WO1996040371A1 - The use of bis(difluoromethyl)ether as a fire extinguishant - Google Patents
The use of bis(difluoromethyl)ether as a fire extinguishant Download PDFInfo
- Publication number
- WO1996040371A1 WO1996040371A1 PCT/US1996/008187 US9608187W WO9640371A1 WO 1996040371 A1 WO1996040371 A1 WO 1996040371A1 US 9608187 W US9608187 W US 9608187W WO 9640371 A1 WO9640371 A1 WO 9640371A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- ether
- difluoromethyl
- bis
- fire
- reaction
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
- C08J9/04—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent
- C08J9/12—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a physical blowing agent
- C08J9/14—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a physical blowing agent organic
- C08J9/143—Halogen containing compounds
-
- A—HUMAN NECESSITIES
- A62—LIFE-SAVING; FIRE-FIGHTING
- A62D—CHEMICAL MEANS FOR EXTINGUISHING FIRES OR FOR COMBATING OR PROTECTING AGAINST HARMFUL CHEMICAL AGENTS; CHEMICAL MATERIALS FOR USE IN BREATHING APPARATUS
- A62D1/00—Fire-extinguishing compositions; Use of chemical substances in extinguishing fires
- A62D1/0028—Liquid extinguishing substances
- A62D1/0057—Polyhaloalkanes
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2203/00—Foams characterized by the expanding agent
- C08J2203/14—Saturated hydrocarbons, e.g. butane; Unspecified hydrocarbons
- C08J2203/146—Saturated hydrocarbons containing oxygen and halogen atoms, e.g. F3C-O-CH2-CH3
Definitions
- Halon 1301 CF 3 Br
- 1211 CF 2 ClBr
- Halon 1301 is generally used in "total flood” applications in which the agent is discharged from a fixed automated system to uniformly fill a space to extinguish a fire or to provide inertion.
- the agent concentration required for fire suppression is the most important performance parameter in this application.
- Halon 1211 is usually used in "streaming" applications in which the halon is discharged from a portable, manual extinguisher to provide localized fire suppression. Both the extinguishment concentration and the discharge characteristics of "streaming" agents are important in determining fire extinguishment capacity.
- the vapor pressure of Halon 1301 is 234 psia, and that of Halon 1211 is 40 psia at room temperature. Either system can be pressurized for faster discharge, if needed.
- the Halons contain chlorofluorocarbons, and thus have been subject to the same restraints as other compounds of that class in view of their potential to deplete the ozone.
- Halon 1211 has an atmospheric life of 15 years and an ozone depletion potential (ODP) of 3.0.
- Halon 1301 has an atmospheric life of 110 years and an ODP of 10.0.
- ODP ozone depletion potential
- Suitable substitutes must meet certain requirements.
- the present invention provides a non-chlorofluorocarbon compound as a fire extinguishant. More specifically, the present inventor has found that Bis(difluoromethyl)ether is non-flammable, has an atmospheric life of only 2,8 years, and has zero ozone depletion potential. The ether behaves well as a fire extinguishant.
- Figure 1 is a schematic view of apparatus used to test fire extinguishing concentrations.
- Bis(difluoromethyl)ether can be prepared by a variety of processes conventional in the art. For example, it can be prepared by chlorination of dimethyl ether followed by isolation and fluorination of bis(dichloromethyl)ether. A preferred approach avoids the unstable complex mixture of chlorinated ethers, some of which are carcinogens, by employing methyl difluoromethyl ether as a starting material.
- the methyl difluoromethyl ether is chlorinated to give a chlorinated reaction mixture including at least one compound of the formula CF 2 H0CH 3 _-C1 Z , wherein z is 1, 2 or 3, which compound can be readily separated from the chlorinated reaction mixture.
- the chlorination reaction product itself may be fluorinated (without prior separation) as follows.*
- methyl difluoromethyl ether which is regarded as the starting material for the process of the present invention is a known compound which may be prepared in the manner reported by Hine and Porter in their aforementioned article published in the Journal of the American Chemical Society. Specifically, difluoromethyl methyl ether is produced by reaction of sodium methoxide (NaOMe) with chlorodifluoromethane (CF 2 HC1) , which reaction may be represented as follows:
- the method involves forming an alcohol solution of sodium methoxide and bubbling the chlorodifluoromethane slowly into the reaction mixture to obtain the methyldifluoromethyl ether as a residue in the reaction mixture.
- Some product is entrained with unreacted CF 2 HC1 and can be separated from it in a distillation operation.
