FIRE EXTINGUISHING COMPOSITION AND PROCESS

Abstract: A process for extinguishing, preventing and controlling fires using a composition containing at least one fluoro-substituted propane selected from the group of CF3-CHF-CF3, CF3-CF2-CHF2, CF3-CFH-CF2H, CF3-CH2-CF3, CF3-CF2-CH2F, CHF2-CF2-CHF2, CF3-CF2-CHCl2, CHFCl-CF2-CClF2, CHF2-CCl2-CF3, CF3-CHCl-CClF2, CHF2-CF2-CHClF, CF3-CF2-CH2Cl, CClF2-CF2-CH2F, CF3-CH2-CClF2, CHClF-CF2-CF3, CHF2-CF2-CF2Cl, CF3-CHCl-CF3, CF3-CHF-CF2Cl, and CHF2-CFCl-CF3 is disclosed. The fluoropropanes can be used in open or enclosed areas with little or no effect on the ozone in the stratosphere and with little effect on the global warming process.

Description: Fire Extinguishing Composition and Process Field of Invention This invention relates to compositions for use in preventing and extinguishing fires based on the combustion of combustible materials. More particularly, it relates to such compositions that are highly effective and "environmentally safe". Specifically, the compositions of this invention have little or no effect on the ozone layer depletion process; and make no or very little contribution to the global warming process known as the "greenhouse effect". Although these compositions have minimal effect in these areas, they are extremely effective in preventing and extinguishing fires, particularly fires in enclosed spaces. Background of the Invention and Prior Art In preventing or extinguishing fires, two important elements must be considered for success: (1) separating the combustibles from air; and (2) avoiding or reducing the temperature necessary for combustion to proceed. Thus, one can smother small fires with blankets or with foams to cover the burning surfaces to isolate the combustibles from the oxygen in the air. In the customary process of pouring water on the burning surfaces to put out the fire, the main element is reducing temperature to a point where combustion cannot proceed. Obviously, some smothering or separation of combustibles -from air also occurs in the water situation. The particular process used to extinguish fires depends upon several items, e.g. the location of the fire, the combustibles involved, the size of the fire, etc. In fixed enclosures such as computer rooms, storage vaults, rare book library rooms, petroleum pipeline pumping stations and the like, halogenated hydrocarbon fire extinguishing agents are currently preferred. These halogenated hydrocarbon fire extinguishing agents are not only effective for such fires, but also cause little, if any, damage to the room or its contents. This contrasts to the well-known "water damage" that can sometimes exceed the fire damage when the customary water pouring process is used. The halogenated hydrocarbon fire extinguishing agents that are currently most popular are the bromine-containing halocarbons, e.g. bromotrifluoromethane (CF_Br, Halon 1301) and bro ochlorodifluoromethane (CF_ClBr, Halon 1211) . It is believed that these bromine-containing fire extinguishing agents are highly effective in extinguishing fires in progress because, at the elevated temperatures involved in the combustion, these compounds decompose to form products containing bromine atoms which effectively interfere with the self-sustaining free radical combustion process and, thereby, extinguish the fire. These bromine-containing halocarbons may be dispensed from portable-equipment or from an automatic room flooding system activated by a fire detector. In many situations, enclosed spaces are involved. Thus, fires may occur in rooms, vaults, enclosed machines, ovens, containers, storage tanks, bins and like areas. The use of an effective amount of fire extinguishing agent in an enclosed space involves two situations. In one situation, the fire extinguishing agent is introduced into the enclosed space to extinguish an existing fire; the second situation is to provide an ever-present atmosphere containing the fire "extinguishing" or, more accurately the fire prevention agent in such an amount that fire cannot be initiated nor sustained. Thus, in U.S. Patent 3,844,354, Larsen suggests the use of chloropentafluoroethane (CF.