Process for preparing a gas generating composition

• US 6,319,341 B1
• Filed: 05/25/2000
• Issued: 11/20/2001
• Est. Priority Date: 05/25/2000
• Status: Expired due to Fees

• Current Assignee: TRW Inc. (Northrop Grumman Corporation)
• Original Assignee: TRW Inc. (Northrop Grumman Corporation)
• Inventors: Blomquist, Harold R.
• Primary Examiner(s): Miller, Edward A.
• Application Number:
  US09/578,658
• Time in Patent Office: 544 Days
• Field of Search: 149/19.92, 264/3.3, 264/3.4
• US Class Current: 149/19.92
• CPC Class Codes: C06B 21/0066 by granulation, e.g. flaking
• CPC Class Codes: C06B 21/0091 Elimination of undesirable or temporary components of an intermediate or finished product, e.g. making porous or low density products, purifying, stabilising, drying; Deactivating; Reclaiming; porous inert particles or chemicals compounded for these purposes C06B23/00
• CPC Class Codes: C06D 5/06 by reaction of two or more solids

Abstract

A process for preparing a gas generating composition (62) for a vehicle occupant protection apparatus (110) comprises the following steps. Desired quantities of ingredients of the gas generating composition (62) measured in predetermined amounts according to the percentage of the ingredients in the gas generating composition (62) are obtained. The ingredients include an elastomeric binder (16), an oxidizer (12), and a fuel (14). The ingredients are mixed with an azeotrope (28) to form a suspension. The suspension is atomized to form a stream (48) of spheroid droplets. The spheroid droplets are contacted with a hot gas to remove the azeotrope (28) from the spray droplets and produce solid spheroid particles of the gas generating composition (62) in which the oxidizer and fuel particles are intimately mixed with each other and bound together by the elastomeric binder.

Claims

1. A process for preparing a gas generating composition for a vehicle occupant protection apparatus comprising the following steps:

obtaining desired quantities of ingredients of the gas generating composition measured in predetermined amounts according to the percentage of the ingredients in the gas generating composition, the ingredients including an elastomeric binder, a fuel, and an oxidizer;

mixing the ingredients with an azeotrope to form a suspension;

atomizing the suspension to form a stream of spheroid droplets; and

contacting the spheroid droplets with gas to remove the azeotrope from said spray droplets and produce solid spheroid particles of the gas generating composition in which the oxidizer and fuel particles are intimately mixed with each other and bound together by the elastomeric binder.

2. The process of claim 1 wherein gas generating composition further includes a dispersant.

3. The process of claim 2 wherein the azeotrope comprises at least two solvents, one of said solvents having a solubility parameter effective to dissolve the elastomeric binder in the azeotrope, and the other of said solvents having a polarity effective to dissolve the dispersant in the suspension.

4. The process of claim 1 wherein the azeotrope has boiling point temperature from about 50°

C. to about 100°

C.

5. The process of claim 4 wherein the azeotrope has a boiling point temperature from about 70°

C. to about 100°

C.

6. The process of claim 1 wherein the azeotrope is a minimum boiling point azeotrope.

7. The process of claim 3 wherein the difference in the solubility parameters of the one liquid solvent and the elastomeric binder [δ

₁−

δ

₂] is less than about 2 (cal^½

cm<sup>−

½</sup>

).

8. The process of claim 7 wherein the azeotrope is a mixture of about 75% by weight cyclohexane and about 24% by weight dioxane.

9. The process of claim 1 wherein the oxidizer is an inorganic salt oxidizer selected from the group consisting of alkali metal nitrates, alkaline earth metal nitrates, alkali metal perchlorates, alkaline earth metal perchlorates, ammonium perchlorate, ammonium nitrate, and mixtures thereof.

10. The process of claim 9 wherein the inorganic salt is ammonium nitrate.

11. The process of claim 1 wherein the fuel is a non-azide organic fuel selected from the group consisting of cyclotrimethylenetrinitramine (RDX), cyclotetramethylenetetranitramine (HMX), and mixtures of cyclotetramethylenetetranitramine and cyclotrimethylenetrinitramine.

12. The process of claim 1 wherein the binder is selected from the group consisting of cellulose acetate butyrate (CAB), polycarbonates, polyurethanes, polyesters, polyethers, polysuccinates, thermoplastic rubbers, polybutadiene, polystyrene, and mixtures thereof.

13. The process of claim 2 wherein the dispersant is a polar dispersant.

14. The process of claim 13 wherein the dispersant is polyvinyl pyrrolidone.

15. A process for preparing a gas generating composition for a vehicle occupant protection apparatus comprising the following steps:

obtaining desired quantities of ingredients of the gas generating composition measured in predetermined amounts according to the percentage of the ingredients in the gas generating composition, the ingredients including an oxidizer, a fuel, an elastomeric binder and a dispersant;

mixing the ingredients with an azeotrope to form a suspension, the azeotrope comprising at least two solvents, wherein one of the solvents has a solubility parameter effective to dissolve the elastomeric binder in the azeotrope and the other of the solvents has a polarity effective to dissolve the dispersant in the azeotrope;

atomizing the suspension to form a stream of spheroid droplets; and

contacting the spheroid droplets with gas to remove the azeotrope from said spray droplets and produce solid spheroid particles of the gas generating composition in which the oxidizer and fuel particles are intimately mixed with each other and bound together by the elastomeric binder.

16. The process of claim 15 wherein the azeotrope has boiling point temperature from about 50°

C. to about 100°

C.

17. The process of claim 16 wherein the azeotrope has a boiling point temperature from about 70°

C. to about 100°

C.

18. The process of claim 15 wherein the azeotrope is a minimum boiling point azeotrope.

19. The process of claim 15 wherein the difference in the solubility parameters of the one liquid solvent and the elastomeric binder [δ

₁−

δ

₂] is less than about 2 (cal^½

cm<sup>−

½</sup>

).

20. The process of claim 15 wherein the azeotrope is a mixture of about 75.4% by weight cyclohexane and about 24.6% by weight dioxane.

21. The process of claim 15 wherein the oxidizer is an inorganic salt oxidizer selected from the group consisting of alkali metal nitrates, alkaline earth metal nitrates, alkali metal perchlorates, alkaline earth metal perchlorates, ammonium perchlorate, ammonium nitrate, and mixtures thereof.

22. The process of claim 21 wherein the inorganic salt is ammonium nitrate.

23. The process of claim 15 wherein the fuel is a non-azide organic fuel selected from the group consisting of cyclotrimethylenetrinitramine (RDX), cyclotetramethylenetetranitramine (HMX), and mixtures of cyclotetramethylenetetranitramine and cyclotrimethylenetrinitramine.

24. The process of claim 15 wherein the binder is selected from the group consisting of cellulose acetate butyrate (CAB), polycarbonates, polyurethanes, polyesters, polyethers, polysuccinates, thermoplastic rubbers, polybutadiene, polystyrene, and mixtures thereof.

25. The process of claim 15 wherein the dispersant is a polar dispersant.

26. The process of claim 25 wherein the dispersant is polyvinyl pyrrolidone.