Gas-generating substances

Bley, Ulrich ;   et al.

Patent Application Summary

U.S. patent application number 10/807289 was filed with the patent office on 2004-11-25 for gas-generating substances. Invention is credited to Bley, Ulrich, Brede, Uwe, Hagel, Rainer, Redecker, Klaus.

Application Number20040231770 10/807289
Document ID /
Family ID33454070
Filed Date2004-11-25

United States Patent Application 20040231770
Kind Code A1
Bley, Ulrich ;   et al. November 25, 2004

Gas-generating substances

Abstract

The invention relates to a gas-generating substance which consists of nitrous oxide and/or nitrogen monoxide and one or more combustibles which are solid at room temperature and normal pressure.


Inventors: Bley, Ulrich; (Nurnberg, DE) ; Brede, Uwe; (Furth, DE) ; Hagel, Rainer; (Erlangen, DE) ; Redecker, Klaus; (Numberg, DE)
Correspondence Address:
    ANTONELLI, TERRY, STOUT & KRAUS, LLP
    1300 NORTH SEVENTEENTH STREET
    SUITE 1800
    ARLINGTON
    VA
    22209-9889
    US
Family ID: 33454070
Appl. No.: 10/807289
Filed: March 24, 2004

Related U.S. Patent Documents

Application Number Filing Date Patent Number
10807289 Mar 24, 2004
09913533 Dec 10, 2001
09913533 Dec 10, 2001
PCT/EP00/00274 Feb 15, 2000

Current U.S. Class: 149/46 ; 149/61
Current CPC Class: C06B 23/008 20130101; C06D 5/10 20130101
Class at Publication: 149/046 ; 149/061
International Class: C06B 031/02; C06B 031/28

Foreign Application Data

Date Code Application Number
Feb 19, 1999 DE 199 07 241.8

Claims



What is claimed:

1. Gas-generating substance for a motor vehicle safety device, comprising a mixture of N.sub.2O, NO and one or more fuels which are solid at room temperature and standard pressure.

2. Gas-generating substance according to claim 1, characterised in that it additionally contains, in order to control the reactivity of the gases, at least one inert gas selected from the group consisting of carbon dioxide, air, helium, neon and/or argon.

3. Gas-generating substance according to claim 1, characterised in that it contains additions of smell-intensive gases in small amounts for detecting leaks.

4. Gas-generating substance according to claim 1, characterised in that it contains additions for improving the smell properties of the combustion gases in the when utilization takes place.

5. Gas-generating substance according to claim 4, characterised in that the additions for improving the smell properties of the combustion gases comprise vanillin.

6. Gas-generating substance according to claim 1, characterised in that the one or more fuels comprise polymers of a material selected from the group consisting of ethylene, propylene, isoprene, and styrene.

7. Gas-generating substance according to claim 1, characterised in that the one or more fuels comprise oxygen-containing fuels derived from a material selected from the group consisting of polyvinyl acetates, polymethacrylates, polyterephthalates, polyesters, polyethers, polycarbonates, polyoxymethylenes, oligosaccharides, polysaccharides, cellulose, starch, polyvinyl acetals and polyvinyl alcohols.

8. Gas-generating substance according to claim 1, further comprising explosive substances as additional reactive components of the fuels.

9. Gas-generating substance according to claim 1, further comprising one or more compounds selected from the group consisting of nitroguanidine (NiGu) 5-aminotetrazole, 5-aminotetrazole nitrate, bistetrazole amine, bistetrazole, aminoguanidine nitrate, diaminoguanidine nitrate, triaminoguanidine nitrate, guanidine nitrate, dicyanodiamidine nitrate, diaminoguanidine azotetrazolate, nitrotriazolone, dicanediamicune nitrate, hexogen, and octogen.

10. Gas-generating substance according to claim 1, further comprising an additional fuel selected from the group consisting of urea, fumaric acid, ascorbic acid, oxalic acid, cork, wood, aluminium, titaniumboron, silicon, nitrides, azides and B.sub.3N.sub.3.