-CF-Cl) in a total flooding system (TFS) to extinguish fires in a fixed enclosure, the chloropentafluoroethane being introduced into the fixed enclosure to maintain its concentration at less than 15%. On the other hand,, in U.S. Patent 3,715,438, Huggett discloses creating an atmosphere in a fixed enclosure which does not sustain combustion. Huggett provides an atmosphere consisting essentially of air, a perfluorocarbon selected from carbon tetrafluoride, hexafluoroethane, octafluoropropane and mixtures thereof. It has also been known that bromine- containing halocarbons such as Halon 1211 can be used to provide an atmosphere that will not support combustion. However, the high cost due to bromine content and the toxicity to humans i.e. cardiac sensitization at relatively low levels (e.g. Halon 1211 cannot be used above 1-2 %) make the bromine-containing materials unattractive for long term use. In recent years, even more serious objections to the use of brominated halocarbon fire extinguishants has arisen. The depletion of the stratospheric ozone layer, and particularly the role of chlorofluorocarbons (CFC's) have led to great interest in developing alternative refrigerants, solvents, blowing agents, etc. It is now believed that bromine-containing halocarbons such as Halon 1301 and Halon 1211 are at least as active as chlorofluorocarbons in the ozone layer depletion process. While perfluorocarbons such as those suggested by Huggett, cited above, are believed not to have as much effect upon the ozone depletion process as chlorofluorocarbons, their extraordinarily high stability makes them suspect in another environmental area, that of "greenhouse effect". This effect is caused by accumulation of gases that provide a shield against heat transfer and results in the undesirable warming of the earth's surface. There is, therefore, a need for an effective fire extinguishing composition and process which contributes little or nothing to the stratospheric ozone depletion process or to the "greenhouse effect". It is an object of the present invention to provide such a fire extinguishing composition; and to provide a process for preventing and controlling fire in a fixed enclosure by introducing into said fixed enclosure, an effective amount of the composition. Summary of Invention The present invention is based on the finding that an effective amount of a composition consisting essentially of at least one partially fluoro- substituted propane selected from the group of the heptafluoropropanes (CF 3 -CF_-CHF 2 and CF--CFH-CF-) , also known as HFC-227ca and HFC-227ea, the hexafluoropropanes (CF_-CH 2 -CF3, CF 3 -CF_-CH_F and CF 2 H-CF 2 -CF 2 H) , also known as HFC-236fa, HFC-236cb and HFC-236ca, and the chlorohexafluoropropanes (CFC1F-CF 2 -CF 3 , CHF 2 -CF 2 -CF 2 C1, C 3 -CHC1-CF 3 , CF 3 -CHF-CF 2 C1, and CHF 2 -CFC1-CF 3 ) , also known as HCFC-226ca, HCFC-226cb, HCFC-226da, HCFC-226ea and HCFC-226ba, will prevent and/or extinguish fire based on the combustion of combustible materials, particularly in an enclosed space, without adversely affecting the atmosphere from the standpoint of ozone depletion or "greenhouse effect". Also useful in this invention are those partially fluoro-substituted propanes with normal boiling points above 25 β C, i.e. HFC-236ea, HCFC-225ca, HCFC-225cb, HCFC-225aa, HCFC-225da, HCFC-235ca, HCFC-235cb, HCFC-235CC, and HCFC-235fa. The partially fluoro-substituted propanes above may be used in conjunction with as little as 1% of at least one halogenated hydrocarbon selected from the group of difluoromethane (HFC-32) , chlorodifluoromethane (HCFC-22) , 2,2-dichloro- 1,1,1-trifluoroethane (HCFC-123) , l,2-dichloro-l,l,2-trifluoroethane (HCFC-123a) , 2-chloro-l,l,l,2-tetrafluoroethane (HCFC-124) , 1-chloro-l,1,2,2-tetrafluoroethane (HCFC-124a) , pentafluoroethane (HFC-125), 1,1,2,2-tetrafluoroethane (HFC-134) , 1,1,1,2-tetrafluoroethane (HFC-134a) , 3,3-dichloro-l,1,1,2,2-pentafluoropropane (HCFC-225ca) , 1,3-dichloro-l,1,2,2,3-pentafluoropropane (HCFC-225cb) , 2,2-dichloro-l,1,1,3,3-pentafluoropropane (HCFC-225aa) , 2,3-dichloro-l,1,1,3,3-pentafluoropropane (HCFC-225da) , 1,1,1,2,2,3,3-heptafluoropropane (HFC-227ca) , 1,1,1,2,3,3,3-heptafluoropropane (HFC-227ea) , 1,1,1,2,3,3-hexafluoropropane (HFC-236ea) , 1,1,1,3,3,3-hexafluoropropane (HFC-236fa) , 1,1,1,2,2,3-hexafluoropropane (HFC-236cb) , 1,1,2,2,3,3-hexafluoropropane (HFC-236ca) , 3-chloro-l,1,2,2,3-pentafluoropropane (HCFC-235ca) , 3-chloro-l,1,1,2,2-pentafluoropropane (HCFC-235cb) , 1-chloro-l,1,2,2,3-pentafluoropropane (HCFC-235cc) , 3-chloro-l,1,1,3,3-pentafluoropropane (HCFC-235fa) , 3-chloro-l,1,1,2,2,3-hexafluoropropane (HCFC-226ca) , 1-chloro-l,1,2,2,3,3-hexafluoropropane (HCFC-226cb) , 2-chloro-1,1,1,3,3,3-hexafluoropropane (HCFC-226da) , 3-chloro-l,1,1,2,3,3-hexafluoropropane (HCFC-226ea) , and 2-chloro-1,1,1,2,3,3-hexafluoropropane (HCFC-226ba) . Preferred Embodiments The partially fluoro-substituted propanes, when added in adequate amounts to the air in a confined space, eliminate the combustion-sustaining