EP0779260A2 - Fuel compositions for use in hybrid inflators containing stored oxidizing gas - Google Patents

Fuel compositions for use in hybrid inflators containing stored oxidizing gas Download PDF

Info

Publication number
EP0779260A2
EP0779260A2 EP96309042A EP96309042A EP0779260A2 EP 0779260 A2 EP0779260 A2 EP 0779260A2 EP 96309042 A EP96309042 A EP 96309042A EP 96309042 A EP96309042 A EP 96309042A EP 0779260 A2 EP0779260 A2 EP 0779260A2
Authority
EP
European Patent Office
Prior art keywords
fuel
oxidizer
mixtures
gas
heat
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
EP96309042A
Other languages
German (de)
French (fr)
Inventor
Carl K. Rink
Robert D. Taylor
Michael W. Barnes
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Morton International LLC
Original Assignee
Morton International LLC
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Morton International LLC filed Critical Morton International LLC
Publication of EP0779260A2 publication Critical patent/EP0779260A2/en
Withdrawn legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C06EXPLOSIVES; MATCHES
    • C06BEXPLOSIVES OR THERMIC COMPOSITIONS; MANUFACTURE THEREOF; USE OF SINGLE SUBSTANCES AS EXPLOSIVES
    • C06B47/00Compositions in which the components are separately stored until the moment of burning or explosion, e.g. "Sprengel"-type explosives; Suspensions of solid component in a normally non-explosive liquid phase, including a thickened aqueous phase
    • C06B47/02Compositions in which the components are separately stored until the moment of burning or explosion, e.g. "Sprengel"-type explosives; Suspensions of solid component in a normally non-explosive liquid phase, including a thickened aqueous phase the components comprising a binary propellant
    • CCHEMISTRY; METALLURGY
    • C06EXPLOSIVES; MATCHES
    • C06DMEANS FOR GENERATING SMOKE OR MIST; GAS-ATTACK COMPOSITIONS; GENERATION OF GAS FOR BLASTING OR PROPULSION (CHEMICAL PART)
    • C06D5/00Generation of pressure gas, e.g. for blasting cartridges, starting cartridges, rockets

