WO1998023558A1 - Ammonium nitrate propellants with molecular sieve - Google Patents

Ammonium nitrate propellants with molecular sieve Download PDF

Info

Publication number
WO1998023558A1
WO1998023558A1 PCT/US1996/018874 US9618874W WO9823558A1 WO 1998023558 A1 WO1998023558 A1 WO 1998023558A1 US 9618874 W US9618874 W US 9618874W WO 9823558 A1 WO9823558 A1 WO 9823558A1
Authority
WO
WIPO (PCT)
Prior art keywords
composition
mixtures
ammonium nitrate
group
total weight
Prior art date
Application number
PCT/US1996/018874
Other languages
French (fr)
Inventor
Wayne C. Fleming
Hugh J. Mcspadden
Donald E. Olander
Original Assignee
Universal Propulsion Co., Inc.
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Universal Propulsion Co., Inc. filed Critical Universal Propulsion Co., Inc.
Priority to EP96946254A priority Critical patent/EP0946464A4/en
Priority to JP52657398A priority patent/JP2002511829A/en
Priority to PCT/US1996/018874 priority patent/WO1998023558A1/en
Priority to KR1019990704638A priority patent/KR20000057253A/en
Priority to CA002273335A priority patent/CA2273335A1/en
Publication of WO1998023558A1 publication Critical patent/WO1998023558A1/en
Priority to NO19992497A priority patent/NO313324B1/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C06EXPLOSIVES; MATCHES
    • C06BEXPLOSIVES OR THERMIC COMPOSITIONS; MANUFACTURE THEREOF; USE OF SINGLE SUBSTANCES AS EXPLOSIVES
    • C06B31/00Compositions containing an inorganic nitrogen-oxygen salt
    • C06B31/28Compositions containing an inorganic nitrogen-oxygen salt the salt being ammonium nitrate
    • C06B31/30Compositions containing an inorganic nitrogen-oxygen salt the salt being ammonium nitrate with vegetable matter; with resin; with rubber
    • CCHEMISTRY; METALLURGY
    • C06EXPLOSIVES; MATCHES
    • C06BEXPLOSIVES OR THERMIC COMPOSITIONS; MANUFACTURE THEREOF; USE OF SINGLE SUBSTANCES AS EXPLOSIVES
    • C06B31/00Compositions containing an inorganic nitrogen-oxygen salt
    • C06B31/28Compositions containing an inorganic nitrogen-oxygen salt the salt being ammonium nitrate
    • CCHEMISTRY; METALLURGY
    • C06EXPLOSIVES; MATCHES
    • C06BEXPLOSIVES OR THERMIC COMPOSITIONS; MANUFACTURE THEREOF; USE OF SINGLE SUBSTANCES AS EXPLOSIVES
    • C06B23/00Compositions characterised by non-explosive or non-thermic constituents
    • C06B23/006Stabilisers (e.g. thermal stabilisers)
    • CCHEMISTRY; METALLURGY
    • C06EXPLOSIVES; MATCHES
    • C06BEXPLOSIVES OR THERMIC COMPOSITIONS; MANUFACTURE THEREOF; USE OF SINGLE SUBSTANCES AS EXPLOSIVES
    • C06B45/00Compositions or products which are defined by structure or arrangement of component of product
    • C06B45/04Compositions or products which are defined by structure or arrangement of component of product comprising solid particles dispersed in solid solution or matrix not used for explosives where the matrix consists essentially of nitrated carbohydrates or a low molecular organic explosive
    • C06B45/06Compositions or products which are defined by structure or arrangement of component of product comprising solid particles dispersed in solid solution or matrix not used for explosives where the matrix consists essentially of nitrated carbohydrates or a low molecular organic explosive the solid solution or matrix containing an organic component
    • C06B45/10Compositions or products which are defined by structure or arrangement of component of product comprising solid particles dispersed in solid solution or matrix not used for explosives where the matrix consists essentially of nitrated carbohydrates or a low molecular organic explosive the solid solution or matrix containing an organic component the organic component containing a resin
    • C06B45/105The resin being a polymer bearing energetic groups or containing a soluble organic explosive
    • CCHEMISTRY; METALLURGY
    • C06EXPLOSIVES; MATCHES
    • C06DMEANS FOR GENERATING SMOKE OR MIST; GAS-ATTACK COMPOSITIONS; GENERATION OF GAS FOR BLASTING OR PROPULSION (CHEMICAL PART)
    • C06D5/00Generation of pressure gas, e.g. for blasting cartridges, starting cartridges, rockets
    • C06D5/06Generation of pressure gas, e.g. for blasting cartridges, starting cartridges, rockets by reaction of two or more solids

Definitions

  • the present invention is directed to ammonium nitrate propellant compositions. More particularly, it is directed to age-stabilized and/or strengthened ammonium nitrate propellant compositions and methods for making the same.
  • Propellant compositions are useful for a variety of applications.
  • One such application is in vehicle air bag restraint devices.
  • it is important to reduce the toxicity of gases produced upon combustion of the propellant.
  • the propellant composition burn in a smokeless or nearly smokeless fashion because the presence of smoke can cause various problems. For example, after an accident in which an air bag has been deployed, smoke not only hinders visibility, it also interferes with any ongoing rescue efforts.