properties of the air and suppress the combustion of flammable materials, such as paper, cloth, wood, flammable liquids, and plastic items, which may be present in the enclosed compartment. These fluoropropanes are extremely stable and chemically inert. They do not decompose at temperatures as high as 350*C to produce corrosive or toxic products and cannot be ignited even in pure oxygen so that they continue to be effective as a flame suppressant at the ignition temperatures of the combustible items present in the compartment. The preferred fluoropropanes are HFC-227ca, HFC-227ea, HFC-236cb, HFC-236fa, HFC-236ca and HFC-236ca, i.e. the HFC-227 and 236 series. The particularly preferred fluoropropanes HFC-227ca, HFC-227ea, HFC-236cb and HFC-236fa are additionally advantageous because of their low boiling points, i.e. boiling points at normal atmospheric pressure of less than 1.2 β C. Thus, at any low environmental temperature likely to be encountered, these gases will not liquefy and will not, thereby, diminish the fire preventive properties of the modified air. In fact, any material having such a low boiling point would be suitable as a refrigerant. The heptafluoropropanes HFC-227ea and HFC-227ca are also characterized by an extremely low boiling point and high vapor pressure, i.e. above 44.3 and 42.0 psig at 21*C respectively. This permits HFC-227 a and HFC-227ca to act as their own propellants in "hand-held" fire extinguishers. Heptafluoropropanes (HFC-227ea and HFC-227ca) may also be used with other materials such as those disclosed on page 5 of this specification to act as the propellant and co- extinguishant for these materials of lower vapor pressure. Alternatively, these other materials of lower vapor pressure may be propelled from a portable fire extinguisher or fixed system by the usual propellants, i.e. nitrogen or carbon dioxide. Their relatively low toxicity and their short atmospheric lifetime (with little effect on the global warming potential) compared to the perfluoroalkanes (with lifetimes of over 500 years) make these fluoropropanes ideal for this fire-extinguisher use. To eliminate the combustion-sustaining properties of the air in the confined space situation, the gas or gases should be added in an amount which will impart to the modified air a heat capacity per mole of total oxygen present sufficient to suppress or prevent combustion of the flammable, non-self-sustaining materials present in the enclosed environment. The minimum heat capacity required to suppress combustion varies with the combustibility of the particular flammable materials present, in the confined space. It is well known that the combustibility of materials, namely their capability for igniting and maintaining sustained combustion under a given set of environmental conditions, varies according to chemical composition and certain physical properties, such as surface area relative to volume, heat capacity, porosity, and the like. Thus, thin, porous paper such as tissue paper is considerably more combustible than a block of wood. In general, a heat capacity of about 40 cal./ β C and constant pressure per mole of oxygen is more than adequate to prevent or suppress the combustion of materials of relatively moderate combustibility, such as wood and plastics. More combustible materials, such as paper, cloth, and some volatile flammable liquids, generally require that the fluoroethane be added in an amount sufficient to impart a higher heat capacity. It is also desirable to provide an extra margin of safety by imparting a heat capacity in excess of minimum requirements for the particular flammable materials. A minimum heat capacity of 45 cal./"C per mole of oxygen is generally adequate for moderately combustible materials and a minimum of about 50 cal./ β C per mole of oxygen for highly flammable materials. More can be added if desired but, in general, an amount imparting a heat capacity higher than about 55 cal./ β C per mole of total oxygen adds substantially to the cost without any substantial further increase in the fire safety factor. Heat capacity per mole of total oxygen can be determined by the formula: C Prι* = (C P- « ° + 2ΪΑ (CP„) Z , P o 2 wherein: C * = ttcotal heat capacity per mole of oxygen at constant pressure; P-. -= partial pressure of oxygen; 2 P_ = partial pressure of other gas; ( C r> - , z = heat capacity of other gas at constant pressure. The boiling points of the fluoropropanes used in this invention and the mole percents required to impart to air heat capacities (Cp) of 40 and 50 cal./"C at a temperature of 25*C and constant pressure while