Definitions

  • This invention relates to a hybrid gas generating system for an airbag inflator. More particularly, it relates to a novel system which minimizes particulates in the generated gas and which provides internal ballistic control of the inflator. Still more particularly, it relates to the use of a solid organic fuel in which some level of an oxidizer has been incorporated to generate heat and vaporize the fuel so that it can then be burned in a stored oxidizing gas.
  • Hybrid gas generators contain a stored gas which may be an oxidizing gas, an inert gas, or a mixture of the two.
  • the oxidizing gas may be mixed with gaseous or liquid fuel and burned to produce heated gaseous products which may be used to inflate an airbag in an automobile.
  • a pyrotechnic heater cartridge When the stored gas is totally inert a pyrotechnic heater cartridge must be used to heat the gas prior to inflation of the airbag.
  • Exemplary of the many patents issued in this field are U. S. Patent Nos.
  • Control over the airbag inflation rate is desirable to minimize the forces a person experiences during dynamic response to an automobile collision.
  • Control over the rate of heating the stored gas provides some measure of control over the rate of gas efflux from the inflator and, hence, the rate of airbag inflation.
  • the extrusion of pyrotechnic materials into various shapes and their formulation to achieve certain burning rates may be used to control the rate of inflation.
  • a disadvantage of using a totally inert gas and a pyrotechnic heater, however, is the production of objectionably high level of particulates to which the occupants of the automobile are subjected.
  • Several criteria must be met by a pyrotechnic gas generant to be satisfactory for inflatable restraint systems.
  • the pyrotechnic must be safe to handle and must be capable of generating a large amount of gas within a very short time frame, i.e., about 35 milliseconds.
  • a method for inflating an air bag in an automobile by igniting an under-oxidized solid fuel composition in response to a signal from a deceleration sensor in the automobile, vaporizing said fuel with heat thus generated, introducing the vaporized fuel into an oxygen-containing gas within a pressure vessel, fully oxidizing the fuel in said gas, thereby generating sufficient heat to raise the pressure within the vessel and force the pressurized gas into an air bag communicating with the vessel.
  • the invention is further described as a hybrid gas generating system comprising a pressure vessel containing oxygen under pressure, a container adapted for communication with the pressure vessel, a solid combustible fuel having a heat of combustion of at least about 3500 calories per gram and an oxidizer within said container, said oxidizer being present in said container in an amount sufficient only to support combustion of the fuel to generate heat to vaporize the fuel, said amount being less than 60% of the stoichiometric amount required for the oxidation of all available carbon in said fuel to carbon dioxide and all available hydrogen in said fuel to water, an igniter for a mixture of the solid fuel and oxidizer, thereby causing said mixture to burn and increasing the pressure of the gas within the pressure vessel.
  • the solid fuel suitable for use in the pyrotechnic material of this invention has the empirical formula C x H y O z N u wherein x and y are positive integers, and z and u are independently zero or positive integers.
  • the stoichiometric amount of oxidizer required for the oxidation of all available carbon in said fuel to carbon dioxide and all available hydrogen in said fuel to water is 2x + y/2-z moles of oxygen per mole of fuel.
  • the level of oxidizer present in the under-oxidized formulations is preferably such that less than one gram of solid particulate is exhausted from a standard-sized airbag module when the fuel composition is oxidized by the internal oxidizer and the oxidizing gas.
  • An airbag module is defined herein as an inflator device plus an inflatable airbag cushion.
