Microcellular composite energetic materials and method for making same

• US 4,632,714 A
• Filed: 09/19/1985
• Issued: 12/30/1986
• Est. Priority Date: 09/19/1985
• Status: Expired due to Term

• Current Assignee: Ireco, Inc.
• Original Assignee: Megabar Corporation
• Inventors: Peterson, John A., Abegg, M. Taylor
• Primary Examiner(s): Lechert, Jr., Stephen J.
• Application Number:
  US06/777,832
• Time in Patent Office: 467 Days
• Field of Search: 149/2, 149/21, 149/45, 149/46, 149/61, 149/76, 149/83, 149/88, 149/92
• US Class Current: 149/2
• CPC Class Codes: C06B 45/00 Compositions or products which are defined by structure or arrangement of component of product explosive charges of particular form or shape F42B1/00, F42B3/00
• CPC Class Codes: C06B 47/145 Water in oil emulsion type explosives in which a carbonaceous fuel forms the continuous phase

Abstract

Essentially anhydrous energetic compositions, including explosives, propellants, flares, and gas generators, are initially formed at process temperatures above the solidification temperature of contained oxidizer salts as stable, melt-in-fuel emulsions having a continuous fuel phase and a discontinuous molten oxidizer phase. Surfactants are employed which cause the compositions to retain general fuel phase continuity and oxidizer phase discontinuity upon solidification. The final product is a firm or solid emulsion generally characterized by an intimate dispersion of discrete solid oxidizer cells in a fuel continuum, the product having excellent storage stability and water resistance.

Claims

1. A castable composite explosive, propellant, flare, or gas generator, comprising in combination:

a substantially water-free, stable emulsion of molten inorganic oxidizer salt(s), immiscible hydrocarbon fuel(s) and surfactant(s), the fuel(s) and surfactant(s) forming the continuous phase in which the oxidizer phase in dispersed in the form of discrete cells which solidify upon cooling without material disruption of the fuel phase continuum, the surfactants being selected for their capacity to form an emulsion at process temperatures which retains substantial fuel phase continuity during solidification, the oxidizer phase being at least 75% by weight of the emulsion, the final product being solid, firm or rigid;

wherein water may be present as water of hydration or because of the hygroscopic nature of the ingredients and is limited to 3% maximum by weight of the composition.

2. A composition as claimed in claim 1 wherein the intimately mixed ingredients allow the molten oxidizer cells to supercool before solidification occurs.

3. A composition as claimed in claim 1 wherein the oxidizer cells in the solid final product are crystalline.

4. A composition as claimed in claim 1 wherein the oxidizer cells in the solid final product are amorphous.

5. A composition as claimed in claim 1 wherein the fluid emulsion can be placed in suitable containers in which the composition subsequently hardens.

6. A composition as claimed in claim 1 wherein the oxygen balance is between +5% and -30%.

7. A composition as claimed in claim 1 wherein the composition employs a metallic fuel and the oxygen balance is between +5% and -50%.

8. A composition as claimed in claim 1 wherein the surfactant concentration is from 0.05% to 15% of the composition by weight.

9. A composition as claimed in claim 1 wherein inorganic nitrates constitute the major portion of the molten oxidizer salt or mixture of salts.

10. A composition as claimed in claim 9 wherein ammonium nitrate is the principal oxidizer salt comprising not less than 40% by weight of the composition.

11. A composition as claimed in claim 10 wherein other oxidizer salts are added in conjunction with ammonium nitrate;

the total concentration of the added salt or salts is limited to 55% by weight of the composition; and

no single salt other than ammonium nitrate is present in concentration greater than 40% by weight of the composition.

12. A composition as claimed in claim 11 wherein the added oxidizers are selected from the group consisting of alkali and alkaline earth nitrates and perchlorates, and ammonium perchlorate.

13. A composition as claimed in claim 12 wherein the added oxidizer is selected from the group consisting of zinc nitrate, manganese nitrate, copper nitrate, lead nitrate and the perchlorate analogs.

14. A composition as claimed in claim 11 wherein oxidizer additives are the perchlorate, chlorate or nitrite analogs of the inorganic nitrates.

15. A composition as claimed in claim 11 wherein any soluble and compatible potassium salt is added to phase-stabilize ammonium nitrate.

16. A composition as claimed in claim 9 wherein lithium nitrate is the principal oxidizer salt.

17. A composition as claimed in claim 1 wherein inorganic perchlorates constitute the major portion of the molten oxidizer salt or mixture of salts.