maintaining a 20% and 16 % oxygen content -are tabulated below: Introduction of the appropriate fluoropropanes is easily accomplished by metering appropriate quantities of the gas or gases into the enclosed air-containing compartment. The air in the compartment can be treated at any time that it appears desirable. The modified air can be used continuously if a threat of fire is constantly present or if the particular environment is such that the fire hazard must be kept at an absolute minimum; or the modified air can be used as an emergency measure if a threat of fire develops. The invention will be more clearly understood by referring to the examples which follow. The unexpected effects of the fluoropropanes, alone and in any of the aforementioned blends, in suppressing and combatting fire, as well as its compatability with the ozone layer and its relatively low "greenhouse effect", when compared to other fire-combatting gases, particularly the perfluoroalkanes and Halon 1211, are shown in the examples. Example 1 - Fire Extinguishing Concentrations The fire extinguishing concentration of the fluoropropane compositions compared to several controls, was determined by the ICI Cup Burner method. This method is described in "Measurement of Flame-Extinguishing Concentrations" R. Hirst and K. Booth, Fire Technology, vol. 13(4): 296-315 (1977). Specifically, an air stream is passed at 40 liters/minute through an outer chimney (8.5 cm. I. D. by 53 cm. tall) from a glass bead distributor at its base. A fuel cup burner (3.1 cm. O.D. and 2.15 cm. I.D.) is positioned within the chimney at 30.5 cm. below the top edge of the chimney. The fire extinguishing agent is added to the air stream prior to its entry into the glass bead distributor while the air flow rate is maintained at 40 liters/minute for all tests. The air and agent flow rates are measured using calibrated rotameters. Each test is conducted by adjusting the fuel level in the reservoir to bring the liquid fuel level in the cup burner just even with the ground glass lip on the burner cup. ith the air flow rate maintained at 40 liters/minute, the fuel in the cup burner is ignited. The fire extinguishing agent is added in measured increments until the flame is extinguished. The fire extinguishing concentration is determined from the following equation: Extinguishing concentration = F. .__ where F. = Agent flow rate F_ = Air flow rate Two different fuels are used, heptane and methanol; and the average of several values of agent flow rate at extinguishment is used for the following table. Table 1 Extinguishing Concentrations of Certain Fluorooropane Com ositio Other A ents Example 2 The ozone depletion potential (ODP) of the fluoropropanes and various blends thereof, compared to various controls, was calculated using the method described in "The Relative Efficiency of a Number of Halocarbon for Destroying Stratospheric Ozone" D. J. Wuebles, Lawrence Livermore Laboratory report UCID-18924, (January 1981) and "Chlorocarbon Emission Scenarios: Potential Impact on Stratospheric Ozone" D. J. Wuebles, Journal Geophysics Research, 88, 1433-1443 (1983) . Basically, the ODP is the ratio of the calculated ozone depletion in the stratosphere resulting from the emission of a particular agent compared to the ODP resulting from the same rate of emission of FC-11 (CFC1_) which is set at 1.0. Ozone depletion is believed to be due to the migration of compounds containing chlorine or bromine through the troposphere into the stratosphere where these compounds are photolyzed by UV radiation into chlorine or bromine atoms. These atoms will destroy the ozone (O ) molecules in a cyclical reaction where molecular oxygen (0 ) and [CIO] or [BrO] radicals are formed, those radicals reacting with oxygen atoms formed by UV radiation of 0_ " to reform chlorine or bromine atoms and oxygen molecules, and the reformed chlorine or bromine atoms then destroying additional ozone, etc. , until the radicals are finally scavenged from the stratosphere. It is estimated that one chlorine atom will destroy 10,000 ozone molecules and one bromine atom will destroy 100,000 ozone molecules. The ozone depletion potential is also discussed in "Ultraviolet Absorption Cross-Sections of Several Brominated Methanes and Ethanes" L. T. Molina, M. J. Molina and F. S. Rowland" J. Phys. Chem. 86, 2672-2676 (1982); in Bivens et al. U.S. Patent 4,810,403; and in "Scientific Assessment of Stratospheric Ozone: 1989" U.N. Environment Programme (21 August 1989) . In the following table, the ozone depletion potentials are presented for the fluoropropanes and the controls.