  • Examples of a solid fuel suitable for the purposes of this invention include polyolefins, waxes, asphalts, and internally partially oxidized compounds such as sugars, polyesters, polyethers, acrylic polymers, phenols, polysaccharides, e.g., cellulose or starch, cellulose ethers, or cellulose esters, and nitrate salts of amines, nitramines, nitro compounds, nitrate esters, and mixtures of two or more of said compounds.
  • the heat of combustion of a suitable fuel is at least about 3500, preferably about 4000 or more, calories per gram.
  • the ratio of the number of moles of oxygen present in the fuel molecule per the quantity (2 x moles of C + 0.5 x moles of H), or O/F ratio is preferably from 0 to about 0.4.
  • the O/F ratio for methyl cellulose (C 18 H 31 O 11 ) is 0.214 and its heat of combustion is-4960 calories per gram.
  • the O/F for poly methylmethacrylate (C 5 H 8 O 2 ) is 0.143 and its heat of combustion is -6530 calories per gram.
  • Suitable solid fuels are exemplified by lactose, ethyl cellulose, hydroxyethyl cellulose, cellulose acetate, cellulose propionate, stearic acid, polyacetal, polyethylene, polypropylene, polystyrene, naphthalene, resorcinol, and a saturated linear polyester such as that sold under the BOSTIC 4156 trademark and number. All of the foregoing fuels are readily available from purveyors of commodity chemicals.
  • any stable, solid inorganic oxidizer is suitable for the purposes of this invention.
  • suitable oxidizers include the sodium, potassium, lithium, and other alkali metal chromates, dichromates, nitrates, chlorates, and perchlorates.
  • the corresponding ammonium salts are also useful.
  • the selection of the oxidizer depends upon the type of solid fuel.
  • From 0 to about 50 % of the total weight of the solid pyrotechnic material may be a plasticizer such as the alkyl and alkoxyalkyl adipates, sebacates, phthalates, azelates, and nitrates.
  • Catalysts and burn rate modifiers are optional and, when used, the maximum amount is about 5% of the weight of the pyrotechnic material.
  • Examples of such include boron hydrides and transition metal oxides such as copper oxide, manganese oxide, and vanadium oxide.
  • the rate of producing heat for the stored gas is a function of the surface area and the linear regression rate of the solid pyrotechnic material.
  • the surface area may be tailored easily by the physical shape of the pyrotechnic.
  • a granular pyrotechnic material will have a high surface area while cylindrical particles will have a small surface area.
  • the shaping of the particles may be by extrusion, solvent extrusion, molding, spray drying and pelletization, or extrusion and spheronization.
  • the amount of oxygen in the stored gas must be sufficient to complete the oxidation of all available carbon in said fuel to carbon dioxide and all available hydrogen in said fuel to water.
  • the oxygen-containing gas may be 100 % oxygen or a mixture of oxygen and an inert gas such as nitrogen or argon. Air is suitable.
  • the oxidizer portion of a pyrotechnic composition is by far the major portion, the ratio of oxidizer to fuel being as high as 4:1 or even higher.
  • the total amount of pyrotechnic material can be reduced greatly along with the proportion of oxidizer.
  • a stoichiometric ratio of 30.00 % of a polyester, 16.16 % of potassium perchlorate, and 52.85 % oxygen is utilized in the heating of x grams of an oxygen/argon mixture in an inflator device when only 11.73 grams of an under-oxidized pyrotechnic material containing 65.73 % of polyester and 34.22 % of the perchlorate is burned in said mixture.
  • the stoichiometric formulation of the ethyl cellulose and potassium perchlorate is 19.7 : 80.3 parts by weight.
  • An under-oxidized pyrotechnic material consisting of 80.5 parts by weight of ethyl cellulose and 19.5 parts by weight of potassium perchlorate is burned in a hybrid inflator containing an oxygen/argon mixture in a pressurized cylinder.
  • the proportion of fuel, perchlorate and oxygen taking part in the combustion is 33.2 : 8.0 : 58.8.
  • the combustion releases 1840 calories per gram of pyrotechnic material in one hundred grams of the combustion mixture. Thirty thousand (30,000) calories of heat are required for the inflation of a passenger side air bag by the hybrid inflator; thus, the inflation requires the combustion of 16.3 grams of the pyrotechnic material.
  • About 1.7 grams of potassium chloride are produced.

