Claims
- 1. Process for the production of a pyrotechnic mixture in the form of granulates, comprising the steps of:
- (a) providing particles of a nitrogen-generating substance, and of an inorganic oxidizing agent having a particle size of from 1 .mu.m to 200 .mu.m, wherein said nitrogen-generating substance is an alkali metal azide, alkaline earth metal azide or ammonium azide,
- (b) mixing the particles from (a) with liquid silicone rubber, wherein the amount of the silicone rubber is 13 to 28% based on the weight of the total mixture,
- (c) producing granulates from the materials mixed according to step (b) having a grain size of 200 .mu.m to 12 mm and
- (d) curing the granulates.
- 2. Process for the production of pyrotechnic mixtures in the form of granulates, comprising the steps of:
- (a) providing particles of a nitrogen-generating substance and of an inorganic oxidizing agent having a particle size of from 1 .mu.m to 200 .mu.m, wherein said nitrogen-generating substance is an alkaline metal azide, alkaline earth metal azide or ammonium azide,
- (b) mixing the particles from (a) with a binder,
- (c) producing pre-granulation products from the materials mixed according to step (b) having a grain size of from 20 .mu.m to 5 .mu.m,
- (d) mixing the pregranulation products from (c) with liquid silicone rubber, wherein the amount of silicone rubber is 13 to 28% based on the weight of the total mixture,
- (e) producing granulates from the materials mixed according to step (d) having a grain size of from 200 .mu.m to 12 mm, and
- (f) curing the granulates.
- 3. Process according to claim 2, characterized in that the binder in step (b) is added in an amount of 1 to 5% based on the weight of the total mixture.
- 4. Process according to claim 2 or 3, characterized in that in step (b) nitrocellulose is used as the binder.
- 5. Process for the production of a pyrotechnic mixture according to claim 1 or 2, characterized in that following a grinding step wherein the azide and the inorganic oxidizing agent comprising a nitrate are crushed to a particle size of from 1 .mu.m to 200 .mu.m, liquid silicone rubber is added and subsequently the mixture is granulated.
- 6. Process according to claim 5, characterized in that an intermediate granulation step follows the grinding step wherein a binder is used.
- 7. Process according to claim 6, characterized in that the intermediate granulation step is carried out by adding 1.6 percent by weight of nitrocellulose as the binder and further adding a highly volatile solvent for nitrocellulose, and effecting subsequent granulation and drying.
- 8. Process according to claim 1 or 2, characterized in that a silicone rubber having a viscosity of 10 to 200,000 mPas at 20.degree. C. is used.
- 9. Process according to claim 1 wherein a hardener is additionally added to mixing step (b).
- 10. Process according to claim 1 wherein a solvent or suspending agent for the binder is additionally added to mixing step (b).
- 11. Process according to claim 2 wherein a hardener is additionally added to mixing step (d).
- 12. Process according to claim 7 wherein the solvent is acetone.
- 13. Process according to claim 5 wherein a hardener is additionally added prior to said granulation.
Priority Claims (2)
Number |
Date |
Country |
Kind |
42 31 521.2 |
Sep 1992 |
DEX |
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43 10 853.9 |
Apr 1993 |
DEX |
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Parent Case Info
This is a divisional of copending application Ser. No. 08/125,029, filed on Sep. 21, 1993.
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Divisions (1)
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Number |
Date |
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Parent |
125029 |
Sep 1993 |
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