Claims: I claim: 1. A process for preventing, controlling and extinguishing fire in an enclosed air-containing area which contains combustible materials of the non-self-sustaining type, which compr ses introducing into the air in said enclosed area an amount of at least one fluoro-substituted propane selected from the group of CF 3 -CHF-CF 3 , CHF 2 ~CF 2 -CF 3 , CF 3 -CH 2 -CF 3 , CF 3 -CF 2 -CH 2 F, CF 2 H-CF 2 -CF 2 H, CHClF-CF 2 -CF 3 , CHF 2 -CF 2 -CF 2 C1, CF 3 -CHC1-CF 3 , CF 3 -CHF-CF 2 C1, and CHF_-CFC1-CF 3 sufficient to impart a heat capacity per mol of total oxygen that will suppress combustion of the combustible materials in said enclosed area. 2. A process as in Claim 1 wherein the amount of said propane in said enclosed area is maintained at a level of about 4 to 100 volume percent. 3. A process as in Claim 1 wherein the amount of said propane in said enclosed area is maintained at a level of about 10 volume percent. 4. A process as in Claim 1 wherein at least 1% of at least one halogenated hydrocarbon is blended with said ethane introduced into said enclosed area, said halogenated hydrocarbon being selected from the group consisting of difluoromethane, chlorodifluoromethane, ,2-dichloro-l,1,1-trifluoroethane, 1,2-dichloro-l,1,2-trifluoroethane, 2-chloro-1,1,1,2-tetrafluoroethane, 1-chloro-l,1,2,2-tetrafluoroethane, pentafluoroethane, 1,1,2,2-tetrafluoroethane, 1,1,1,2-tetrafluoroethane, 1,2-dichloro-1,2-difluoroethane, 1,1-dichloro-l,2-difluoroethane, 3,3-dichloro-1,1,1,2,2-pentafluoropropane, 1,3-dichloro-l,1,2,2,3-pentafluoropropane, 2,2-dichloro-l,1,1,3,3-pentafluoropropane, 2,3-dichloro-1,1,1,3,3-pentafluoropropane, 1,1,1,2,2,3,3-heptafluoropropane, 1,1,1,2,3,3,3-heptafluoropropane, 1,1,1,2,3,3-hexafluoropropane, 1,1,1,3,3,3-hexafluoropropane, 1,1,1,2,2,3-hexafluoropropane, 1,1,2,2,3,3-hexafluoropropane, 3-chloro-1,1,2,2,3-pentafluoropropane, 3-chloro-1,1,1,2,2-pentafluoropropane, 1-chloro-l,1,2,2,3-pentafluoropropane, 3-chloro-l,1,1,3,3-pentafluoropropane, 3-chloro-1,1,1,2,2,3-hexafluoropropane, 1-chloro-l,1,2,2,3,3-hexafluoropropane, 2-chloro-1,1,1,3,3,3-hex fluoropropane, 3-chloro-1,1,1,2,3,3-hexafluoropropane and 2-chloro-1,1,1,2,3,3-hexafluoropropane. 5. A process for extinguishing a fire which comprises introducing a volume of at least one fluoro-substituted propane selected from the group of CF 3 -CHF-CF 3 , CHF 2 -CF 2 "CF 3 , CF 3 -CH 2 -CF 3 , CF 3 -CF 2 -CH 2 F, CF 2 H-CF 2 -CF 2 H, CHC1F-CF 2 -CF 3 , CHF 2 -CF 2 -CF 2 Cl, CF 3 -CHC1-CF 3 , CF 3 -CHF-CF 2 C1, and CHF 2 -CFC1-CF 3 sufficient to provide an extinguishing concentration in an enclosed area, and maintaining said concentration at a value of less than 80 volume percent until said fire is extinguished. 