Composition and process for inflating a safety crash bag

COMPOSITION AND PROCESS FOR INFLATING A SAFETY CRASR BAG ~... , ~ ., :

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BACKGROUND OF THE INVENTION 1.

Field of the invention This invention relates to a composition and process for inflating a safety crash bag. -~ 2.

Description of the prior art .

In the prior art, the generation of nitrogen gas in order to fill an airbag for use as an aircraft or automobile safety crash bag has involved the use of azide compounds.

Azide compounds such as sodium azide are highly toxic materials prior to combustion.

Such azide salts also reatily react with heavy metals such as copper, lead, etc. to form extremely sensitive solids that are sub~ect to unexpected ignition or detonation and therefore require special handling ln the manufacture, storage and disposal of such compounds.

Methots oi generating nitrogen gas to fill a safety crash bag using metal salts of 5,5'-bitetrazole with oxidizers which contain no oxygen in the molecule are disclosed in U. S.

Patent No. 4,370,181 to Lundstrom et al.

The prior art use of tetrazole compounds with oxjgen containing oxidizers are dismissed in view of the fact that such compositions do not meet the present .. ..

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2014603 requirements for the generation of gases which are able to meet the industrial standards for toxicity with respect to such gases as carbon monoxide, carbon dioxide, etc.

The disclosure of prior art non-azide nitrogen gas generants by Lundstrom et al are to various hydroxamine acid and hydroxylamine deriva~ives, various polymeric binders, hydrocarbons and carbohydrates which are oxidized to produce non-corrosive and, often termed, "non-toxic" gases.

In addition, Lundstrom et al dis~lose as other approaches to non-azide nitrogen gas generants utilizing tetrazole compounds such as aminotetrazole, metal salts of aminotetrazole, or other tetrazole salts which contain hydrogen in the molecule.

These are used in combination with oxygen containing oxidizers such as potassium perchlorate.

Upon combustion, these compositions tend to form various toxic species such as hydrogen cyanide, nitrogen oxides, and carbon monoxide in unacceptable proportions so as not to meet the present toxicity requirements for the ~0 non toxicity of the gas generated.

In U. S.

Patent No. 4,369,079 to Shaw, solid, non-azite nitrogen gas generant compositions for inflation of a safety crash bag are disclosed as consisting essentially of a metal salt of a non-hydrogen containing a tetrazole compound in admixture with an oxidizer containing nitrogen.

The specific tetrazole which is tiscloset as useful is azobitetrazole.

In U. S.

Patent No. 3,910,595, an apparatus is describet for aspirating air into a gas mixture used to inflate a crash restraint device.

20l~6a~ SUMMARY OF THE INVENTION A composition and process is disclosed for inflating an airbag su~table for a number of purposes including use as a safety crash bag in aircraft or automobiles in which a primary source of gas is generated by the ignition of pellets prepared from a dry blend of at least one tetrazole or triazole compound, at least one oxygen containing oxidizer, and at least one metal oxide.

By the method of the invention it is possible to form easily filterable solids and to obtain a substantially higher yield of gas for use in inflating the crash bag by the provision of passing the gas mixture generated upon ~ombustion of said pellets ~ through a venturi so as to aspirate outside air to form a gas mixture which is then used to inflate the crash bag.

The method of the invention overcomes the disadvantages referred to above in the discussion of the prior art relating to the use of certain non-azide gas generant mixtures consisting of tetrazole compounds or mixtures thereof, such as aminotetrazole, triazole compounds such as 1,2,4-triazole-5-one, metal salts of aminotetrazole, or other tetrazole salts which contain hydrogen ln the molecule in combination with oxygen containing oxidizers.

While the gases produced upon combustion of such generant mixtures may contain higher amounts of toxic species of gases than are presently acceptable for use in inflating air bags, by the novel provision of diluting the primary source of gas ~O (produced upon combustion) with a secondary source of 2014603 gas tair~, acceptable levels of the toxic species are obtained thus making such gas generants practical.

Both tetrazole and triazole compounds are useful in the composition and process of the invention.