  • propellant composition combustion products be smoke-free or nearly so.
  • propellant compositions Another application of propellant compositions is their use in rockets and in other munitions as propulsive propellant compositions.
  • Combustion of propulsive propellant compositions in rockets and the like provides the energy required to transport them over long distances towards a given target.
  • rockets powered by propulsive propellant compositions be as undetectable as possible upon launch and during deployment.
  • double base refers to a propellant composition containing both nitroglycerine (NG) and nitrocellulose (NC) .
  • Double base propellants are prone to premature explosion or premature deflagration in response to various unplanned stimuli (e.g., fire, heat, shrapnel, bullets, other fragments etc.) that may be encountered in battle.
  • HMX cyclotetramethylene tetranitramine
  • RDX cyclotrimethylene trinitramine
  • propellant compositions including double base propellants were pursued at the expense of safety, especially in regards to naval operations. Consequently, the U.S. Navy has taken the lead in formulating a series of standards concerning insensitive ammunition requirements, formalized as MIL-STD-2105B, incorporated herein by reference in its entirety. Equivalent insensitive ammunition standards have been adopted by most major military powers (e.g., England, France, Germany, etc.). These standards require that propellant compositions meet or exceed insensitive ammunition safety standards for the weapons platforms for which they were designed.
  • STANAG 6016 (NATO Standardized Agreement Solid Propellant Smoke Classification) .
  • STANAG 6016 is incorporated herein by reference in its entirety.
  • the smoke effluent is calculated by a number of thermo-chemical codes that are well known in the industry. For example, STANAG 6016 classifications "AA” and “AC” correspond to the definitions of minimum smoke and reduced smoke, respectively.
  • the "smoke-free”, “nearly smoke free” and/or “substantially smoke free” terms as used herein are synonymous with the definition of minimum smoke (i.e., code AA) .
  • Ammonium or metal perchlorates produce hydrogen chloride during combustion. Hydrogen chloride reacts with moisture in the ambient air to yield a liquid/gas aerosol. The aerosol forms another visible smoke referred to as "secondary smoke". Either "primary smoke” or “secondary smoke” formed as an effluent from the combustion of a propulsive propellant composition negates the advantage of surprise. The smoke trail aids opposing forces in destroying or otherwise countering the incoming missile. In addition, such effluent smoke points to the launch position. During battle, such smoke places launch personnel in greater danger of potentially successful retaliation, e.g., by counter battery fire. Ammonium nitrate as a propellant ingredient may produce a propellant that does not produce primary or secondary smoke upon combustion.
  • ammonium nitrate presents other drawbacks as a propellant component. Principally, it is recognized that ammonium nitrate undergoes several crystal phase changes at various well-recognized temperatures. Pure ammonium nitrate undergoes a series of structural and volumetric crystal phase transformations over typical operating temperature ranges. In pure ammonium nitrate, structural crystal phase transitions are observed at about -18°C, 32.3°C, 84.2°C and 125.2°C, respectively. The phase transition at about 32.3°C is particularly troublesome.
  • the term “age-stabilized” refers to a state of ammonium nitrate wherein the crystal phase III-IV and volumetric changes associated with thermal cycling are substantially reduced.
  • shelf-life of an ammonium nitrate propellant composition is considerably increased from about 1-2 years to about 5-20 years or more.
  • the term “strengthened”, as used herein, refers to a state of ammonium nitrate propellant wherein the tensile strength of the propellant is increased without unduly sacrificing elongation or, alternatively, is accompanied by an increase in elongation.
  • the strengthened ammonium nitrate propellant composition is substantially resistant to physical destruction of the propellant.
  • safe refers to an ammonium nitrate propellant composition that meets or exceeds the insensitive ammunition requirements promulgated in MIL- STD-2105B wherein the tendency to violent deflagration or explosion is substantially reduced and the shelf-life is substantially increased from about 1-2 years to about 5-20 years or more. Further, the term “safe” is used herein to refer to an ammonium nitrate propellant composition wherein the tendency to form grain fissures due to crystal phase changes is substantially reduced or altogether eliminated.
  • non-strengthened/non-age- stabilized ammonium nitrate propellant compositions that have been stored (e.g., either in munitions or in vehicle air bag restraint devices) for more than about 1 to 2 years may have undergone several crystal phase changes to the extent that the physical integrity of the propellant has been compromised and the propellant will no longer perform in the desired manner. Consequently, the useful shelf-life of prior art ammonium nitrate propellant compositions is disadvantageously shortened. Thus, it is desirable to formulate a smoke-free (or substantially smoke free) yet safe ammonium nitrate propellant composition having an extended shelf-life.
  • a propulsive or gas generating device containing a propellant composition requires a shelf-life from about 5 to about 20 years or more.
  • the shelf-life of the device is largely dependent on the shelf-life of the propellant composition contained therein.
  • a desirable shelf-life for a munition (propulsive) propellant composition or a vehicle air bag (gas producing) propellant composition is about 5 or more years, preferably, from about 7 to 20 years.
  • efforts have been directed at solving the crystal phase stabilization problem (i.e., of ammonium nitrate) .
