The data are generated on a one ton basis, that is to say, on the removal of heat from a space at the rate of 12,000 Btu/hr (12.66 x 10 J/hr) . The data are based on the ideal refrigeration cycle. TABLE I COMPARISON OF REFRIGERATION PERFORMANCES elκht Percentages 46X HFC-134a 90X HFC-134a CFC-12 HFC-134a 54X DME 10J_ DME Evaporator Temp. , *F 35.0 35.0 35.0 35.0 CC) (1.67) (1.67) (1.67) (1.67) Evaporator pre "-(Eli! 47.2 45.1 39.7 42.3 (325) (311) (274) (292) Condenser Temp., 'F 150.0 150.0 150.0 150.0 (*c> (65.6) (65.6) (65.6) (65.6) Condenser Press., psla 249.5 274.9 239.6 261.4 (kPa) (1717) (1895) (1652) (1802) Superheat, *f . with Vapor-Llq. Heat Exchange 30.0 30.0 30.0 30.0 (- 1.1) (- 1.1) (- 1.1) (- 1.1) Coefficient of Performance 2.96 2.81 3.12 2.91 Compressor Displacement, 3 Ft. /mln/ton 4.44 4.55 4.56 4.61 Coefficient of Performance (COP) is a measure of refrigerant energy efficiency. For a refrigeration cycle typified by the above conditions, the COP of the (46/54) weight percent HFC-134a/DME composition represents a somewhat better performance than both dichlorodifluoromethane (CFC-12) , the industry refrigerant standard and HFC-134a (1,1,1,2-tetrafluoroethane) alone. This azeotropic mixture is flammable. The 90/10 weight percent HFC-134a/DME mixture has a COP of 2.91, which is near that of CFC-12 and is better than HFC-134a alone. Additives such as lubricants, corrosion inhibi¬ tors, stabilizers, dyes and other appropriate materials may be added to the novel compositions of the invention for a variety of purposes provided they do not have an adverse influence on the composition, for their in¬ tended applications. Example 3 An aerosol room freshener was prepared with the HFC-134a/dimethyl ether azeotrope. The formulation and vapor pressure are shown in Table II. TABLE II AEROSOL ROOM FRESHENER FORMULATION Ingredient Wt. % Perfume 2.0 HFC-134a/ 98.0 Dimet-iyl ether (46/54) Vapor Pressure 60.5 at 70 β F, psig (at 21°C, kPa) (417) Example 4 The solubility of the HFC-134a/dimethyl ether azeotrope is determined in a polyurethane polyol. The azeotrope is readily soluble at 30.0 weight percent; whereas, HFC-134a is insoluble. The solubility data are summarized in Table III. TABLE III SOLUBILITY OF HFC-134a/DIMETHYL ETHER AZEOTROPE IN POLYOL Blowing Wt. % Agent in Polyol Appearance HFC-134a 30.0 Insoluble, two phases HFC-134a/ Dimethyl ether 30.0 Soluble, single phase (46/54) * Stepanpol ® PS-2852 (Stepan Company) an aromatic polyester polyol. Example 5 The solubility of the HFC-134a/dimethyl ether azeotrope in polystyrene is determined by combining a piece of polystyrene (about 2.5 cm long, 0.5 cm wide and 0.5 cm thick) with about 50g. azeotrope. Whereas HFC-134a has essentially no solvency in polystyrene, the HFC-134a/dimethyl ether azeotrope softens and deforms the polystyrene. The data are summarized in Table IV. TABLE IV SOLUBILITY OF HFC-134a/DIMETHYL ETHER AZEOTROPE IN POLYSTYRENE Blowing Agent Appearance of Polystyrene HFC-134a No effect HFC-134a/Dimethyl Polystyrene softened and ether deformed* (46/54) * On removing the polystyrene from the azeotrope, expansion occurs from solubilized HFC-134a. Example 6 The quantity of HFC-134a required in the vapor space above blends of HFC-134a and dimethyl ether for nonflammability is determined. The test conditions and results are summarized in Table V. TABLE V NONFLAMMABLE BLEND OF HFC-134a/DIMETHYL ETHER Ignition Source: 3-mil copper exploding wire (110 Volts) Temperature: 80'C lSO'C Quantity of HFC-134a greater than greater than required for 91 wt. % 98 wt. % nonflammability* * In HFC-134a/dimethyl ether vapor mixtures in air. The preceding examples can be repeated with similar success by substituting the generically or specifically described reactants and/or operating conditions of this invention for those used in the preceding examples. From the foregoing description, one skilled in the art can easily ascertain the essential characteristics spirit and scope thereof, can make various changes and modifications of the invention to adapt it to various usages and conditions.