The useful tetrazole compounds include aminotetrazole, metal salts of tetrazole, other tetrazole salts containing hydrogen in the molecule, and metal salts of such hydrogen containing tetrazoles. DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT OF THE INVENTION The present ~nvention relates to a composition and process for inflating a crash bag utilizing a mixture of at least one of a triazole or a tetrazole compound, at least one oxygen containing oxidizer, and at least one metal oxide.

Upon combustion of this mixture at elevated pressure, a primary gas mixture is fonmed which when passed through an aspirating venturi draws in about 1 to about 4 volumes of outside air for use in cooling the primary gas mixture and diluting the primary gas mixture, thus producing a final gas mixture in which the substantially non-toxic primary gas mixture is reduced below unacceptable levels and permitting the use of triazole or tetrazole compounds which have safety and toxicity advantages over the azide compounds used in the prior art.

Generally, combustion of the pyrotechnic compositions of the invent~on takes place at an elevated pressure of about 100 psi to about 3000 psi, preferably, about 500 psi to about 2500 psi, and most preferably, about 750 psi to about 2000 psi is used.

There is a 2014603 substantial safety advantage in the use of the compositions of the invention over the use of compositions based on more readily combustible azide compounds, such as sodium azide, as a basis for the generation of a gas mixture comprising nitrogen gas for the inflation, for instance, of an automobile safety crash bag.

In addition, the triazole and tetrazole compounds are relatively nontoxic and therefore much more suitable for use in this application than the azide compounds, which are highly toxic.

Thus, the triazole and tetrazole compounds in admixture with said oxidizer compounds require less special handling in the manufacture, storage and eventual disposal than is the case with the gas generants prepared from azide compounds which are toxic.

An especially useful oxidizer compound is a mixture of ammonium perchlorate and sodium nitrate in a 1 to 1 mole ratio so that the sodium and chlorine combine during combustion to form the harmless sodium chloride.

An excess of chlorine must be avoided since toxic gases such as hydrogen chloride would be formed.

A small excess of sodium can be tolerated since it would resùlt in the formation of sodium carbonate.

Other useful oxidizing compounds are salts such as the ammonium, alkali metal, and alkaline earth metal nitrateQ and perchlorates.

The proportion of gas generant compound utilized in admixture with an oxygen containing oxidizer compound is generally about 20 to about 60% by weight of tetrazole or triazole compound in ~01460~ combination with about 20 to about 80% by weight of said oxidizer compound.

In general, the ratio of oxidizer to the tetrazole or triazole compound must be adjusted to provide an excess of oxygen after all carbon and hydrogen have been oxidized to form carbon dioxide and water.

The amount of excess oxygen required is about 1 to 25Z by volume in the ga~i formed upon combustion.

By the inclusion of a metal oxide in the pyrotechnic mixture of the invention, more easily filterable solid combustion products are formed.

For instance, use of silicon dioxide together with the reduction of the oxidizer compound, ammonium perchlorate, results in the formation, upon combustion of the pyrotechnic mixtures of the invention, of metal silicate ~iolids ~instead of metal chlorides) which are more easily filtered out of the gas produced upon combustion.

In addition, the formation of metal silicates avoids the formation of metal carbonates, thus allowing the carbon dioxide produced upon combustion to contribute as a component of the gas produced for inflation of the crash bag. A preferred metal oxide compound is silicon dioxide.

Other similarly useful metal oxides which are representative of the metal oxide compound are: iron oxide, cobalt oxide, nickel oxide, chromium oxide, aluminum oxide, boron oxide, and vanadium oxide.

Upon combustion, these metal oxides are converted, respectively, to metal silicates, metal ferrates, metal cobaltates, metal nickelates, metal ~014603 chromates, metal aluminates, metal borates, and metal vanadates.

By the method of the invention, the primary gas mixture formed upon combustion at elevated pressure of the pyrotechnic mixture of said tetrazole or triazole compound, said metal oxide, and said oxygen containing oxidizer compound, is generally diluted to form a final gas mixture with about 1 to about 4 volumes of air, preferably, about 1 to about 2.5 volumes of air.