  • phase stabilizing additives relate to the formation of large amounts of undesirable residue as combustion products.
  • KF potassium nitrate
  • it must be added to the molten phase (I) of ammonium nitrate. Thereafter, the KF modified ammonium nitrate is cooled.
  • the requirement for melting ammonium nitrate before adding KF is cumbersome, expensive and time consuming.
  • the effluent of a device using such a propellant is corrosive, smoky (with an enhanced radar cross section) and toxic.
  • the use of the metal oxides also has several drawbacks.
  • solid particulates are formed upon combustion when MgO, NiO, CuO and/or ZnO are used.
  • Solid particulates contribute to the formation of primary smoke which is undesirable.
  • NiO is carcinogenic.
  • NiO and CuO present environmental hazards.
  • both NiO and ZnO are only marginally effective. That is, once exposed to moisture, these oxides are no longer effective ammonium nitrate phase stabilizers. Further, NiO and ZnO increase the detonatability of the ammonium nitrate which is undesirable. Additionally, manufacturing propellant compositions including NiO and/or ZnO is more expensive.
  • phase III in ammonium nitrate depends on the presence of water, e.g., down to as little as about 0.1% by weight of the ammonium nitrate. See Choi et al., J. Appl. Cryst., Vol. 13, p. 403 (1980).
  • a high moisture content is said to favor III-IV phase transitions.
  • U.S. Patent No. 4,486,396 to Kjohl et al. (at column 1, lines 30-32), these phase transitions render the ammonium nitrate less stable to thermal cycling.
  • U.S. Patent No. 5,061,511 to Baczuk suggests the use of aluminum silicate molecular sieves (having a pore size of less than about 10 angstroms) as a stabilizer in propellant compositions such as single base or double base propellant.
  • propellant compositions such as single base or double base propellant.
  • propellant compositions include nitrocellulose and nitroglycerin, high energy fluorine containing propellants, single or double base nitrate ester propellants and composite propellants such as ammonium perchlorate/Al with rubber binders.
  • ammonium nitrate is not a propellant of the class described by Baczuk (i.e., See '511) and it does not give off the N 2 , C0 2 , CO, N0 X or F 2 gases (i.e., see '511) during aging, there is no expectation that molecular sieves in general, much less those having a pore size of 10 angstroms or less would stabilize ammonium nitrate.
  • ammonium nitrate is not a urethane cross- linked double base propellant (i.e., see '261)
  • molecular sieves e.g., having a pore size of 10 angstroms or more, would stabilize ammonium nitrate against volumetric crystal phase changes.
  • Kjohl et al. since water is associated with the undesirable crystal phase changes of ammonium nitrate, Kjohl et al., supra , used porous additives which could absorb water to stabilize ammonium nitrate. They further discovered that the presence of water absorbing porous particles resulted in no movement of water in the ammonium nitrate particles and that, during thermal cycling, swelling of ammonium nitrate was observed only to a small extent. Kjohl et al., however, state that the porous particles should be added to the ammonium nitrate after the ammonium nitrate is dried. Finally, they state that not any type of porous particle is suitable for stabilizing ammonium nitrate.
  • silicates of the molecular sieve type can bind water, but it has been found difficult to give such particles the required particle size and binding to the ammonium nitrate particles.
  • Kjohl et al. conclude that molecular sieves performed poorly in stabilizing ammonium nitrates (see column 3, lines 18-23).
  • the process for forming a safe, age-stabilized ammonium nitrate propellant composition comprises the steps of providing a quantity of ammonium nitrate, adding a sufficient quantity of a silicate molecular sieve to absorb water from the ammonium nitrate, grinding the ammonium nitrate with the molecular sieve, maintaining contact between the ammonium nitrate and the sieve, then adding at least a binder (except any curing agent e.g., isocyanate curing agent), maintaining contact between the ground molecular sieve and the other ingredients and finally adding a curing agent, if any, to yield the safe, age-stabilized ammonium nitrate propellant composition having a long shelf-life.
  • a binder except any curing agent e.g., isocyanate curing agent
  • these and other objects are accomplished by the addition of a strengthening agent to a mixture of ammonium nitrate and at least a binder to yield a strengthened propellant composition.
  • a molecular sieve may also be added to the strengthened ammonium nitrate propellant to yield an enhanced, strengthened and age- stabilized ammonium nitrate propellant composition.
  • an age-stabilized ammonium nitrate composition may be formed by adding a molecular sieve to ammonium nitrate (e.g., at least about 1 gram of a molecular sieve per pound of ammonium nitrate) and then grinding the mixture. Thereafter, the mixture may be safely stored without deleterious changes for an extended period of time in a sealed container.
  • a molecular sieve e.g., at least about 1 gram of a molecular sieve per pound of ammonium nitrate
  • the first embodiment of the present invention relates to an age-stabilized ammonium nitrate propellant composition.
  • the second embodiment relates to a strengthened ammonium nitrate propellant composition.
  • the third embodiment relates to an age-stabilized and strengthened ammonium nitrate propellant composition.
  • each embodiment may be used, with certain modifications, as a gas producing ammonium nitrate propellant composition or as a propulsive ammonium nitrate propellant composition.