6. A process as in Claim 5 wherein at least 1% of at least one halogenated hydrocarbon is blended with said ethane introduced into said enclosed area, said halogenated hydrocarbon being selected from the group consisting of difluoromethane, chlorodifluoro- methane, 2,2-dichloro-l,1,1-trifluoroethane, 1,2-dichloro-l,1,2-trifluoroethane, 2-chloro-l,1,1,2-tetrafluoroethane, 1-chloro-l,1,2,2-tetratfluoroethane, pentafluoroethane, 1,1,2,2-tetrafluoroethane, 1,1,1,2-tetrafluoroethane, 1,2-dichloro-l,2-difluoroethane, 1,1-dichloro-l,2-difluoroethane, 3,3-dichloro-l,1,1,2,2-pentafluoropropane, 1,3-dichloro-l,1,2,2,3-pentafluoropropane, 2,2-dichloro-l,1,1,3,3-pentafluoropropane, 2,3-dichloro-1,1,1,3,3-pentafluoropropane, 1,1,1,2,2,3,3-heptafluoropropane, 1,1,^,2,3,3,3-heptafluoropropane, 1,1,1,2,3,3-hexafluoropropane, 1,1,1,3,3,3-hexafluoropropan , 1,1,1,2,2,3-hexafluoropropane, 1,1,2,2,3,3-hexafluoropropane, 3-chloro-1,1,2,2,3-pentafluoropropane, 3-chloro-1,1,1,2,2-pentafluoropropane, 1-chloro-l,1,2,2,3-pentafluoropropane, 3-chloro-l,1,1,3,3-pentafluoropropane, 3-chloro-l,1,1,2,2,3-hexafluoropropane, 1-chloro-l,1,2,2,3,3-hexafluoropropane, 2-chloro-1,1,1,3,3,3-hexafluoropropane, 3-chloro-l,1,1,2,3,3-hexafluoropropane and 2-chloro-1,1,1,2,3,3-hexafluoropropane. 7. A fire extinguishing composition comprising at least 4 volume percent of at least one fluoro-substituted propane selected from the group of CF 3 -CHF-CF 3 , CHF 2 -CF 2 -CF 3 , CF 3 -CH 2 "CF 3 , CF 3 -CF 2 "CH 2 F CF 2 H-CF 2 -CHF 2 , CHC1F-CF 2 -CF 3 , CHF 2 -CF 2 -CF 2 C1, CF 3 -CHC1-CF 3 , CF 3 -CHF-CF 2 C1, and CHF 2 -CFC1-CF 3 . 8. The composition of Claim 7 wherein at least 1% of at least one halogenated hydrocarbon is blended with said propane introduced into said enclosed area, said halogenated hydrocarbon being selected from the group consisting of difluoromethane, chlorodifluoromethane, 2,2-dichloro-l ,1,1-trifluoroethane, 1,2-diσhloro-1,1,2-trifluoroethane, 2-chloro-1,1,1,2-tetrafluoroethane, 1-chloro-l,1,2,2-tetrafluoroethane, pentafluoroethane, 1,1,2,2-tetrafluoroethane, 1,1,1,2-tetrafluoroethane, 1,2-dichloro-l,2-difluoroethane, 1,1-dichloro-l,2-difluoroethane, 3,3-dichloro-1,1,1,2,2-pentafluoropropane, 1,3-dichloro-1,1,2,2,3-pentafluoropropane, 2,2-dichloro-l,1,1,3,3-pentafluoropropane, 2,3-dichloro-l,1,1,3,3-pentafluoropropane, 1,1,1,2,2,3,3-heptafluoropropane, 1,1,1,2,3,3,3-heptafluoropropane, 1 / 1 / 1,2,3,3-hexafluoropropane, 1,1,1,3,3,3-hexafluoropropane, 1,1,1,2,2,3-hexafluoropropane, 1,1,2,2,3,3-hexafluoropropane, 3-chloro-l,1,2,2,3-pentafluoropropane, 3-chloro-l,1,1,2,2-pentafluoropropane, 1-chloro-l,1,2,2,3-pentafluoropropane, 3-chloro-l,1,1,3,3-pentafluoropropane, 3-chloro-l,1,1,2,2,3-hexafluoropropane, 1-chloro-l,1,2,2,3,3-hexafluoropropane, 2-chloro-1,1,1,3,3,3-hexafluoropropane, 3-chloro-l,1,1,2,3,3-hexafluoropropane, and 2-chloro-1,1,1,2,3,3-hexafluoropropane. 