The amount of dilution with air of the gas mixture, formed upon combustion, is dependent upon several factors including the temperature of the primary gas mixture, the molecular weight of the primary gas mixture and the design of the aspirator utilized.

Any toxic gases in the primary gas mixture upon dilution with air would be decreased by a factor of about 2 to about 5 upon dilution with outside air.

The final diluted gas mixture generally contains about 2 to about lOX by volume, preferably less than about 5% by volume carbon dioxide, less than about 4X by volume hydrogen, and less than about 50%, preferably less than about 20% by volume of water.

The use of tetrazole compounds such as tetrazole, aminotetrazole, metal salts of tetrazole or aminotetrazole, or other tetrazole salts which contain hydrogen in the molecule in admixture with oxygen containing oxidizer compounds such as potassium perchlorate have been dismissed as unsuitable by workers in the prior art on the basis that such mixtures, when burned, tend to form small amounts of various toxic ~146~3 species (in addition to nitrogen) such as hydrogen cyanide, nitrogen oxides, and carbon monoxide.

Nevertheless, such mixtures have been found to be eminently satisfactory, upon dilut~on with outside air, to inflate a crash bag.

Representative useful triazole compounds are 1,2,4-triazole; 1,2,4-triazole-5-one; and 3-nitro-4,5-dihydro-1,2,4,-triazole-5-one.

The use of a gas mixture comprising a primary gas mixture diluted with a secondary gas mixture (air) to inflate a crash bag provides several advantages, namely, the primary gas mixture is cooled substantially by such dilution, thus avoiding the potential for burning the occupants of the aircraft or automobile in which the crash bag is utilized.

In addition, the air dilution of the primary gas mixture reduces the level of toxic species present to much lower levels, which are acceptable.

Thus the use of tetrazole or triazole compounds containing hydrogen in the molecule is practical, since the concentration of hydrogen in the gas produced can generally be reduced by oxidation to very low levels, generally less than 4% by volume, by the formation of water.

In addition, the level of water in the gas mixture can be reduced to about less than about 20X by volume, preferably to about 2% to about 20% by volume, depending upon the gas generant composition used.

The use of hydrogen containing tetrazoles and triazoles as gas generant compounds is particularly advantageous in con~unction with a system in which out8ide air is aspirated so as to form a mixture with ~01~03 the ~as generated by combustion of the hydrogen containing ~etrazoles and triazoles in that water is formed in the combustion of the tetrazoles and triazoles Water has a low molecular weight and is non toxic. A low molecular weight in the gases for~ed upon combustion is especially desirable in a system in which aspiration of outside air is utilized.

In order to prepare the gas generating compositions utilized in the process of the invèntion, the components, for instance, the sodium salt of tetrazole, and the oxygen and chlorine containing oxidizer compound, for instance, a mixture of ammonium perchlorate and sodium nitrate, can be dry blended as powders by standard methods.

The components can also be lS blended with other additives for burning rate improvement or adjustment and for improving the propellant grain processing properties.

The blended powder can, if desired, be compressed into granules, or pellets by conventional techniques.

Since the components of the gas generating composlt~on used in the process of the invention are not highly toxic or highly reactive and ignite readily only at elevated pressure, special handling techniques, beyond those required in the use of ordinary solid propellants (to minimize exposure because of toxicity or contamination which might increase reactivity) are not required in the fabrication of the gas generating compositions used or in the pelletizing thereof.

One skilled in the art will recognize that at least one of any other alkali metal, an alkaline earth 201~603 metal or an ammonium salt of a tetrazole containing hydrogen or an alkali metal, an alkaline earth metal, or an ammonium salt of an aminotetrazole or a triazole can be substituted for the metal salt in the below Examples S or, alternatively, a hydrogen containing tetrazole, aminotetrazole, or triazole compound can be utilized per se in admixtures with at least one metal oxide and an oxygen containing, preferably an oxygen and chlorine containing oxidizing compound in the preparation of granules or pellets by conventional techniques.