- the starting ether, CHF 2 OCH 3 also might be prepared by first reacting NaOH with CH 3 0H, in effect making CH 3 ONa, and then reacting it with CF 2 HC1. However, water is also formed in the NaOH/CH 3 OH reaction. The effect water has on the subsequent reaction to form CHF 2 OCH 3 is to reduce the yield of CHF 2 OCH 3 .
- chlorination and fluorination steps of this invention can be represented as follows:
- the oxygen should be present in an amount effective for the desired inhibition.
- the air is added in an amount from about 1.5 to about 5.5% of the total gas flow.
- the amounts will be about 1/5 that of air.
- the oxygen source is added to the reaction medium for as long as the chlorine gas is flowing.
- CHF 2 OCH 3 may be suitably chlorinated by liquefying the CHF 2 OCH 3 and reacting it with chlorine gas while irradiating with a source of visible light.
- a source of visible light e.g., one may use other light sources such as ultraviolet light or heat, a catalyst or a free radical initiator to aid in the reaction.
- the chlorination products of CHF 2 OCH 3 can be readily separated prior to fluorination or the reaction mixture can be fluorinated without separation to give an admixture of CF 2 H0CC1 2 F, CF 2 H0CF 2 C1, CF ⁇ OCK j F, CFjHOCFHCl, CF 2 HOCF 2 H. All separations may be effected by fractional distillation.
- a preferred method of chlorinating the CHF 2 OCH 3 is to maintain the CHF 2 OCH 3 in a vapor phase and react it with chlorine gas while subjecting the chlorination reaction to a source of light, preferably visible or ultraviolet light.
- a source of light preferably visible or ultraviolet light.
- other reaction aids such as a catalyst, heat or a free radical initiator may be used instead of light in the chlorination reaction.
- the HF may be diluted with an organic solvent, preferably a dipolar aprotic solvent such as methyl pyrrolidone, in order to reduce fragmentation of the fluorinated material, resulting in higher yields of desired product with less by-product generation.
- organic solvent preferably a dipolar aprotic solvent such as methyl pyrrolidone
- Other sources of fluorine for the fluorination step include metal fluorides that can form salts of the HF 2 ⁇ anion, such as KHF 2 , NaHF 2 , LiHF 2 , NH 4 HF 2 , etc., and pyridine salts of HF and NaF and KF in suitable solvents.
- the resultant fluorinated products may be separated by distillation or by the process as taught in U.S. Patent 4,025,567 or U.S. Patent 3,887,439 which are incorporated herein by reference in their entirety.
- the Bis(difluoroomethyl)ether thus produced has been found to be effective as a fire extinguishant at a minimum concentration of about 11.7 volume percent in air.
- the bis(difluoromethyl)ether can be used in conjuction with inert gases, such as nitrogen, carbon dioxide, CF 3 H, etc. Carbon dioxide is especially preferred, since it exhibits some degree of solubility in the ether.
- a 25 wt % solution of sodium methoxide in methanol (1533.lg) containing 7.1 moles of sodium methoxide was placed in a 4 liter jacketed autoclave fitted with a temperature sensor, a pressure gauge and a dipleg.
- the vessel was cooled to 0 to 5°C and chlorodifluoromethane (318.2g, 3.70 moles) added over a period of 2.5 hours with agitation.
- the autoclave was slowly warmed to about 60°C while venting gaseous products through the water-cooled condenser-into a collection trap cooled to about - 70°C.
- Chlorine and CF 2 HOCH 3 in a gaseous phase are passed through separate condensers cooled to 0°C and then the gas streams combine and pass into one arm of a U-shaped reactor, irradiated with visible light or UV. Both arms of the reactor are jacketed and cooled with water.
- a Dewar-type condenser cooled to -50°C is attached to the outlet of the second arm of the U-tube and, in turn, it is connected in series with a cold trap to collect unreacted chlorine and an NaOH scrubber to remove HC1.
- the reaction is normally carried out at atmospheric pressure, but higher or lower pressure can be used. Temperature should not be allowed to rise much above 50°C in the reactor to avoid attack on the glass.
- the apparatus is flushed with nitrogen and then chlorine and CHF 2 OCH 3 are fed to the reactor at rates such that the ratio of the flow of chlorine to that of the ether is maintained at about 2.5:1 for optimum results, i.e., yield of CF 2 H0CHC1 2 .
- a predominant amount of any one of the three products can be obtained by changing the ratio of the gas flows .