9. A fire extinguishing composition comprising at least one fluoro-substituted propane selected from the group of CF 3 -CFH-CF 3 , CF 3 ~CF 2 -CHF 2 , CF 3 -CHF-CF 2 H, CF 3 -CH 2 -CF 3 , CF^CF^O^F, CF 2 H-CF 2 -CHF 2 , 5 CF 3 -CF 2 -CHC1 2 , CHFC1-CF 2 -CF 2 C1, CHF 2 -CC1 2 -CF 3 , CF 3 -CHC1-CC1F 2 , CHF 2 -CF 2 -CHC1F, CF 3 -CF 2 -CH 2 Cl, CC1F 2 -CF 2 -CH 2 F, CF 3 -CH 2 -CC1F 2 , CHC1F-CF 2 -CF 3 , CHF 2 -CF 2 -CF 2 C1, CF 3 -CHC1-CF 3 , CF 3 -CHF-CF 2 C1, and CHF 2 -CFC1-CF 3 . 10 10. The composition of Claim 9 wherein nitrogen or any other propellant usually used in portable fire extinguishers is added in sufficient quantity to provide a pressure of at least 140 psig in 15 said portable fire extinguisher. 11. The composition of Claim 9 wherein at least 1% of at least one halogenated hydrocarbon is blended with said propane, said halogenated hydrocarbon 20 being selected from the group consisting of difluoromethane, chlorodifluoromethane, 2,2-dichloro-l,1,1-trifluoroethane, 1,2-dichloro-l,1,2-trifluoroethane, 2-chloro-1,1,1,2-tetrafluoroethane, • 25 1-chloro-l,1,2,2-tetrafluoroethane, pentafluoroethane, 1,1,2,2-tetrafluoroethane, 1,1,1,2-tetra luoroethane, 1,2-dichloro-l,2-difluoroethane, 1,1-dichloro-l,2-difluoroethane, 3,3-dichloro-l,1,1,2,2-pentafluoropropane, 30 1,3-dichloro-l,1,2,2,3-pentafluoropropane, 2,2-dichloro-l,1,1,3,3-pentafluoropropan , 2,3-dichloro-1,1,1,3,3-pentafluoropropane, 1,1,1,2,2,3,3-heptafluoropropane, 1,1,1,2,3,3,3-heptafluoropropane, 3 5 1,1,1,2,3,3-hexafluoropropane, 1,1,1,3,3,3-hexafluoropropane, 1,1,1,2,2,3-hexafluoropropane, 1,1,2,2,3,3-hexafluoropropane, 3-chloro-1,1,2,2,3-pentafluoropropane, 3-chloro-l,1,l,2,2-pentafluoropropane, 1-chloro-l,1,2,2,3-pentafluoropropane, 3-chloro-l,1,l,3,3-pentafluoropropane, 3-chloro-1,1,1,2,2,3-hexafluoropropane, 1-chloro-l,1,2,2,3,3-hexafluoropropane, 2-chloro-1,1,1,3,3,3-hexafluoropropane, 3-chloro-l,1,1,2,3,3-hexafluoropropane, and 2-chloro-1,1,1,2,3,3-hexafluoropropane. 12. The composition of Claim 11 wherein nitrogen or any other propellant usually used in portable fire extinguishers is added in suffucient quantity to provide a pressure of at least 140 psig at 21 " C in said portable fire extinguisher. 13. A fire extinguishing composition comprising at least one fluoro-substituted propane selected from the group of CF 3 ~CFH-CF 3 , CF -CF 2 -CHF 2 , CF 3 -CHF-CF 2 H, CF 3 -CH 2 -CF 3 , CF 3 -CF 2 -CH 2 F and CF„H-CF„-CHF 2,'

Inventors: FERNANDEZ RICHARD EDWARD, FERNANDEZ, RICHARD, EDWARD
Applicants: DU PONT, E.I. DU PONT DE NEMOURS AND COMPANY
Application year: 1990
Main classification: A62C2
IPC codes: A62D1