The oxidizing compound is exemplified by an alkali metal or alkaline earth metal nitrate or perchlorate or mixtures of alkali metal or alkaline earth metal nitrates with ammonium perchlorates.

One skilled in the art will also recognize that catalysts or combustion rate modifiers can be used or added in addition to the oxygen containing oxidizing compound described above.

Thus, additional catalyst compounds such as vanadium pentoxide, copper oxide, and iron oxide may be substituted or added to the mixture to be pelletized.

Preferably, an oxidizer compound or oxidizer compound mixture can be selected which will result in complete conversion of any metal (whether contained ln the oxidizer, the metal oxide, or in the combustion compound used as fuel) to the chloride salt or metal oxide salt.

Thus, a metal salt such as the sodium salt of tetrazole can be reacted with an equimolar quantity of ammonium perchlorate in order to convert all of the sodium to sodium chloride.

In order to provide the additional oxygen required to oxidize the carbon to 2014603 carbon dioxide and the hydrogen to water, an oxidizer balanced to produce a metal salt can be used.

For example, an equimolar mixture of ammonium perchlorate and sodium (or potassium) nitrate can be used.

Alternatively, a metal perchlorate or chlorate can be used such as potassium perchlorate.

Reduction or elimination of the amount of ammonium perchlorate used in the pyrotechnic mixture of the invention can be desirably accomplished by the use of a metal oxide as a component of the mixture.

Upon combustion of such a mixture, for instance, containing silicon dioxide as the metal oxide, the solids produced are metal silicates~ which are easily filterable, as compared to the metal chlorides, which are produced when the combustible mixture does not contain a metal oxide.

Ammonium perchlorate, although a good oxidizer, is not useful as the sole oxidizer since it will produce hydrogen chloride or other toxic products if not balanced by the presence of a metal such as sodium or potassium, Alkali metal nitrates such as sodium or potassium nitrate can be used without a chlorine containing oxidizer but the products obtained upon combustion must be carefully evaluated in order to avoid disadvantageous results.

In general, unless a metal oxide is present in the pyrotechnic composition of the invention, a metal carbonate such as sodium carbonate can be formed upon combustion by the use of a metal nitrate oxidizer compound.

The formation of such a salt is also disadvantageous because, in the formation of said salt, carbon dioxide is removed as a component 2014603 from the gases formed upon combustion.

Carbon dioxide is a useful gas for inflating a crash bag since it has a relatively low toxicity.

In addition, if not enough carbon dioxide is available in the gas formed upon combustion, then other hazardous products can be formed such as sodium or potassium oxide.

The use of a metal oxide as a component of the compositions of the invention thus overcomes the disadvantageous effect of the use of a metal nitrate oxidizer compound.

It is believed that the use of oxidizers which are balanced to produce some metal chloride salt, particularly, a sodium or potassium chloride salt, result in an additional safety advantage, as compared with the use of oxidizer compounds which do not produce a metal chloride salt, because the gas generants prepared from such oxidizers in combination with the tetrazole compounds disclosed as useful in the process of the invention burn with difficulty at atmospheric pressure but burn vigorously at elevated pressures.

This unexpected result is not fully understood but it is assumed that the salt vapor formed during combustion quenches the flame at low pressures but not at higher pressures.

Although many satisfactory ignition mechanisms wlll occur to one skilled in the art, a particularly convenient and preferred igniter composition consists of a mixture of boron and potassium nitrate which is well known to those skilled in the art as BKN03.

Other ignitor compositions such as mixtures of potassium perchlorate, ammonium perchlorate, and aluminum powder 12 2014603 are also suitable.

Firing of the ignitor composition may be accomplished utilizing standard electrical means including any desired safety devices in the circuitry, such as spark gaps and/or ferrite resistors to prevent 5unwarranted initiation from strong radio frequency or high voltage sources.

The process of the invention can utilize conventional gas generator mechanisms of the prior art.

These are referred to in V. S.

Patent No. 4,369,079.

10Other more suitable gas generating devices are envisioned.

Generally, the methods of the prior art involve the use of a hermetically sealed metallic cartridge containing the pyrotechnic material, the oxygen containing oxidizer, 15and an initiator.