11. Gas-generating substance according to claim 1, characterised in that the one or more fuels are in the form of powder, granules, pressings, cut fibres, twisted fibres, mats, woven fabrics, or porous foams.

12. Gas-generating substance according to claim 1, characterised in that the one or more fuels are surface-treated by being impregnated or mixed with liquids or pasty substances, to control the burn-off.

13. Gas-generating substance according to claim 1, further comprising a catalyst selected from the group consisting of ferrocene and derivatives, iron acetylacetonate and copper acetylacetonate.

14. Gas-generating substance according to claim 1, further comprising one or more oxidising agents selected from the group consisting of nitrates of alkali and alkaline earth elements, perchlorates of alkali and alkaline earth elements, ammonium nitrate, ammonium perchlorate, zinc peroxide, perborates, peroxodisulphates, permanganates, tin dioxide, manganese dioxide, oxidising agents derived from nitramines and mixtures of these components.

15. Gas-generating substance according to claim 3, wherein the smell-intensive gases comprise a mercaptan.

16. Gas-generating substance according to claim 1, further comprising a porosity generator selected from the group consisting of ammonium hydrogencarbonate, acetone dicarboxylic acid, azoiso-butyronitrile and hollow plastics spheres.
Description



[0001] The invention relates to gas-generating substances, in particular for gas generators in belt tighteners and inflatable air-bags for protecting the occupants of motor vehicles against injuries.

[0002] With the gas generators currently used for inflatable air-bags, a gas charge in tablet or disc form or as granules or e.g. in noodle form is used as a combustible gas-evolving material. During burn-off, this gas charge generates the useful or compressed gas for the inflation of the air-bag. The disadvantage of the combustion of solid gas-evolving materials is the extremely high amount of slag produced during the combustion, which may make up more than 50% of the gas charge material used. Because of the slag and dust formed during the combustion, complicated filter stages are required in the gas generator in order to retain slag and dust particles. Otherwise the air-bag would be damaged during the discharge of these particles and the occupants may be exposed to danger.

[0003] As an alternative to these gas charges, generators containing compressed gases or air exist. Very high charging pressures are required for the formation of a sufficient gas volume, since cooling takes place during the outflow of the gases and no increase in volume is achieved through exothermic reactions as in the case of solid mixtures. In order to offset the cooling, a solid propellant fuel is frequently used, which ensures the operation of the gas generator merely through the heat of reaction during its burn-off and the additional gas evolution.

[0004] The invention is based on the object of providing a gas-evolving material for a gas generator, in particular for a belt tightener for an inflatable air-bag for protecting the occupant of a motor vehicle against injuries, where slag retention equipment is not required for the gas-evolving material.

[0005] The achievement of the aforementioned object consists in a mixture of laughing gas as oxidising agent and one or more fuels that are solid under the usual conditions (room temperature and standard pressure). Used as a gas-evolving material is laughing gas (N.sub.2O) as oxidising agent in combination with solid fuels or mixtures which react after ignition in a controlled manner in the combustion chamber to form slag-free or largely slag-free gaseous reaction products. The pressurised laughing gas is ignited together with the solid fuels by an ignition device containing an ignition charge. Use may be made as an ignition charge, for example, of an exploding wire or an ignition bridge, optionally with reinforcement with a booster charge, to produce a particle-rich, hot flame.

[0006] The ignition fumes and hot combustion gases ignite the gas/solid mixture. The latter burns in the combustion chamber without solid particles remaining. Filter stages that are positioned before at least one outlet opening of the gas generator housing wall may therefore be dispensed with when the gas/solid mixture according to the invention is used. If filter stages are provided, the latter serve exclusively cooling purposes. The cooling may also be carried out in another manner, however, by, for example, fitting downstream of the combustion chamber a distribution compartment of the housing, from which the combustion gases pass to the outside via at least one outlet opening.