Abstract

An air bag is inflated by vaporizing an under-oxidized solid fuel composition and introducing the vapor into a vessel containing oxygen under pressure wherein it is fully oxidized to generate sufficient heat to raise the pressure within the vessel and force the pressurized gas into an air bag. The amount of oxidizer in the under-oxidized solid fuel composition is sufficient only to support combustion of the fuel to generate sufficient heat to vaporize the fuel, said amount being less than 60% of the stoichiometric amount required for the oxidation of all of the available carbon in said fuel to carbon dioxide and all available hydrogen in said fuel to water.

Description

  • This invention relates to a hybrid gas generating system for an airbag inflator. More particularly, it relates to a novel system which minimizes particulates in the generated gas and which provides internal ballistic control of the inflator. Still more particularly, it relates to the use of a solid organic fuel in which some level of an oxidizer has been incorporated to generate heat and vaporize the fuel so that it can then be burned in a stored oxidizing gas.
  • Hybrid gas generators contain a stored gas which may be an oxidizing gas, an inert gas, or a mixture of the two. The oxidizing gas may be mixed with gaseous or liquid fuel and burned to produce heated gaseous products which may be used to inflate an airbag in an automobile. When the stored gas is totally inert a pyrotechnic heater cartridge must be used to heat the gas prior to inflation of the airbag. Exemplary of the many patents issued in this field are U. S. Patent Nos. 3,692,495 (Schneiter et al); 3,723,205 (Scheffee); 3,756,621 (Lewis et al); 3,785,149 (Timmerman); 3,897,285 (Hamilton et al); 3,901,747 (Garner); 3,912,562 (Garner); 3,950,009 (Hamilton); 3,964,255 (Catanzarite); 4,128,996 (Garner et al); and 4,981,534 (Scheffee).
  • In the case of a mixture of an oxidizing gas and an inert gas, the combustion of a gaseous or liquid fuel with the oxidizing gas heats the stored gas and augments the stored gas for inflation of the airbag.
  • Control over the airbag inflation rate is desirable to minimize the forces a person experiences during dynamic response to an automobile collision. Control over the rate of heating the stored gas provides some measure of control over the rate of gas efflux from the inflator and, hence, the rate of airbag inflation. The extrusion of pyrotechnic materials into various shapes and their formulation to achieve certain burning rates may be used to control the rate of inflation. A disadvantage of using a totally inert gas and a pyrotechnic heater, however, is the production of objectionably high level of particulates to which the occupants of the automobile are subjected. Several criteria must be met by a pyrotechnic gas generant to be satisfactory for inflatable restraint systems. It must produce non-toxic, non-flammable and smokeless gas over a wide range of temperatures and other environmental conditions. The pyrotechnic must be safe to handle and must be capable of generating a large amount of gas within a very short time frame, i.e., about 35 milliseconds.
  • Some mixed gas systems have been proposed in which either a metal, a gas, or a liquid is used as the fuel. The use of a metal (see U.S. 5,230,532) suffers from the same particulates disadvantage as the pyrotechnic heater cartridge. The reaction of a gaseous fuel such as hydrogen (see U.S. 5,263,740) or a liquid is generally very rapid and does not allow for an easily controlled release of gas from the inflator. The orifice size in the inflator is sometimes the only control over the efflux rate. On the other hand, if the reaction rate of the gas or liquid is too slow, possibly toxic, unreacted components are exhausted into the airbag and thence into the automobile. In one embodiment of U.S. 5,263,740, a mixture of a flammable gas, an inert gas, and the amount of an oxidizing gas required for complete combustion of the fuel is used. In another, a pyrotechnic material containing PVC and a stoichiometric amount of oxidizer is used.
  • It is an object of this invention, therefore, to provide a hybrid gas generating system whereby the rate at which stored gas is heated depends on the rate at which a solid fuel, the source of the heat, is vaporized.
  • It is another object of this invention to provide a hybrid system in which the vaporization rate is the controlling factor rather than the relatively very fast combustion rate of the vaporized fuel.
  • It is another object of this invention to provide a pyrotechnic composition which contains an amount of oxidizer sufficient to vaporize the fuel therein.
  • It is a related object of this invention to provide an air bag inflator system wherein the level of solids in the inflating gas is very low.
  • It is a related object of this invention to provide a hybrid gas generating system wherein the rate of heating the stored gas is a function of the surface area of a solid pyrotechnic material in the system.
  • It is a related object of this invention to provide a hybrid gas generating system wherein the rate of heating the stored gas is a function of the linear regression rate of a solid pyrotechnic material in the system.
  • It is yet another object of this invention to provide a method for inflating an air bag by vaporizing an under-oxidized solid fuel composition and introducing the vaporized fuel into an oxygen-containing gas within a pressure vessel, wherein it is fully oxidized to generate sufficient heat to raise the pressure within the vessel and force the pressurized gas into the air bag.
  • These and other objects of the invention which shall become apparent from the following description of the invention are achieved by a method for inflating an air bag in an automobile by igniting an under-oxidized solid fuel composition in response to a signal from a deceleration sensor in the automobile, vaporizing said fuel with heat thus generated, introducing the vaporized fuel into an oxygen-containing gas within a pressure vessel, fully oxidizing the fuel in said gas, thereby generating sufficient heat to raise the pressure within the vessel and force the pressurized gas into an air bag communicating with the vessel.