Upon initiation of combustion by the firing of a squib, the sealing mechanism ruptures.

This allows gas to flow out of the combustion chamber through several orifices and into an aspirating venturl through which outside air is drawn into the gas formed upon ~0combustion so that the gas utilized to inflate the airbag is a mixture of outside air (secondary gas source) and the gaseous mixture formed upon ignition ~primary gas source) which together constitute the total amount of inflation gas.

25When utilizing the gas generating compositions described above, a less efficient filter is required because the solids formed upon combustion in the process of the invention are easily filtered out.

The solids consist, for example, of solids such as sodium chloride, 30sodium silicate, and potassium chloride.

Such solids of 13 ., ~ .I : ':, :. ' ::

201~603 low toxicity are generally referred to as nuisance particulates.

The following Examples illustrate the various aspects of the invention but are not intended to limit its scope.

Where not otherwise specified throughout this specification and claims, temperatures are given in degrees centigrade and parts, percentages, and proportions are by weight except for gases in which case percentages are by volume. ExamPle 1 A mixture of the sodium salt of tetrazole, ammonium perchlorate, and sodium nitrate was prepared having the following composition in percent by weight:

34X sodium sslt of tetrazolea 38.3% ammonium perchlorate~ and 27.7Z sodium nitrate.

These powders were dry blended and pellets were prepared by compres~ion molding.

The pellets would not su~tain combustion upon repeated ignition at atmospheric pressure using a propane-oxygen torch but continued burning when ignited under a helium pressure of 300 psi.

Subsequent burning rate measurements at a pressure of 1000 psi indicated a burning rate of about 2 inches per second.

The combustion temperature of this mixture is theoretically 3345F.

The primary gas composition protuced upon combustion contained 45.4Z wt. of nltrogen, 9X by wt. of carbon dioxide, 34.5Z of water, and 11.1% by wt. of oxygen.

The solit residue formed upon combustion consisted of sodium chloride and sodium carbonate.

When this primary gas composition is diluted with 2.5 volumes of air to each volume of the primary 14 2014603 gas produced upon combustion, the water content of the mixture is reduced to 9.9% by volume and the carbon d~oxide content of the mixture is reduced to 2.6% by volume.

Example 2 A mixture of 5-aminotetrazole, ammonium perchlorate, and sodium nitrate was made by dry blending - and pellets were formed upon compression molding~ The ~ percent by weight compoYition of the mixture was: 34% 5-aminotetrazoleS 38.3X ammonium perchlorate; and 27.7Z of sodium nitrate.

The pellets would not sustain combustion at atmospheric pressure but burn completely when pressurized to 300 psi with helium.

The burning rate measured at 1000 psi. was 0.53 inches per second.

~5 The combustion temperature i~ theoretically 4300F and the primary gas compositlon produced upon combustion contains 42.9Z by volume nitrogen, 12.9% by volume carbon dioxide, 40.3X by volume water, and 3.7% by volume oxygen.

The solid residue produced upon combustion was sodium chloride.

Upon dilution with air at a ratio of 2.5 to 1 a water content of 11.5% by volume i~ obtained and a carbon dioxide content of 3.7% by volume i8 obtained.

Example 3 The mixture described in Example 2 was modified by addition of 0.5X by weight of iron oxide (Fe203).

The final composition used in percent by weight was: 34X 5-aminotetrazole, 38.05% ammonium perchlorate, 27,45~ sodium nitrate, and O.5Z iron oxide.

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' ' 2014603 This mixture was dry blended and pellets were formed by compression molding.

The pellets when ignited at atmospheric pressure continued to burn slowly.

The burning rate measured at lC00 psi was found to be 0.77 inches per second.

Example 4 A mixture as described in Example 3 was prepared except that vanadium pentoxide (V20s-~ was substituted for iron oxide~ The mixture was dry blended and pellets were formed by compression molding.

The pellets continued to burn slowly when ignited at atmospheric pressure.

The burning rate measured at 1000 psi was found to be 0.56 inches per second.