[0007] According to the invention gases or gas mixtures with low intake pressure are proposed, which, as a result of exothermic conditions, produce a manifold increase in volume on burn-off and require no filters of any kind. The gas or gas mixture usable according to the invention consists of the oxidising agent. In order to avoid high intake pressures, oxygen or air is dispensed with as oxidising agent. In dinitrogen monoxide (laughing gas) there exists a gas which may be easily liquefied (critical pressure: 72.7 bar, critical temperature: 36.4.degree. C.). The oxidising capacity is twice as high as that of air and in contrast to pure oxygen or air, laughing gas behaves up to at least 200.degree. C. as an inert gas, as a result of which quiescent oxidising processes are prevented even during storage at high temperature. Nitrogen monoxide (NO/N.sub.2O, critical pressure 64 bar, critical temperature -93.degree. C.) may also be used in a mixture with laughing gas or as a gaseous oxidising agent on its own. In order to control the reactivity of the gases, inert gases (carbon dioxide, air, helium, neon, argon) may be added. The use of nitrogen monoxide has the advantage that there is no formation of condensed portions which first have to evaporate during the burn-off reaction. Additions of smell-intensive gases such as e.g. mercaptans in small amounts may make a rapid detection of leaks possible. The addition of e.g. vanillin improves the smell properties of the burn-off fumes in the application case.

[0008] According to the invention, used as fuels are polymers from the group of the hydrocarbons, such as ethylene, propylene, isoprene, styrene, as well as those which may also contain oxygen and are derived from e.g. carboxylic acids such as polyvinyl acetates, polymethacrylates, polyterephthalates and other polyesters, polyethers, polycarbonates, and also polyoxymethylene, oligo- and polysaccharides such as sugar, cellulose, starch, polyvinyl acetals or polyvinyl alcohols. In addition, however, further polymers of different compositions are also usable, provided the reaction products do not contain any dangerous components in an inadmissible amount, such as e.g. HCl, HCN, HF or phosgene. Explosive substances may also be used as additional reactive components of the fuels. Examples are nitroguanidine (NiGu), derivatives of tetrazole such as 5-aminotetrazole, 5-aminotetrazole nitrate, bistetrazole amine or bistetrazole, aminoguanidine nitrate, diaminoguanidine nitrate, triaminoguanidine nitrate, guanidine nitrate, dicyanodiamidine nitrate, diaminoguanidine azotetrazolate, nitrotriazolone, dicanediamidine nitrate, hexogen, octogen. The following may be used, for example, as further fuels: urea, organic acids (e.g. fumaric acid, ascorbic acid, oxalic acid), cork, wood, metals (e.g. aluminium, titanium) and non-metals (e.g. boron, silicon), nitrides, azides or inorganic benzene (B.sub.3N.sub.3). The fuels may be applied in the form of powder, granules, pressings such as e.g. tablets, or in the case of polymers e.g. also as cut fibres or twisted fibres, mats, woven fabrics, porous foams e.g. of polyurethanes. To control the burn-off, the specific embodiments may be surface-treated by being impregnated or mixed with liquids or pasty substances (inhibitors).

[0009] Further additives catalysts may be used, for example ferrocene and derivatives, iron or copper acetylacetonate and/or oxidising agents such as, for example, nitrates of alkali and alkaline earth elements, perchlorates of alkali and alkaline earth elements, ammonium nitrate, ammonium perchlorate, zinc peroxide, perborates, peroxodisulphates, permanganates, tin dioxide, manganese dioxide, oxidising agents derived from the nitramines and mixtures of these components and/or porosity generators, such as for example ammonium hydrogencarbonate, acetone dicarboxylic acid, azoisobutyronitrile and/or hollow plastics spheres.