  • The invention is further described as a hybrid gas generating system comprising a pressure vessel containing oxygen under pressure, a container adapted for communication with the pressure vessel, a solid combustible fuel having a heat of combustion of at least about 3500 calories per gram and an oxidizer within said container, said oxidizer being present in said container in an amount sufficient only to support combustion of the fuel to generate heat to vaporize the fuel, said amount being less than 60% of the stoichiometric amount required for the oxidation of all available carbon in said fuel to carbon dioxide and all available hydrogen in said fuel to water, an igniter for a mixture of the solid fuel and oxidizer, thereby causing said mixture to burn and increasing the pressure of the gas within the pressure vessel.
  • The solid fuel suitable for use in the pyrotechnic material of this invention has the empirical formula CxHyOzNu wherein x and y are positive integers, and z and u are independently zero or positive integers. The stoichiometric amount of oxidizer required for the oxidation of all available carbon in said fuel to carbon dioxide and all available hydrogen in said fuel to water is 2x + y/2-z moles of oxygen per mole of fuel. The level of oxidizer present in the under-oxidized formulations is preferably such that less than one gram of solid particulate is exhausted from a standard-sized airbag module when the fuel composition is oxidized by the internal oxidizer and the oxidizing gas. An airbag module is defined herein as an inflator device plus an inflatable airbag cushion.
  • Examples of a solid fuel suitable for the purposes of this invention include polyolefins, waxes, asphalts, and internally partially oxidized compounds such as sugars, polyesters, polyethers, acrylic polymers, phenols, polysaccharides, e.g., cellulose or starch, cellulose ethers, or cellulose esters, and nitrate salts of amines, nitramines, nitro compounds, nitrate esters, and mixtures of two or more of said compounds.
  • The heat of combustion of a suitable fuel is at least about 3500, preferably about 4000 or more, calories per gram. With reference to the empirical formula of a internally partially oxidized fuel, the ratio of the number of moles of oxygen present in the fuel molecule per the quantity (2 x moles of C + 0.5 x moles of H), or O/F ratio, is preferably from 0 to about 0.4. For example, the O/F ratio for methyl cellulose (C18H31O11) is 0.214 and its heat of combustion is-4960 calories per gram. The O/F for poly methylmethacrylate (C5H8O2) is 0.143 and its heat of combustion is -6530 calories per gram. Suitable solid fuels are exemplified by lactose, ethyl cellulose, hydroxyethyl cellulose, cellulose acetate, cellulose propionate, stearic acid, polyacetal, polyethylene, polypropylene, polystyrene, naphthalene, resorcinol, and a saturated linear polyester such as that sold under the BOSTIC 4156 trademark and number. All of the foregoing fuels are readily available from purveyors of commodity chemicals.
  • Any stable, solid inorganic oxidizer is suitable for the purposes of this invention. Examples of such suitable oxidizers include the sodium, potassium, lithium, and other alkali metal chromates, dichromates, nitrates, chlorates, and perchlorates. The corresponding ammonium salts are also useful. The selection of the oxidizer depends upon the type of solid fuel.
  • From 0 to about 50 % of the total weight of the solid pyrotechnic material may be a plasticizer such as the alkyl and alkoxyalkyl adipates, sebacates, phthalates, azelates, and nitrates.
  • Catalysts and burn rate modifiers are optional and, when used, the maximum amount is about 5% of the weight of the pyrotechnic material. Examples of such include boron hydrides and transition metal oxides such as copper oxide, manganese oxide, and vanadium oxide.
  • The rate of producing heat for the stored gas is a function of the surface area and the linear regression rate of the solid pyrotechnic material. The surface area may be tailored easily by the physical shape of the pyrotechnic. A granular pyrotechnic material will have a high surface area while cylindrical particles will have a small surface area. The shaping of the particles may be by extrusion, solvent extrusion, molding, spray drying and pelletization, or extrusion and spheronization.
  • The amount of oxygen in the stored gas must be sufficient to complete the oxidation of all available carbon in said fuel to carbon dioxide and all available hydrogen in said fuel to water. The oxygen-containing gas may be 100 % oxygen or a mixture of oxygen and an inert gas such as nitrogen or argon. Air is suitable.
  • Example 1
  • Conventionally, the oxidizer portion of a pyrotechnic composition is by far the major portion, the ratio of oxidizer to fuel being as high as 4:1 or even higher. When the combustion of the fuel is completed in an oxygen atmosphere, however, the total amount of pyrotechnic material can be reduced greatly along with the proportion of oxidizer. For example, a stoichiometric ratio of 30.00 % of a polyester, 16.16 % of potassium perchlorate, and 52.85 % oxygen is utilized in the heating of x grams of an oxygen/argon mixture in an inflator device when only 11.73 grams of an under-oxidized pyrotechnic material containing 65.73 % of polyester and 34.22 % of the perchlorate is burned in said mixture. In comparison, 28 grams of a stoichiometric formulation of polyester and potassium perchlorate (1:4 by weight) is required to heat x grams of argon. About 1 gram of solid residue is produced from the under-oxidized pyrotechnic material. The amount of solids in the inflating gas may be even less with certain formulations. The heat of reaction generated by the combustion of the under-oxidized pyrotechnic in the oxygen/argon mixture is greater than when all of the oxidizer is present in the pyrotechnic material.
  • Example 2
  • The stoichiometric formulation of the ethyl cellulose and potassium perchlorate is 19.7 : 80.3 parts by weight. An under-oxidized pyrotechnic material consisting of 80.5 parts by weight of ethyl cellulose and 19.5 parts by weight of potassium perchlorate is burned in a hybrid inflator containing an oxygen/argon mixture in a pressurized cylinder. The proportion of fuel, perchlorate and oxygen taking part in the combustion is 33.2 : 8.0 : 58.8. The combustion releases 1840 calories per gram of pyrotechnic material in one hundred grams of the combustion mixture. Thirty thousand (30,000) calories of heat are required for the inflation of a passenger side air bag by the hybrid inflator; thus, the inflation requires the combustion of 16.3 grams of the pyrotechnic material. About 1.7 grams of potassium chloride are produced.