  • the gas producing ammonium nitrate propellant compositions are designed to be used in vehicle air bag restraint systems and the like wherein gas production is paramount.
  • the propulsive ammonium nitrate propellant compositions are designed to be used in rockets and other munitions wherein energy output is paramount.
  • the substantially smoke-free ammonium nitrate propellant composition comprises ammonium nitrate, a molecular sieve and a binder.
  • the first embodiment may contain one or more of a variety of additives.
  • additives include, but are not limited to, a nitroplasticizer (e.g., nitramines and/or nitrate esters which are in a liquid phase when added, typically, at room temperature such as at about 25°C) , an energetic additive (e.g., nitramines which are in a solid phase when added, typically, at room temperature) , a nitrate ester stabilizer, a curing agent, a cure accelerator, an opacifier and a polymer protector (i.e., an antioxidant) .
  • the ammonium nitrate may be present as fines, prills, granules and the like.
  • the size of the ammonium nitrate may vary between about 5 microns and about 5,000 microns (or any value therebetween) in thickness.
  • a particle thickness is, preferably, from about 5 microns to about 400 microns and, most preferably, from about 30 to about 50 microns.
  • the amount of ammonium nitrate included is dependent upon the application for which the propellant composition is designed.
  • additives that increase the energy output (e.g., nitroplasticizers and/or energetic additives) of the first embodiment are preferably included therein.
  • nitroplasticizers and/or energetic additives are often omitted from the first embodiment.
  • nitroplasticizers and/or energetic additives may be optionally included therein.
  • the amount of ammonium nitrate included in the first embodiment is varied depending upon the presence or absence of nitroplasticizers and/or energetic additives therein.
  • the percent by weight values of the various propellant components denoted below refer to a percent of the total weight of the propellant composition.
  • the ammonium nitrate when used for gas producing applications, is present in an amount of at least about 60%.
  • the amount of ammonium nitrate present may range from about 65% to about 85%.
  • the amount of ammonium nitrate added when combined with optional nitroplasticizers and/or energetic additives, the amount of ammonium nitrate added may range from about 40% to about 80% (or any value therebetween) . In the absence of such nitroplasticizers and energetic additives, the amount of ammonium nitrate added to the first embodiment designed for propulsive applications ranges from about 65% to about 85%.
  • the first embodiment of the invention contains a molecular sieve.
  • molecular sieve is an aluminosilicate type molecular sieve, commonly referred to as a zeolite molecular sieve.
  • a zeolite molecular sieve is an aluminosilicate type molecular sieve, commonly referred to as a zeolite molecular sieve.
  • a zeolite molecular sieve commonly referred to as a zeolite molecular sieve.
  • An exemplary type A synthetic zeolite has the formula Na 12 ( (A10 2 ) 12 (Si0 2 ) 12 ) • 27H 2 0.
  • a molecular sieve is obtained by heating a zeolite to about 350°C under a vacuum to remove the water of hydration.
  • a typical molecular sieve such as Na 12 ( (Al 12 Si 12 0 48 ) • 27H 2 0
  • a type A zeolite with anhydrous cubic microcrystals is formed.
  • it must have two properties.
  • the molecular sieve must retain the absorbed water molecules so that the water is not available to any other component of the ammonium nitrate propellant composition, especially the ammonium nitrate. Thus, the retention of the water in the molecular sieve/water adduct must be extremely robust.
  • the water molecules must not be simply adsorbed onto the surface of the molecular sieve. It is believed that molecular sieves hold the water molecules within the pores present in the sieve. Further, without being bound by theory, it is believed that the water molecules may at first be adsorbed onto the surface of the molecular sieve. However, after a short period of time (e.g., up to about 48 hours) , the water molecules are transported to the interior of the molecular sieve via its pores.
  • a short period of time e.g., up to about 48 hours
  • the sieve has an adequate pore dimension (e.g., typically about 13 angstroms or less such as from about 3 to about 13 angstroms or any value therebetween) , then the water can be absorbed into the interior of the sieve.
  • the other components of the ammonium nitrate propellant composition e.g., binders, nitroplasticizers, energetic additives, nitrate ester stabilizers, curing agents, cure catalysts, opacifiers and/or anti-oxidants
  • the other components of the ammonium nitrate propellant composition e.g., binders, nitroplasticizers, energetic additives, nitrate ester stabilizers, curing agents, cure catalysts, opacifiers and/or anti-oxidants
  • a pore size sufficient for this purpose is about 13 angstroms or less.
  • the pore size is from about 3 to about 13 angstroms or any value therebetween. More preferably, the pore size is from about 3 to about 5 angstroms. The most preferred pore size is about 4 angstroms.
  • molecular sieves compatible with the first embodiment of the invention include, but are not limited to, molecular sieves type 3A, 4A, 5A and 13X, respectively. These sieves are made by various companies, including Union Carbide (N.Y., N.Y.) which sells its molecular sieves under the trademark LINDE ® .
  • Molecular Sieve 4A is a sodium form of the type A crystal structure. It is an alkali metal alumino-silicate. The type 4A sieve will absorb molecules with critical diameters up to about 4 angstroms.