- the chlorination apparatus consisted of two vertical lengths of jacketed glass tubing, 4 feet long by 2 inches I.D., connected at the lower ends in a U-tube fashion by a short length of unjacketed 2 inch I.D. tubing.
- a drain tube led from the lowest point of the U-tube arrangement so that product could be collected as it formed and removed continuously from the apparatus or alternatively allowed to accumulate in a receiver.
- Three 150 watt incandescent flood lamps were arranged along the length of each tube.
- the gases were fed into the upper end of one arm of the U-tube arrangement. Flow rates were measured by calibrated mass flowmeters.
- a low temperature condenser on the outlet of the second arm of the U-tube returned unreacted E-152a and chlorine to the illuminated reaction zone. Hydrogen chloride by-product and air passed through the condenser into a water scrubber where the hydrogen chloride was removed.
- a mixture of methanol and water, cooled to 0 to 5°C was circulated through the cooling jackets of the apparatus.
- coolant at a temperature of 0 to 5°C is circulated through the cooling jackets, the flood lamps were turned on and dry ice placed in the low temperature condenser. Chlorine was introduced into the apparatus first, followed by difluoromethyl ether and air in the desired ratios. Product was removed at intervals from the receiver and washed with saturated NaHC0 3 solution to remove HC1. Since the reaction was continuous, it could proceed for any length of time desired. At the end of the reaction, gas flows were stopped and product allowed to drain from the vertical reactor tubes into the receiver.
- Examples 6- 29-1 to 6-29-7 show the distribution of products normally obtained without the addition of air to the gas stream.
- Examples 7-7-3 through 7-8-6 show the effect of the addition of air in diminishing amounts, in accordance with the present invention.
- the extinguishing concentra ion of Bis(difluoromethyl)ether was determined using the I.C.I, cup burner method, which is a standard test.
- the apparatus is shown in Figure 1, and consisted of a 8.5 cm by 53 cm tall outer chimney through which air was passed at 40L/min from a glass bead distributor at its base.
- An inner fuel cup burner with a 3.1 cm O.D. and a 2.15 cm I.D. was positioned 30.5 cm below the top edge of the chimney.
- Bis(difluoromethyl)ether was added to the air stream prior to entering the glass bead distributor. The air flow rate was maintained at 40L/min for the trial. Air and bis (difluoromethyl) ether flow rates were measured using rotameters.
- the test was conducted by adjusting the extended fuel reservoir to bring the liquid (heptane) level in the cup burner to just even with the base of a ground glass lip on the burner cup. With the air flow maintained at 40L/min, the fuel in the cup burner was ignited. Bis(difluoromethyl)ether was gradually added to the air stream until the flame was extinguished. The bis- (difluoromethyl)ether totameter reading was then recorded. The extinguishing concentration of the ether was calculatedd as a percentage of the combined flow of the ether and air. Reference agents Halon 1301 and HFC-227ea were tested similarly. Several runs were made with each test material, and the average values of the extinguishing concentration were as follows:
Abstract
Description
Claims
Priority Applications (6)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AU61475/96A AU699193B2 (en) | 1995-06-07 | 1996-05-31 | The use of bis(difluoromethyl)ether as a fire extinguishant |
MX9709476A MX9709476A (en) | 1995-06-07 | 1996-05-31 | The use of bis(difluoromethyl)ether as a fire extinguishant. |
DE0841967T DE841967T1 (en) | 1995-06-07 | 1996-05-31 | USE OF BIS-DIFLUORMETHYL ETHER AS A FIRE EXTINGUISHER |
EP96919022A EP0841967A4 (en) | 1995-06-07 | 1996-05-31 | The use of bis(difluoromethyl)ether as a fire extinguishant |
BR9609407A BR9609407A (en) | 1995-06-07 | 1996-05-31 | Use of bis (methyl diluor) ether as a flame extinguisher |
JP9500906A JPH11506648A (en) | 1995-06-07 | 1996-05-31 | Use of bis (difluoromethyl) ether as a fire extinguishing agent |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US48400595A | 1995-06-07 | 1995-06-07 | |