Claims (16)

  1. A combustible gas generant comprising at least one solid fuel having a heat of combustion of at least 3500 calories per gram and an oxidizer in an amount sufficient to support combustion which generates sufficient heat to volatilize the fuel, said amount being less than 60% of the stoichiometric amount required for the oxidation of all available carbon in said fuel to carbon dioxide and all available hydrogen in said fuel to water.
  2. A composition according to claim 1 wherein the fuel has the empirical formula CxHyOzNu wherein x and y are positive integers, and z and u are independently zero or positive integers.
  3. A composition according to claim 1 or claim 2 wherein the fuel is selected from polyolefins, waxes, asphalts, internally partially oxidized compounds, and mixtures thereof.
  4. A composition according to claim 1 wherein the fuel is an internally partially oxidized compound selected from the group consisting of sugars, polyesters, polyethers, acrylic polymers, phenols, polysaccharides, amine nitrates, nitrate esters, nitramines, and mixtures thereof.
  5. A composition according to claim 1 or claim 2 wherein the fuel is a cellulose ether.
  6. A composition according to any preceding claim wherein the oxidizer is selected from nitrates, perchlorates, and chlorates of an ammonium ion, alkali metals, and alkaline earth metals, transition metal oxides, and mixtures thereof.
  7. A hybrid gas generating system comprising a pressure vessel containing oxygen under pressure, a container adapted for communication with the pressure vessel, a solid combustible fuel having a heat of combustion of at least 3500 calories per gram and an oxidizer within said container, said oxidizer being present in an amount sufficient only to support combustion of the fuel to generate heat to vaporize the fuel, and an igniter for a mixture of the fuel and oxidizer.
  8. A system according to claim 7 wherein said amount is less than 60% of the stoichiometric amount required for the oxidation of all available carbon in said fuel to carbon dioxide and all available hydrogen in said fuel to water.
  9. A system according to claim 7 or claim 8 wherein the oxygen in the pressure vessel is sufficient to complete the oxidation of all carbon in the vaporized fuel to carbon dioxide and of all hydrogen in the vaporized fuel to water.
  10. A system according to any one of claims 7 to 9 wherein the oxygen is mixed with an inert gas.
  11. A system according to any one of claims 7 to 10 wherein the fuel has the empirical formula CxHyOzNu wherein x and y are positive integers, and z and u are independently zero or positive integers.
  12. A system according to any one of claims 7 to 11 wherein the fuel is selected from polyolefins, waxes, asphalts, internally partially oxidized compounds, and mixtures of two or more such fuels.
  13. A system according to any one of claims 7 to 11 wherein the fuel is an internally partially oxidized compound selected from sugars, polyesters, polyethers, acrylic polymers, phenols, polysaccharides, amine nitrates, nitrate esters, nitramines, and mixtures of two or more of said compounds.
  14. A system according to any one of claims 7 to 11 wherein the fuel is a cellulose ether.
  15. A system according to any one of claims 7 to 14 wherein the oxidizer is selected from nitrates, perchlorates, and chlorates of an ammonium ion, alkali metals, and alkaline earth metals, transition metal oxides, and mixtures thereof.
  16. A system according to any one of claims 7 to 15 characterized further in that it is part of an inflator for a vehicle passenger restraint system.
EP96309042A 1995-12-13 1996-12-12 Fuel compositions for use in hybrid inflators containing stored oxidizing gas Withdrawn EP0779260A2 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US57150295A 1995-12-13 1995-12-13
US571502 1995-12-13