  • the molecular sieve is present in an amount from about 0.02% to about 6% (or any value therebetween). Preferably, the molecular sieve is present from about 0.2% to about 0.4% and, most preferably, from about 0.20% to about 0.22%.
  • the preferred molecular sieve is the type 4A sieve.
  • Binders compatible with the first embodiment of the present invention include, but are not limited to, thermoplastic elastomers (e.g., FinapreneTM, KratonTM or mixtures thereof) and a cure hardening material.
  • cure hardening materials include, but are not limited to, a hydroxy terminated polybutadiene (HTPB) , hydroxy terminated polyether (HTPE) , polyglycol adipate (PGA) , glycidylazide polymer (GAP), poly bis-3 , 3 '-azido ethyl oxetane (BAMO) , poly-3-nitratomethyl-3-methyl oxetane (PNMMO) , polyethylene glycol (PEG) , polypropylene glycol (PPG) , cellulose acetate (CA) or mixtures thereof.
  • An exemplary binder is a mixture of 7 parts by weight of BAMO and 3 parts by weight of PNMMO.
  • the preferred binder is PGA. It is noted that other binders well-known in the art may be used.
  • nitroplasticizers are incompatible with HTPB (i.e., they are insoluble in one another), preferably, they are not combined in any of the embodiments of the propellant composition.
  • energetic additives e.g., solid phase nitramines such as RDX, HMX
  • other plasticizers such as dioctyl adipate (e.g., in an amount of about 3 to about 10% or any value therebetween) may be used.
  • Other plasticizers compatible with HTPB are well known to those skilled in the art and may be used therewith.
  • thermoplastic elastomeric binders compatible with the first, i.e., age-stabilized, embodiment of the present invention are those that have melting points or plasticized melting points above the expected use and storage temperatures of the propellant compositions. Typically, the use and storage temperatures range from about -65°F to about 200°F. Further, the thermoplastic elastomers must melt in their plasticized state below the decomposition temperature of ammonium nitrate and/or any nitroplasticizer present therein. In the first embodiment, the binder is present from about 3% to about 40% (or any value therebetween) , preferably, from about 5% to about 30%.
  • the first embodiment may additionally contain an energetic additive (i.e., a solid phase component that increases energy output, e.g., some nitramines) and/or a nitroplasticizer (i.e., a liquid phase component that increases energy output, e.g., some nitrate esters and some nitramines) .
  • an energetic additive i.e., a solid phase component that increases energy output, e.g., some nitramines
  • a nitroplasticizer i.e., a liquid phase component that increases energy output, e.g., some nitrate esters and some nitramines
  • Typical nitroplasticizers compatible with the age-stabilized ammonium nitrate propellant composition (i.e., the first embodiment) of the present invention include, but are not limited to, tri ethylol ethane trinitrate (TMETN) , triethylene glycol dinitrate (TEGDN) , triethylene glycol trinitrate (TEGTN) , butanetriol trinitrate (BTTN) , diethyleneglycol dinitrate (DEGDN) , ethyleneglycol dinitrate (EGDN) , nitroglycerine (NG) , diethylene glycerin trinitrate (DEGTN) , dinitroglycerine (DNG) , nitrobenzene (NB) , N-butyl-2- nitratoethylnitramine (BNEN) , methy1-2-nitratoethylnitramine
  • the preferred nitroplasticizer is a 50-50 by weight mixture of TMETN and TEGDN.
  • the nitroplasticizer is optionally present up to about 40% by weight.
  • energetic additives compatible with the first embodiment include, but are not limited to, dinitroxydiethylnitramine (DNDEN) , cyclotrimethylene trinitramine (RDX) , cyclotetramethylene tetranitramine (HMX) or mixtures thereof.
  • the preferred energetic additives are RDX, HMX or mixtures thereof. In the first embodiment, they are preferably present up to about 40%. As other similar nitroplasticizers and energetic additives become commercially available, they can be included in this list as one of ordinary skill in the art would recognize.
  • nitroplasticizers and energetic additives tend to increase the energy output, flame temperature and explosive nature of an ammonium nitrate propellant composition, these materials are not always included within the first embodiment of the invention when used for gas producing applications, rather they may be optionally included therein.
  • the nitroplasticizer and/or energetic additive may be present (i.e., as an optional additive) in an amount of up to about 35%.
  • the nitroplasticizer and/or energetic additive is typically present in an amount from about 5% to about 40% or any value therebetween.
  • the amounts of the binder plus any nitroplasticizer and energetic additive must total at least about 20% to form a physically acceptable first embodiment and, preferably, from about 20% to about 35%.
  • physically acceptable means a composition that can be formed into various desirable shapes, (e.g., grains, etc.) and which can be maintained in those shapes.
  • a nitroplasticizer which is a nitrate ester is included in the first embodiment, it is preferred that a nitrate ester stabilizer be added as well.
  • the nitrate ester stabilizer may be omitted from the propellant composition.
  • the nitrate ester stabilizer may be present in an amount of up to about 3%, more preferably, from about 0.1% to about 2% and, most preferably, from about 0.35% to about 0.5%.