18. A composition as claimed in claim 17 wherein lithium perchlorate is the principal oxidizer salt.

19. A composition as claimed in claim 17 wherein additives selected from the group consisting of ammonium, lithium, sodium, potassium, magnesium, calcium, strontium, barium, copper, zinc, manganese and lead perchlorates, nitrates, chlorates and nitrites are added;

and the concentration of any single such additive is not more than 45% by weight of the total composition.

20. A composition as claimed in claim 17 wherein ammonium perchlorate is the additive.

21. A composition as claimed in claim 1 wherein the principal oxidizer is selected from the chlorate salts and wherein additives selected from the perchlorate, nitrite, and nitrate salts are optional.

22. A composition as claimed in claim 21 wherein lithium perchlorate is the principal oxidizer.

23. A composition as claimed in claim 1 wherein the principal oxidizer is selected from the nitrite salts and wherein additives selected from the perchlorate, nitrate, and chlorate salts are optional.

24. A composition as claimed in claim 1 wherein the fuel is polymerizable or crosslinkable and where polymerization or crosslinking or both may be accomplished in situ.

25. A composition as claimed in claim 1 wherein the fuel is a thermoplastic polymer.

26. A compositon as claimed in claim 24 wherein polymerizable fuels are selected from the group consisting of polyesters, polyethers, polydienes, polysulfides, polyperflourocarbons, polyoefins, polyamines, polyalkanes, polyphenols and polyacetylenes.

27. A composition as claimed in claim 1 wherein the hydrocarbon fuel is nonpolymerizable.

28. A composition as claimed in claim 1 wherein molten compound explosives may be employed as fuel(s), singly or in combination.

29. A composition a claimed in claim 1 wherein combinations of molten compound explosive(s) and hydrocarbon fuel(s) constitute the fuel phase of the composition.

30. A composition as claimed in claim 1 wherein the fuels are selected from the group consisting of silicones and polysiloxanes.

31. A composition as claimed in claim 1 wherein the fuels are halogenated hydrocarbons.

32. A composition as claimed in claim 1 wherein the fuels are synthetic oils.

33. A composition as claimed in claim 1 wherein the fuels are molten surfactants.

34. A composition as claimed in claim 1 wherein the surfactants form oil-continuous emulsions and are selected from those having chain lengths equal to or greater than 12 carbon atoms in length.

35. A composition as claimed in claim 1 wherein the surfactants are crystal habit modifiers which are dialkylnaphthalene sulfonates.

36. A composition as claimed in claim 1 wherein additives selected from the group consisting of aromatic and alkylaryl surfactants are employed.

37. A composition as claimed in claim 1 wherein fuels which are soluble in the oxidizer portion are employed singly or in combination.

38. A composition as claimed in claim 37 wherein the soluble fuels are compound explosives.

39. A composition as claimed in claim 38 wherein the soluble compound explosive is the nitrate or perchlorate adduct of an alkylamine or alkanolamine.

40. A composition as claimed in claim 38 wherein the soluble compound explosive is an oxidizer.

41. A composition as claimed in claim 38 wherein the oxidizer portion is comprised of molten compound explosives, singly or in combination.

42. A composition as claimed in claim 38 wherein the compound explosive is selected from the group consisting of hexamethylenetetramine nitrates and hexamethylenetetramine perchlorates.

43. A composition as claimed in claim 38 wherein the compound explosive is a nitroazole salt.

44. A composition as claimed in claim 1 wherein the originally fluid mixture is employed as a matrix into which insoluble solids or liquids may be added.

45. A composition as claimed in claim 44 wherein the added solid is a compound explosive.

46. A composition as claimed in claim 44 wherein the added solid is a metallic fuel.

47. A composition as claimed in claim 44 wherein a compound explosive which is a metal ammonia coordination compound is added.

48. A composition as claimed in claim 44 wherein insoluble molten compound explosives are dispersed in the originally fluid mixture.

49. A composition as claimed in claim 44 wherein the insoluble solid additive is an oxidizer.

50. A composition as claimed in claim 1 wherein density control or sensitization is achieved by the use of additives selected from microballoons, perlite, fumed silica, entrained gas, and gas generated in situ.

51. A method of preparing a composition as claimed in claim 1 which comprises heating the ingredients until they are molten, mixing the ingredients while in the molten state, forming a stable emulsion in which the hydrocarbon fuel forms the continuous phase and the molten oxidizer forms the discontinuous phase, imparting sufficient additional shear to achieve particle sizes small enough to maintain emulsion stability during solidification, and cooling the stable emulsion until the individual oxidizer droplets solidify as separate cells without material disruption of the fuel continuum, the final product being solid, firm or rigid.

52. A method as claimed in claim 51 wherein the additional shear imparted is sufficient to reduce the size of substantially all oxidizer phase particles to less than one micron in at least one dimension.