Claims: WHAT IS CLAIMED IS: 1. An azeotropic composition consisting essentially of about 45 to 55 weight percent 1,1,1,2- tetrafluoroethane and about 55 to 45 weight percent dimethyl ether. 2. A binary mixture consisting of about 40.0-99.5 weight percent 1,1,1,2-tetrafluoroethane and 0.5 to 60.0 weight percent dimethyl ether. 3. The binary mixture of Claim 2 consisting essentially of about 91.C to 99.5 weight percent of 1,1,1,2-tetrafluoroethane and 0.5 to 9.0 weight percent dimethyl ether, said mi.rt/are being nonflammable. 4. The binary mixture of Claim 3 consisting essentially of 91.0 to 95.0 weight percent of 1,1,1,2- tetrafluoroethane and 5.0 to 9.0 weight percent dimethyl ether, said mixture being nonflammable. 5. A process of producing refrigeration comprising evaporating a constant boiling mixture of Claim 1 in the vicinity of a body to be cooled. 6. A process of producing refrigeration comprising evaporating a mixture of Claim 2 in the presence of a body to be cooled. 7. The process of Claim 6 wherein the mixture consists essentially of from 91.0 to 99.5 weight percent 1,1,1,2-tetrafluoroethane and 0.5 to 9.0 weight percent dimethyl ether. 8. The process of C]^i 6 wherein the mixture consists essentially of from 91.0 to 95.0 weight percent of 1,1,1,2-tetrafluoroethane and 5.0 to 9.0 weight percent dimethyl ether, said mixture being 9. A process for producing heat, comprising condensing a refrigerant having the composition of Claim 1 in the vicinity of a body to be heated. 10. A process for producing heat comprising condensing a refrigerant having the composition of Claim 2 in the vicinity of a body to be heated. 11. The process of Claim 10 wherein the refrigerant consists essentially of 91.0 to 99.5 weight percent 1,1,1,2-tetrafluoroethane and 0.5 to 9.0 weight percent dimethyl ether. 12. The process of Claim 10 wherein the refrigerant consists essentially of 91.0 to 95.0 weight percent 1,1,1,2-tetrafluoroethane and 5.0 to 9.0 weight percent dimethyl ether. 13. In a process for preparing a polymer foam comprising utilizing a blowing agent to expand a polymer, the improvement wherein the blowing agent is a composition of Claim 1. .14. The process of Claim 13, wherein the amount of the azeotropic composition used is from 1 to 30 weight percent of the total polymer foam formulation. 15. The process of Claim 14, wherein the polymer foam is a pclyurethane foam, a phenolic foam, or a polystyrene foam. 16. The process of Claim 15, wherein the polymer foam is a polyurethane foam. 17. A process for preparing aerosol formulations, comprising combining active ingredients in an aerosol container with an effective amount of the composition of Claim 1 as propellant. 18. In an aerosol composition comprising active ingredients and a propellant, the improvement wherein the propellant is a composition of Claim 1. 19. In an aerosol composition comprising active ingredients and a propellant, the improvement wherein the propellant is a composition of Claim 2. 20. In a refrigerant composition comprising a halocarbon or halocarbon mixture and a stabilizer, anti-corrosive agent, dye or lubricant, the improvement wherein the halocarbon or halocarbon mixture is a composition of Claim 1. 21. In a refrigerant composition comprising an azeotropic mixture and _ stabilizer, anti-corrosive agent, dye or lubricant, the improvement wherein the azeotrope or azeotropic mixture is a composition of Claim 1. 22. The composition of claim 1, consisting of about 45 to 55 weight percent 1,1,1,2-tetrafluoroethane and about 55 to 45 weight percent dimethyl ether. 23. The- composition of claim 1, wherein if said mixture is fractionally distilled, it would produce an azeotrope containing only 1,1,1,2-tetrafluoroethane and dimethyl ether in at least one fraction.

Inventors: BARTLETT PHILIP LEE, BIVENS DONALD BERNARD, YOKOZEKI AKIMICHI, BARTLETT, PHILIP, LEE, BIVENS, DONALD, BERNARD, YOKOZEKI, AKIMICHI
Applicants: DU PONT, E.I. DU PONT DE NEMOURS AND COMPANY
Application year: 1991
Main classification: C09K3
IPC codes: C07C19, C08G18, C08G101, C08J9, C08L25, C09K3, C09K5, C11D7