  • Nitrate ester stabilizers compatible with the first embodiment of the present invention include, but are not limited to, N-methyl- 4-nitroaniline (MNA) , 2-nitrodiphenylamine (NDA) , ethyl centralite (EC) or mixtures thereof.
  • MNA N-methyl- 4-nitroaniline
  • NDA 2-nitrodiphenylamine
  • EC ethyl centralite
  • the preferred nitrate ester stabilizer is a mixture of MNA and NDA, preferably, in a weight ratio of about 1:1.
  • Curing agents compatible with the first embodiment of the present invention include, but are not limited to, hexamethylene diisocyanate (HMDI) , isophorone diisocyanate (IPDI) , toluene diisocyanate (TDI) , trimethylxylene diisocyanate (TMDI) , dimeryl diisocyanate (DDI) , diphenylmethane diisocyanate (MDI) , naphthalene diisocyanate (NDI) , dianisidine diisocyanate (DADI) , phenylene diisocyanate (PDI) , xylylene diisocyanate (MXDI) , other diisocyanates, triisocyanates, higher isocyanates than the triisocyanates, polyfunctional isocyanates (e.g., Desmodur N 100) , other polyfunctional isocyanates or mixtures thereof.
  • HMDI hexamethylene diiso
  • the isocyanate have at least two reactive isocyanate groups. If there are no binder ingredients with a functionality that is greater than 2, then the curative functionality (e.g., number of reactive isocyanate groups per molecule of isocyanate curing agent) must be greater than 2.0.
  • the amount of the curing agent is determined by the desired stoichiometry (i.e., stoichiometry between curable binder and curing agent) .
  • the curing agent is present in an amount of up to about 5%. However, if a curable binder (e.g., binder having reactive hydroxy1 groups such as HTPB) is used, the curing agent is present from about 0.5% to about 5%.
  • a cure catalyst is preferably added to the propellant composition.
  • the cure catalyst is used to accelerate the curing reaction between the curable binder and the curing agent.
  • Cure catalysts compatible with the first embodiment of the present invention include, but are not limited to, a tin dilaurate (e.g., an alkyl tin dilaurate, butyl tin dilaurate, isopropyl tin dilaurate etc.), metal acetylacetonate, triphenyl bismuth, maleic anhydride, magnesium oxide or mixtures thereof.
  • a preferred cure catalyst is an equal % by weight mixture (i.e., 33 1/3%) of each of triphenyl bismuth, maleic anhydride and magnesium oxide.
  • the cure catalyst is present up to about 0.3% by weight.
  • one opacifier which is compatible with the first embodiment is carbon black.
  • the opacifier is present up to about 2%. Those skilled in the art are aware of other opacifiers that may be used.
  • Antioxidants may also be added to the first embodiment of the present invention.
  • Antioxidants compatible with the first embodiment of the present invention include, but are not limited to, 2, 2 '-bis (4-methyl-6-tert- butylphenol) , 4,4 '-bis (4-methyl-6-tert-butylphenol) or mixtures thereof.
  • Other antioxidants well known in the art are within the scope of the present invention. The antioxidant is present in an amount of up to about 1%.
  • the propellant composition comprises ammonium nitrate, a strengthening agent and a binder.
  • the ammonium nitrate component included in this embodiment is the same as that previously described with respect to the first embodiment.
  • Preferred strengthening agents compatible with the second embodiment of the present invention include, but are not limited to, azodicarbonamide, dicyandiamide, oxamide or mixtures thereof.
  • the most preferred strengthening agent is azidocarbonamide.
  • the strengthening agent is present in an amount from about 2% to about 20%.
  • the strengthening agent is present from about 3% to about 12% and, most preferably, from about 8% to about 12%.
  • Optional additives compatible with the second embodiment include, but are not limited to, a curing agent, a cure accelerator, a nitroplasticizer, an energetic additive, a nitrate ester stabilizer, an opacifier, and/or an antioxidant.
  • the binders, nitroplasticizers, energetic additives, nitrate ester stabilizers, curing agents, cure catalysts, opacifiers and/or anti-oxidants compatible with the first embodiment are equally compatible with the second embodiment. Further, the amounts of ammonium nitrate, nitroplasticizer, energetic additive, nitrate ester stabilizer, curing agent, cure catalyst, opacifier and/or anti-oxidant described with respect to the first embodiment are equally applicable to the second embodiment.
  • the binder included in the second embodiment is present in an amount from about 3% to about 40% or any value therebetween.
  • the binder is preferably present in the subject embodiment in an amount from about 3% to about 20%.
  • the binder plus any nitroplasticizer and energetic additive must total at least about 20% to form a physically acceptable second embodiment and, preferably, from about 20% to about 35%. It should be noted that the second embodiment does not contain a molecular sieve.
  • a strengthening agent to a propellant composition reduces its impulse.
  • nitroplasticizers and/or energetic additives are added.
  • ammonium nitrate propellant compositions lose their detonatable characteristic when the impulse is less than or equal to about 229 lb. force - seconds/lb. mas ⁇ .
  • a sufficient amount of one or more nitroplasticizers and/or energetic additives is added to an ammonium nitrate propellant composition containing a strengthening agent, then the advantages of the strengthening agent are obtained without loss of impulse.