[0010] The ratio by weight of the fuels to dinitrogen monoxide is preferably adjusted in such a way that a non-combustible gas mixture is obtained after the reaction. Accordingly the ratio by weight of the fuels to dinitrogen monoxide should be adapted to the stoichiometric proportions of a (where possible) complete combustion. Dinitrogen monoxide is therefore used to advantage in a slight excess, referred to the fuel. The reaction products then consist substantially of gaseous substances (CO.sub.2, H.sub.2O and N.sub.2). The gas/solid systems described according to the invention produce, according to how they are chosen, residue-free, almost CO- and NO.sub.x-free, reaction products, with the burn-off property being controllable according to the nature, proportion by weight, geometry and configuration of the fuel.

[0011] The invention will be described in detail below through examples, without however limiting it:

EXAMPLES

[0012] All the tests are carried out in a sealed pressure vessel with a volume of approx. 120 ml. The ignition is performed electrically with 150 mg of a boron/potassium nitrate mixture as booster. The laughing gas is fed into the vessel by means of a compressor. The weighed portion of laughing gas may be determined by weighing of the vessel before and after the charging. The internal pressure in the vessel comes after the feeding to approx. 4 Mpa. The solid selected is weighed into the vessel prior to the charging with laughing gas. The pressure measurement is carried out in the vessel by piezoelectric pressure elements. Maximum pressure (p.sub.max), pressure increase time (.DELTA.t) and time until maximum pressure(t.sub.pmax)is reached are measured. In Example 1 the behaviour of the laughing gas without additional fuel is shown (see Table 1). Heating and pressure increase takes place in the vessel due to the ignition, which pressure increase however differs significantly from the burn-off behaviour in the presence of solids, as Examples 2-4 show. In Examples 2-4 the burn-off behaviour of various materials such as polystyrene, nitroguanidine and starch is represented. A summary of the results is given in Table 1.

1TABLE 1 Summary of results of Examples 1-4 Weighed Weighed portion Ex- portion laughing p.sub.max .DELTA.t t.sub.pmax ample Solid solid [g] gas [g] [Mpa] [ms] [Mpa] 1 -- -- 11 42 11.2 15.4 2 Poly- 1.1 11 62 2.2 7.1 styrene 3 Nitroguani- 1.1 11 69 1.1 4.4 dine 4 Starch 1.1 11 64 4.2 11.5 (flour)

[0013] In Examples 5-9 the influence of various make-ups and geometries of the solid on the burn-off characteristics in the pressure vessel is shown. Two solids are used, first of all starch in various modifications, here characterised by the particle diameter, and secondly nitroguanidine as a loose powder with a grain size of approx. 50 .mu.m and as tablet with a diameter of 7 mm and a depth of approx. 2.3 mm. A summary of results is given in Table 2.

2TABLE 2 Summary of results of Examples 5-9 p.sub.max t.sub.pmax Example Solid Geometry [Mpa] .DELTA.t [ms] [Mpa] 5 Starch Sphere D: 63.7 4.2 11.6 1-2 .mu.m 6 Starch Sphere D: 66.4 7.01 21.9 approx. 250 .mu.m 7 Starch Sphere D: 61.7 9.4 29.9 approx. 1 mm 8 Nitroguani- Powder 68.6 1.1 4.4 dine grain size approx. 50 .mu.m 9 Nitroguani- Tablet D 60.1 10.7 38.5 dine 7 mm, D 2.3 mm

[0014] Very good estimates of gas composition and combustion temperatures are obtained by means of thermodynamic calculations. In Examples 10-12 a thermodynamic calculation is carried out with the ICT code for polystyrene, nitroguanidine and starch. It is based in each case on a solid-laughing gas mixture of 9 to 91 wt %. A summary of the results is given in Table 3.

3TABLE 3 Summary of results of Examples 10-12 Combustion temperature N.sub.2 CO.sub.2 H.sub.2O O.sub.2 CO NO.sub.x Example [K] [vol. %] [vol. %] [vol. %] [vol. %] [vol. %] [vol. %] 10 4075 63.1 21.2 10.4 5.2 <0.001 0.06 11 2710 64.9 2.4 5.0 27.5 <0.001 0.14 12 3181 61.2 9.8 8.2 20.6 <0.001 0.11

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