Publications (1)

Publication Number Publication Date
EP0779260A2 true EP0779260A2 (en) 1997-06-18

Family

ID=24283963

Family Applications (1)

Application Number Title Priority Date Filing Date
EP96309042A Withdrawn EP0779260A2 (en) 1995-12-13 1996-12-12 Fuel compositions for use in hybrid inflators containing stored oxidizing gas

Country Status (2)

Country Link
EP (1) EP0779260A2 (en)
JP (1) JPH09183682A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0930284A1 (en) * 1998-01-19 1999-07-21 Snpe Ablative solid material for hybrid gas generator
EP1935863A3 (en) * 2006-12-18 2014-12-03 Daicel Chemical Industries, Ltd. Hybrid inflator

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3608902B2 (en) 1997-03-24 2005-01-12 ダイセル化学工業株式会社 Gas generating agent composition and molded body thereof
JP2002166817A (en) 1999-10-01 2002-06-11 Daicel Chem Ind Ltd Hybrid inflator

Citations (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3692495A (en) 1970-06-19 1972-09-19 Thiokol Chemical Corp Gas generator
US3723205A (en) 1971-05-07 1973-03-27 Susquehanna Corp Gas generating composition with polyvinyl chloride binder
US3756621A (en) 1971-11-03 1973-09-04 Allied Chem Argon compressed gas supply
US3785149A (en) 1972-06-08 1974-01-15 Specialty Prod Dev Corp Method for filling a bag with water vapor and carbon dioxide gas
US3897285A (en) 1973-09-10 1975-07-29 Allied Chem Pyrotechnic formulation with free oxygen consumption
US3901747A (en) 1973-09-10 1975-08-26 Allied Chem Pyrotechnic composition with combined binder-coolant
US3912562A (en) 1973-09-10 1975-10-14 Allied Chem Low temperature gas generator propellant
US3950009A (en) 1972-02-08 1976-04-13 Allied Chemical Corporation Pyrotechnic formulation
US3964255A (en) 1972-03-13 1976-06-22 Specialty Products Development Corporation Method of inflating an automobile passenger restraint bag
US4128996A (en) 1977-12-05 1978-12-12 Allied Chemical Corporation Chlorite containing pyrotechnic composition and method of inflating an inflatable automobile safety restraint
US4981534A (en) 1990-03-07 1991-01-01 Atlantic Research Corporation Occupant restraint system and composition useful therein
US5230532A (en) 1992-03-20 1993-07-27 Trw Vehicle Safety Systems Inc. Apparatus for inflating a vehicle occupant restraint
US5263740A (en) 1991-12-17 1993-11-23 Trw Inc. Hybrid air bag inflator