  • this embodiment comprises ammonium nitrate, a molecular sieve, a strengthening agent and a binder.
  • ammonium nitrates, molecular sieves, strengthening agents, binders, nitroplasticizers, energetic additives, nitrate ester stabilizers, curing agents, cure catalysts, opacifiers and/or anti-oxidants compatible with the first and/or second embodiments are equally compatible with the third embodiment.
  • the amounts of ammonium nitrate, nitroplasticizer, energetic additive, nitrate ester stabilizer, curing agent, cure catalyst, opacifier and/or anti-oxidant described with respect to the first and/or second embodiments are equally applicable to the third embodiment.
  • the third embodiment contains both a molecular sieve and a strengthening agent in accordance with the first and second embodiments, respectively.
  • the amounts of strengthening agent added to the second embodiment are equally applicable to this third embodiment.
  • the amounts of the molecular sieve added to the first embodiment are equally applicable to the third embodiment.
  • the binder is present in an amount from about 5% to about 30%.
  • the binder plus any nitroplasticizer and energetic additive must total at least about 20% to form a physically acceptable third embodiment and, preferably, from about 20% to about 35%.
  • the molecular sieve to be ultimately added is mixed with the ammonium nitrate.
  • the molecular sieve is added to the extent of at least about 1 gram per pound of ammonium nitrate.
  • the mixture of the ammonium nitrate and the molecular sieve may be allowed to stand for a first aging period.
  • the first aging period is up to about 48 hours or longer, preferably, from about 0.25 hour to about 16 hours and, most preferably, as close to zero as possible.
  • the mixture of the molecular sieve and the ammonium nitrate is exposed to the ambient air (i.e., including the moisture therein) , it is preferably ground immediately after mixing (i.e., the first aging period is zero minutes or nearly so) . If, however, the mixture is held in a sealed container (i.e., with limited exposure to ambient air and the moisture therein) , then the mixture may be maintained indefinitely without grinding.
  • the first aging period may be up to about 48 hours (or more) such as from about 4 to about 16 hours. However, it is preferred to grind the mixture immediately (or, for example, as soon as it is practical to do so on a production or assembly line) after mixing to yield a first mixture.
  • grinding allows the molecular sieve to be in closer physical proximity to the ammonium nitrate and the water associated with it. Thereby, it is further believed that grinding allows the molecular sieve to more effectively and efficiently absorb (and retain) water away from the ground ammonium nitrate.
  • the particle characteristics e.g., particle thickness, particle size, particulate for —grains, prills, crystals size etc.
  • the size of the ammonium nitrate should be, as previously noted, from about 5 microns to about 400 microns, preferably, from about 30 microns to about 50 microns in thickness.
  • first aging period zero hours
  • second mixture the remaining components of the propellant composition (except for any curing agent) are added to the first mixture to yield a second mixture. Thereafter, the second mixture is allowed to stand for a second aging period.
  • the second aging period allows the molecular sieve to absorb (and retain) a sufficient amount of the water present to age-stabilize the second mixture.
  • the second aging period is up to about 48 hours or longer, preferably, from about 0.25 hour to about 24 hours and, most preferably, from about 16 to about 24 hours.
  • the curing agent if any, (e.g., isocyanate curing agent) is optionally added to the second mixture to complete and form the final age- stabilized ammonium nitrate propellant composition or the final age-stabilized/strengthened propellant composition.
  • the propellant composition of Example 8, infra was prepared wherein the first aging period was set to zero hours and the second aging period was set to zero, 2 hours and 48 hours, respectively.
  • the effect of varying the second aging period on hardness (Shore A) , ultimate tensile strength (psi) and elongation at break (%) for the propellant composition of Example 8, infra is given in Table III below.
  • Elongation is an indication of elasticity. It indicates the length through which the propellant composition can be stretched before it breaks.
  • An increase in tensile strength with a concurrent increase in elongation indicates an increase in "toughness” .
  • the increase in "toughness” indicates that less damage will occur in bullet or fragment impact scenarios. Less damage means less surface area to burn and therefore the reaction to unplanned stimuli (e.g., bullet or fragment impact) will be less violent.
  • the aging periods significantly increase the shelf-life (e.g., to 20 years or more) of the ammonium nitrate propellant composition.
  • the ammonium nitrate is ground by ball milling, fluid energy milling or micropulverizing. Other grinding methods well known in the art may also be used. Thereafter, the ground ammonium nitrate is mixed with the remainder of the other components of the propellant composition, including the strengthening agent.
  • a strengthening agent e.g., the second embodiment
  • the ground ammonium nitrate is mixed with the remainder of the other components of the propellant composition, including the strengthening agent.
  • an increase in the elasticity and the maximum stress of a propellant composition indicates that the propellant composition is less prone to cracking, etc. , and less prone to violent deflagration or premature explosion.
  • propellant compositions were prepared using the components in the quantities indicated below. However, where indicated the examples are prophetic. It should be noted that in all the prophetic examples, a nitrate ester plasticizer and a cure catalyst are included where appropriate as previously explained. Further, all components in each formulation add up to a total of 100% by weight.
