Claims
- 1. An active binder propellant composition comprising, by weight:
- (A) a nitrocellulose binder in the range 8-99.9 percent;
- (B) oxidizer or monopropellant in the range 0-60 percent; and
- (C) a burn rate catalyst, in the range 0.01-20 percent, which consists of certain decahydrodecaborate salts, having the common anion B.sub.10 H.sub.10.sup.-2 wherein the cation is selected from the group consisting of:
- (i) ammonium, wherein the salt has the formula (NH.sub.4).sub.2 B.sub.10 H.sub.10 ;
- (ii) hydrazinium, wherein the salt has the general formula (NH.sub.2 NH.sub.3)B.sub.10 H.sub.10 ;
- (iii) substituted ammonium cations, wherein the salt has the general formula (R.sub.3 NH).sub.2 B.sub.10 H.sub.10, wherein further R is selected from the group consisting of hydrogen and alkyl radicals containing less than six carbon atoms;
- (iv) substituted hydrazinium cations, wherein the salt has the general formula (R.sub.2 NNR.sub.2 H).sub.2 B.sub.10 H.sub.10 wherein further R is selected from the group consisting of hydrogen and alkyl radicals containing less than six atoms,
- wherein said burn rate catalyst is further the resultant product of a coprecipitation of one of said group of decahydrodecaborate salts, and a solid oxidizing agent, by the process of:
- (i) dissolving both the decahydrodecaborate (-2) salt and the solid oxidizing agent in a mutually soluble solvent, at a temperature sufficiently high to maintain said salt and said oxidizing agent in solution;
- (ii) forming a pressurized stream of said solution and bringing said solution stream together with a pressurized stream of a miscible nonsolvent, under conditions of extreme turbulence within a mixing chamber, to effect a substantially complete coprecipitation;
- (iii) recovering the coprecipitated product by filtering the effluent from said mixing chamber, and washing said product with an inert and nonsolvent fluid;
- (iv) drying the product to remove all remaining fluid.
- 2. An active binder propellant composition comprising, by weight:
- (A) a nitrocellulose binder in the range 8-99.9 percent;
- (B) oxidizer or monopropellant in the range 0-60 percent; and
- (C) a burn rate catalyst, in the range 0.01-20 percent, which consists of certain decahydrodecaborate salts, having the common anion B.sub.10 H.sub.10.sup.-2, and a cation selected from the group consisting of:
- (i) tetramethylammonium, (CH.sub.3).sub.4 N+, tetraethylammonium, (CH.sub.3 CH.sub.2).sub.4 N+, and quaternary ammonium cations having the general formula R.sub.4 N+ wherein R is an alkyl radical;
- (ii) pyrididinium, bipyridinium aryl-diazonium, aryl containing cations and substituted aryl containing cations,
- wherein said burn rate catalyst is further the resultant product of a coprecipitation of one of said group of decahydrodecaborate salts, and a solid oxidizing agent, by the process of:
- (i) dissolving both the decahydrodecaborate (-2) salt and the solid oxidizing agent in a mutually soluble solvent, at a temperature sufficiently high to maintain said salt and said oxidizing agent in solution;
- (ii) forming a pressurized stream of said solution and bringing said solution stream together with a pressurized stream of a miscible nonsolvent, under conditions of extreme turbulence within a mixing chamber, to effect a substantially complete coprecipitation;
- (iii) recovering the coprecipitated product by filtering the effluent from said mixing chamber, and washing said product with an inert and nonsolvent fluid;
- (iv) drying the product to remove all remaining liquid.
- 3. An active propellant composition comprising, by weight:
- (A) a nitrocellulose binder in the range 8-99.9 percent;
- (B) oxidizer or monopropellant in the range 0-60 percent; and
- (C) a burn rate catalyst, in the range 0.01-20 percent, which consists of a decahydrodecaborate salt, having the anion B.sub.10 H.sub.10.sup.-2, wherein the cation is guanidinium, and the salt has the formula (C(NH.sub.2).sub.3).sub.2 B.sub.10 H.sub.10,
- wherein said burn rate catalyst is further the resultant product of a coprecipitation of bis guanidinium decahydrodecaborate, and a solid oxidizing agent, by the process of:
- (i) dissolving both the decahydrodecaborate (-2) salt and the solid oxidizing agent in a mutually soluble solvent, at a temperature sufficiently high to maintain said salt and said oxidizing agent in solution;
- (ii) forming a pressurized stream of said solution and bringing said solution stream together with a pressurized stream of a miscible nonsolvent, under conditions of extreme turbulence within a mixing chamber, to effect a substantially complete coprecipitation;
- (iii) recovering the coprecipitated product by filtering the effluent from said mixing chamber, and washing said product with an inert and nonsolvent fluid;
- (iv) drying the product to remove all remaining liquid.
