Process for manufacturing a gas generator composition

• US 5,563,367 A
• Filed: 03/23/1995
• Issued: 10/08/1996
• Est. Priority Date: 04/10/1992
• Status: Expired due to Fees

• Current Assignee: NOF Corporation
• Original Assignee: NOF Corporation
• Inventors: Ochi, Koji, Matsuda, Kazunori, Narita, Kazuyuki, Asano, Nobukazu
• Primary Examiner(s): Nelson, Peter A.
• Application Number:
  US08/409,278
• Time in Patent Office: 565 Days
• Field of Search: 149/35, 102/288, 102/289, 264/3.2
• US Class Current: 102/288
• CPC Class Codes: C06B 35/00 Compositions containing a metal azide
• CPC Class Codes: C06D 5/06 by reaction of two or more solids

Abstract

The gas generator composition contains sodium azide and an oxidizing agent as major components. This gas generator composition additionally contains 2 to 8% by weight of magnesium aluminate. To produce this composition, sodium azide and the oxidizing agent are admixed to a colloidal silica having a silica concentration of 3 to 15% by weight to form a slurry, followed by granulation and drying of the slurry.

Claims

1. A process for producing a gas generator composition comprising the steps of:

adding sodium azide, an oxidizing agent and magnesium aluminate to a colloidal silica having a silica concentration of 3 to 15% by weight and blending the resultant mixture to form a slurry; and

granulating and drying said slurry to provide a gas generator composition.

2. The process according to claim 1, wherein pH of said slurry is 8 to 10.

3. The process according to claim 1, wherein said oxidizing agent is a substance which is negatively charged in said slurry.

4. The process according to claim 1, wherein said oxidizing agent is manganese dioxide.

5. The process according to claim 1, wherein said oxidizing agent is manganese dioxide baked at 250°

to 500°

C.

6. The process according to claim 1, wherein the ratio of silica derived from colloidal silica to said gas generator composition is 4 to 10% by weight.

7. The process according to claim 1, wherein the ratio of said magnesium aluminate to said gas generator composition is 2 to 6% by weight.

8. The process according to claim 1, wherein said magnesium aluminate has a specific surface area of 100 to 250 m² /g.

9. The process according to claim 1, wherein the ratio of silica derived from colloidal silica to said gas generator composition is 4 to 10% by weight and a ratio of said magnesium aluminate to said gas generator composition is 2 to 8% by weight.

10. The process according to claim 1, wherein the total amount of said magnesium aluminate and said silica derived from colloidal silica is 6 to 12% by weight.

11. The process according to claim 1, wherein an adding ratio of said magnesium aluminate to said silica derived from colloidal silica is 1:

1 to 1;

3 in terms of weight ratio.