Example 5 A mixture of 40% by weight of the sodium salt of tetrazole, 49.7% by weight of sodium nitrate, and 10.3Z by weight of silicon dioxide was dry blended and pellets were formed by compression molding.

When lgnitet at atmospheric pressure, the pellets burned completely and very rapidly.

The burning rate measured at 1000 p8i was found to be 1.5 inches per second.

The combustion temperature of this mixture is theoretically 3432F and the primary gas composition produced at combustion contains 72.2% by volume nitrogen, 6% by ~5 volume carbon dioxide, 16.9% by volume water and 4.9% by volume oxygen.

The solid products formed upon combustion consist of sodium carbonate and sodium silicate.

When the primary gas composition is diluted with 2.5 volumes of air to each volume of primary gas 16 2014603 formed, the waeer content of the diluted mixture is 4.8% by volume and the carbon dioxide content is 1.7% by volume.

Example 6 A mixture of 30Z by weight of 1,2,4-triazole5-one, 40.4% by weight ammonium perchlorate, 29X by weight sodium nitrate, and 0.5~ by weight vanadium pentoxide was dry blended and pellets were formed by compression molding.

When ignited at atmospheric pressure, the pellets continued to burn slowly.

The burning rate measured at 1000 psi was found to be 0.37 inches per second.

The theoretical combustion temperature of this mixture is 4309F and the primary gas composition produced at combustion contains 30.5% by volume nitrogen, 24.6% by volume carbon dioxide, 42.5% by ~olume water, and 2.4% by volume oxygen.

The solid product formed by combustion is sodium chloride.

When the primary gas is diluted with 2.5 volumes oi air to each volume of primary gas, the water content is reduced to 12.2% by volume and the carbon dioxide is reduced to 7X by volume.

Example 7 A mixture of 30% by wt. of 5-aminotetrazole, 54X by wt. of potassium nitrate, and 16% by wt. of silicon dioxite was dry blended and pellets were formed by compression molding.

Burning rate measurements at 1000 p~i indicated a burning rate of about 0.82 inches per second.

The combustion temperature of this mixture i8 theoretically 3500F.

The primary gas composition 201460.

produced upon combustion contained (by volume) 55% nitrogen, 17X carbon dioxide, 25% water and 2.4X oxygen.

The solid product which is produced upon combustion is potassium silicate.

Example 8 A mixture of 20.7% by wt. of 5-aminotetrazole, 35.lZ by wt. of ammonium perchlorate, 41Z by wt. of potassium nitrate, and 3.2X by wt. of silicon dioxide was dry blended and pellets were formed by compression molding.

Burning rate mea~urements at a pressure of 1000 psi indicated a burning rate of about 0.63 inches per second.

The combustion temperature of this mixture i8 theoretically 3100F.

The primary gas produced by combustion contains (by volume) 37% nitrogen, 9Z carbon dioxide, 37% water, and 17X oxygen.

The solid products produced upon combustion are potassium chloride and potassium s~licate.

Examples 9-15 Example 7 is repeated substituting individually for silicon dioxide an equal amount of the oxides of iron, cobalt, nickel, chromium, aluminum, boron or vanadium.

Similar results are obtained.

The solid product formed is a salt of potass~um and the residue of the metal oxide used in the pyrotechnic mixture, ior ~nstance, potassium ferrate, potassium cobaltate, potassium nickelate, potassium chromate, potassium aluminate, potassium borate, and potassium vanadate.

2014603 Examples 16-22 Example 8 is repeated substituting individually for the silicon dioxide an equal amount of the oxides of iron, cobalt, nickel, chromium~ aluminum, boron, or vanadium.

Similar results are obtained.

The solid product formed upon combustion is potassium chloride and respectively a salt of the residue of the metal oxide used in the pyrotechnlc material with potassium, namely, potassium ferrate, potassium cobaltate, potassium nickelate, potassium chromate, potassium aluminate, potassium borate, and potassium vanadate~ While the preferred embodiment of the invention has been disclosed, it should be appreciated that the invention is susceptible of modification without departing from the scope of the following claims. :

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