- 4. An active binder propellant composition comprising, by weight:
- (A) a nitrocellulose binder in the range 8-99.9 percent;
- (B) oxidizer or monopropellant in the range 0-60 percent; and
- (C) a burn rate catalyst, in the range 0.01-20 percent, which consists of a metallic decahydrodecaborate salt, having the common anion B.sub.10 H.sub.10.sup.-2, wherein the cation is selected from the group consisting of:
- (i) metal ions derived from the elements in Groups 1, 2, 8, 3b, 4b, 5b, 6b, 7b, and the elements of Groups 3a, 4a, 5a, and 6a which have atomic numbers respectively greater than 5, 14, 33 and 52,
- wherein said burn rate catalyst is further the resultant product of a coprecipitation of one of said group of decahydrodecaborate salts, and a solid oxidizing agent, by the process of:
- (i) dissolving both the decahydrodecaborate (-2) salt and the solid oxidizing agent in a mutually soluble solvent, at a temperature sufficiently high to maintain said salt and said oxidizing agent in solution;
- (ii) forming a pressurized stream of said solution and bringing said solution stream together with a pressurized stream of a miscible nonsolvent, under conditions of extreme turbulence within a mixing chamber, to effect a substantially complete coprecipitation;
- (iii) recovering the coprecipitated product by filtering the effluent from said mixing chamber, and washing said product with an inert and nonvolvent fluid;
- (iv) drying the product to remove all remaining liquid.
- 5. An active binder propellant composition according to claim 1 wherein said nitrocellulose base binder is selected from the group consisting of nitrocellulose, nitrocellulose/nitroglycerine, and nitrocellulose/nitroglycerine/nitroguanidine.
- 6. An active binder propellant composition according to claim 2 wherein said nitrocellulose base binder is selected from the group consisting of nitrocellulose, nitrocellulose/nitroglycerine, and nitrocellulose/nitroglycerine/nitroguanidine.
- 7. An active binder propellant composition according to claim 3 wherein said nitrocellulose base binder is selected from the group consisting of nitrocellulose, nitrocellulose/nitroglycerine, and nitrocellulose/nitroglycerine/nitroguanidine.
- 8. An active binder propellant composition according to claim 4 wherein said nitrocellulose base binder is selected from the group consisting of nitrocellulose, nitrocellulose/nitroglycerine, and nitrocellulose/nitroglycerine, and nitrocellulose/nitroglycerine/nitroguanidine.
- 9. A nitrocellulose base propellant composition according to claim 5 wherein said oxidizing agent is selected from the group consisting of ammonium nitrate, potassium nitrate, potassium perchlorate, ammonium perchlorate, guanidine nitrate, triaminoguanidine nitrate, potassium permanganate, sodium chromate, barium nitrate, barium chromate, barium manganate, sodium dichromate, tetramethylammonium nitrate and cesium nitrate.
- 10. A nitrocellulose base propellant composition according to claim 6 wherein said oxidizing agent is selected from the group consisting of ammonium nitrate, potassium nitrate, potassium perchlorate, ammonium perchlorate, guanidine nitrate, triaminoguanidine nitrate, potassium permanganate, sodium chromate, barium nitrate, barium chromate, barium manganate, sodium dichromate, tetramethylammonium nitrate and cesium nitrate.
- 11. A nitrocellulose base propellant composition according to claim 7 wherein said oxidizing agent is selected from the group consisting of ammonium nitrate, potassium nitrate, potassium perchlorate, ammonium perchlorate, guanidine nitrate, triaminoguanidine nitrate, potassium permanganate, sodium chromate, barium nitrate, barium chromate, barium manganate, sodium dichromate, tetramethylammonium nitrate and cesium nitrate.
- 12. A nitrocellulose base propellant composition according to claim 8 wherein said oxidizing agent is selected from the group consisting of ammonium nitrate, potassium nitrate, potassium perchlorate, ammonium perchlorate, guanidine nitrate, triaminoguanidine nitrate, potassium permanganate, sodium chromate, barium nitrate, barium chromate, barium manganate, sodium dichromate, tetramethylammonium nitrate and cesium nitrate.
- 13. An active binder propellant composition according to claim 12 wherein the metallic salt selected is cesium decahydrodecaborate, said solid oxidizing agent is potassium nitrate, said solvent is water, and said nonsolvent stream is acetone.
- 14. An active binder propellant composition according to claim 13 wherein said propellant binder selected is of the double base type, comprising nitrocellulose/nitroglycerine.
- 15. An active binder propellant composition according to claim 14 wherein said double base propellant further comprises approximately, by weight, 48% nitroglycerine, 12.05% triactin, 5% cellulose acetate, 2% nitrodiphenylamine, 2% lead 2-ethyl hexoate and 0.05% candilla wax.
- 16. An active binder propellant composition according to claim 14 wherein said burn rate catalyst is in the range 0.01-10 percent.
- 17. An active binder propellant composition according to claim 15 wherein said burn rate catalyst is present in the range 0.01-10 percent.
CROSS REFERENCE TO RELATED APPLICATIONS
This application is a continuation-in-part of copending application METHOD FOR PREPARING A HIVELITE HIGH BURN PROPELLANT COMPOSITION, Ser. No. 592,449, filed July 2, 1975, now abandoned, which in turn is a continuation-in-part of Ser. No. 585,216, filed June 6, 1975 and entitled HIGH BURN PROPELLANT COMPOSITIONS, now abandoned.
US Referenced Citations (8)
Continuation in Parts (2)
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Number |
Date |
Country |
Parent |
592449 |
Jul 1975 |
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Parent |
585216 |
Jun 1975 |
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