Patent Citations (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3692495A (en) 1970-06-19 1972-09-19 Thiokol Chemical Corp Gas generator
US3723205A (en) 1971-05-07 1973-03-27 Susquehanna Corp Gas generating composition with polyvinyl chloride binder
US3756621A (en) 1971-11-03 1973-09-04 Allied Chem Argon compressed gas supply
US3950009A (en) 1972-02-08 1976-04-13 Allied Chemical Corporation Pyrotechnic formulation
US3964255A (en) 1972-03-13 1976-06-22 Specialty Products Development Corporation Method of inflating an automobile passenger restraint bag
US3785149A (en) 1972-06-08 1974-01-15 Specialty Prod Dev Corp Method for filling a bag with water vapor and carbon dioxide gas
US3912562A (en) 1973-09-10 1975-10-14 Allied Chem Low temperature gas generator propellant
US3901747A (en) 1973-09-10 1975-08-26 Allied Chem Pyrotechnic composition with combined binder-coolant
US3897285A (en) 1973-09-10 1975-07-29 Allied Chem Pyrotechnic formulation with free oxygen consumption
US4128996A (en) 1977-12-05 1978-12-12 Allied Chemical Corporation Chlorite containing pyrotechnic composition and method of inflating an inflatable automobile safety restraint
US4981534A (en) 1990-03-07 1991-01-01 Atlantic Research Corporation Occupant restraint system and composition useful therein
US4981534B1 (en) 1990-03-07 1997-02-04 Atlantic Res Corp Occupant restraint system and composition useful therein
US5263740A (en) 1991-12-17 1993-11-23 Trw Inc. Hybrid air bag inflator
US5230532A (en) 1992-03-20 1993-07-27 Trw Vehicle Safety Systems Inc. Apparatus for inflating a vehicle occupant restraint

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0930284A1 (en) * 1998-01-19 1999-07-21 Snpe Ablative solid material for hybrid gas generator
FR2773797A1 (en) * 1998-01-19 1999-07-23 Poudres & Explosifs Ste Nale SOLID ABLATABLE MATERIAL FOR HYBRID GAS GENERATOR
EP1935863A3 (en) * 2006-12-18 2014-12-03 Daicel Chemical Industries, Ltd. Hybrid inflator

Also Published As

Publication number Publication date
JPH09183682A (en) 1997-07-15

Similar Documents

Publication Publication Date Title
CA2181543C (en) Metal complexes for use as gas generants
US5542999A (en) Gas-generating mixture
US3964255A (en) Method of inflating an automobile passenger restraint bag
US5482579A (en) Gas generator compositions
KR100243443B1 (en) Two-part igniter for gas generating compositions
US4246051A (en) Pyrotechnic coating composition
US4909549A (en) Composition and process for inflating a safety crash bag
US4238253A (en) Starch as fuel in gas generating compositions
EP0400809B1 (en) Gas generant compositions containing salts of 5-nitrobarbituric acid, salts of nitroorotic acid, or 5-nitrouracil
US4244758A (en) Ignition enhancer coating compositions for azide propellant
US3910805A (en) Low temperature gas generating compositions
US5542998A (en) Gas-generating mixture
WO1998042642A1 (en) Gas generator composition and molding thereof
JP2009530226A (en) Gas generation using copper complex imidazole and derivatives
US5160386A (en) Gas generant formulations containing poly(nitrito) metal complexes as oxidants and method
US4203786A (en) Polyethylene binder for pyrotechnic composition
WO1998008716A1 (en) Use of mixed gases in hybrid air bag inflators
WO2007016594A2 (en) Autoignition/booster composition
US6550808B1 (en) Guanylurea nitrate in gas generation
EP0779260A2 (en) Fuel compositions for use in hybrid inflators containing stored oxidizing gas
JP3920773B2 (en) Gas evolution by metal complexes of guanylurea nitrate.
JP2002537208A (en) Gas generating substance
US6136111A (en) Combustible composition for use in vehicle safety systems
US6277221B1 (en) Propellant compositions with salts and complexes of lanthanide and rare earth elements
JPH1192265A (en) Gas generating agent composition for air bag

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

AK Designated contracting states

Kind code of ref document: A2

Designated state(s): DE FR GB IT

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: THE APPLICATION HAS BEEN WITHDRAWN

18W Application withdrawn

Withdrawal date: 19971017