US08/484,005 | 1995-06-07 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO1996040371A1 true WO1996040371A1 (en) | 1996-12-19 |
Family
ID=23922346
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/US1996/008187 WO1996040371A1 (en) | 1995-06-07 | 1996-05-31 | The use of bis(difluoromethyl)ether as a fire extinguishant |
Country Status (12)
Country | Link |
---|---|
EP (1) | EP0841967A4 (en) |
JP (1) | JPH11506648A (en) |
CN (1) | CN1199349A (en) |
AU (1) | AU699193B2 (en) |
BR (1) | BR9609407A (en) |
CA (1) | CA2220431A1 (en) |
DE (1) | DE841967T1 (en) |
ES (1) | ES2128279T1 (en) |
MX (1) | MX9709476A (en) |
TW (1) | TW349874B (en) |
WO (1) | WO1996040371A1 (en) |
ZA (1) | ZA964268B (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0793982A1 (en) * | 1996-03-07 | 1997-09-10 | AUSIMONT S.p.A. | Flame-extinguishing compositions |
CN106823227A (en) * | 2017-03-17 | 2017-06-13 | 公安部天津消防研究所 | A kind of higher boiling gas extinguishing agent extinguishing concentration experimental rig and test method |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5444101A (en) * | 1993-04-23 | 1995-08-22 | Imperial Chemical Industries Plc | Process for rigid polyurethane foams |
US5444102A (en) * | 1993-03-05 | 1995-08-22 | Ikon Corporation | Fluoroiodocarbon blends as CFC and halon replacements |
US5484546A (en) * | 1993-05-19 | 1996-01-16 | E. I. Du Pont De Nemours And Company | Refrigerant compositions including an acylic fluoroether |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2066905A (en) * | 1935-03-23 | 1937-01-05 | Westinghouse Electric & Mfg Co | Halogenated methyl ethers |
CA1075854A (en) * | 1976-08-16 | 1980-04-22 | Charles W. Simons | Aerosol propellants for personal products |
-
1996
- 1996-05-27 ZA ZA964268A patent/ZA964268B/en unknown
- 1996-05-31 CN CN96194633A patent/CN1199349A/en active Pending
- 1996-05-31 AU AU61475/96A patent/AU699193B2/en not_active Ceased
- 1996-05-31 DE DE0841967T patent/DE841967T1/en active Pending
- 1996-05-31 JP JP9500906A patent/JPH11506648A/en active Pending
- 1996-05-31 ES ES96919022T patent/ES2128279T1/en active Pending
- 1996-05-31 CA CA002220431A patent/CA2220431A1/en not_active Abandoned
- 1996-05-31 EP EP96919022A patent/EP0841967A4/en not_active Withdrawn
- 1996-05-31 WO PCT/US1996/008187 patent/WO1996040371A1/en not_active Application Discontinuation
- 1996-05-31 MX MX9709476A patent/MX9709476A/en unknown
- 1996-05-31 BR BR9609407A patent/BR9609407A/en not_active Application Discontinuation
- 1996-06-04 TW TW085106651A patent/TW349874B/en active
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5444102A (en) * | 1993-03-05 | 1995-08-22 | Ikon Corporation | Fluoroiodocarbon blends as CFC and halon replacements |
US5444101A (en) * | 1993-04-23 | 1995-08-22 | Imperial Chemical Industries Plc | Process for rigid polyurethane foams |
US5484546A (en) * | 1993-05-19 | 1996-01-16 | E. I. Du Pont De Nemours And Company | Refrigerant compositions including an acylic fluoroether |
Non-Patent Citations (1)
Title |
---|
See also references of EP0841967A4 * |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0793982A1 (en) * | 1996-03-07 | 1997-09-10 | AUSIMONT S.p.A. | Flame-extinguishing compositions |
US5856587A (en) * | 1996-03-07 | 1999-01-05 | Ausimot Spa | Flame extinguishing compositions |
CN106823227A (en) * | 2017-03-17 | 2017-06-13 | 公安部天津消防研究所 | A kind of higher boiling gas extinguishing agent extinguishing concentration experimental rig and test method |
CN106823227B (en) * | 2017-03-17 | 2019-08-16 | 公安部天津消防研究所 | A kind of higher boiling gas extinguishing agent extinguishing concentration experimental rig and test method |
Also Published As
Publication number | Publication date |
---|---|
ES2128279T1 (en) | 1999-05-16 |
EP0841967A1 (en) | 1998-05-20 |
CA2220431A1 (en) | 1996-12-19 |
BR9609407A (en) | 1999-05-11 |
CN1199349A (en) | 1998-11-18 |
AU6147596A (en) | 1996-12-30 |
TW349874B (en) | 1999-01-11 |
DE841967T1 (en) | 1999-02-25 |
MX9709476A (en) | 1998-02-28 |
JPH11506648A (en) | 1999-06-15 |
ZA964268B (en) | 1996-12-04 |
EP0841967A4 (en) | 1999-11-17 |
AU699193B2 (en) | 1998-11-26 |
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