  • Prophetic examples 9, 10, 11 and 12 indicate age-stabilized and mildly strengthened propellant compositions with a slight loss in propellant composition impulse.
  • Prophetic examples 13, 14, 15 and 16 indicate age-stabilized and moderately strengthened propellant compositions with a moderate loss in propellant composition impulse.
  • Prophetic examples 17, 18, 19 and 20 indicate age-stabilized and strongly strengthened propellant compositions with a significant loss in propellant composition impulse.
  • Example 1 (Age-Stabilized) Chemical Component Relative Percentage by Weight
  • Cellulose acetate (4.0 grams) was dissolved in 25 ml of acetone.
  • AN was ground according to Example 21 without molecular sieve being added.
  • Ground AN 60 grams
  • RDX 36 grams
  • Acetone was added as necessary to form a thick paste.
  • the paste was then formed into sheets or extruded into strands or made into granules by screening while still damp.
  • 7019-A was formed into sheets about 0.030 inches thick, then dried in a vacuum oven at 140°F. The sheets were then broken into smaller pieces and then screened through a 5 mesh screen.
  • composition 7019-A with age-stabilization The procedure followed was the same as Example 22 except that the AN was ground with molecular sieve according to Example 21.
  • Example 24 (Strengthened Propellant Composition) The same procedure as in Example 7 was followed except that the molecular sieve was omitted from the composition. The amount of binder was increased by 0.22% by weight. Otherwise the procedure followed was identical to Example 7.
  • Example 7 The same procedure as in Example 7 was followed except that the strengthening agent was omitted from the composition. The amount of binder was increased by 4.0% by weight. Otherwise the procedure followed was identical to Example 7.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Dispersion Chemistry (AREA)
  • Molecular Biology (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Air Bags (AREA)

Abstract

The present invention is directed to an age-stabilized and/or strengthened ammonium nitrate propellant composition wherein the strengthening agent is selected from the group consisting of azodicarbonamide, dicyandiamide, oxamide and mixtures thereof and wherein the age-stabilizing agent is a molecular sieve having a pore size of 13 angstroms or less.

Description

AMMONIUM NITRATE PROPELLANTS WITH MOLECULAR SIEVE
FIELD OF THE INVENTION
The present invention is directed to ammonium nitrate propellant compositions. More particularly, it is directed to age-stabilized and/or strengthened ammonium nitrate propellant compositions and methods for making the same.
BACKGROUND OF THE INVENTION
Propellant compositions are useful for a variety of applications. One such application is in vehicle air bag restraint devices. In such restraint devices, it is important to reduce the toxicity of gases produced upon combustion of the propellant. It is also desirable that the propellant composition burn in a smokeless or nearly smokeless fashion because the presence of smoke can cause various problems. For example, after an accident in which an air bag has been deployed, smoke not only hinders visibility, it also interferes with any ongoing rescue efforts. Thus, it is desirable that propellant composition combustion products be smoke-free or nearly so.
Another application of propellant compositions is their use in rockets and in other munitions as propulsive propellant compositions. Combustion of propulsive propellant compositions in rockets and the like provides the energy required to transport them over long distances towards a given target. During battle, it is critical to maintain the advantage of surprise and stealth. Therefore, it is desirable that rockets powered by propulsive propellant compositions be as undetectable as possible upon launch and during deployment.
To maintain the advantages of stealth and surprise, it is important that the propellant composition be smoke-free or nearly so during combustion. In an effort to meet the requirement of a smoke-free combustible propellant composition, several compositions have been developed by the U.S. military. Among the compositions developed are the "double base" propellant compositions. As is known in the art, "double base" refers to a propellant composition containing both nitroglycerine (NG) and nitrocellulose (NC) . Double base propellants are prone to premature explosion or premature deflagration in response to various unplanned stimuli (e.g., fire, heat, shrapnel, bullets, other fragments etc.) that may be encountered in battle. In addition, for propulsive applications, the energy output upon combustion of double base propellants is sometimes insufficient. Thus, the addition of energetic additives such as cyclotetramethylene tetranitramine (HMX) and/or cyclotrimethylene trinitramine (RDX) is often required to provide the energy output sought during combustion. However, the addition of such energetic additives exacerbates the already hazardous tendency of double base propellants to premature explosion or premature deflagration.
Nevertheless, to fulfill the smoke free and high energy requirements of propulsive propellants, as defined herein, propellant compositions including double base propellants were pursued at the expense of safety, especially in regards to naval operations. Consequently, the U.S. Navy has taken the lead in formulating a series of standards concerning insensitive ammunition requirements, formalized as MIL-STD-2105B, incorporated herein by reference in its entirety. Equivalent insensitive ammunition standards have been adopted by most major military powers (e.g., England, France, Germany, etc.). These standards require that propellant compositions meet or exceed insensitive ammunition safety standards for the weapons platforms for which they were designed.
Further, with regards to military propulsive applications, various smoke characteristics required of propellant compositions have been strictly defined. Based on the empirical work performed by the U.S. Missile Command at Redstone Arsenal and some of their counterparts in other countries, industry accepted definitions of "minimum smoke" and "reduced smoke" have been promulgated in STANAG 6016 (NATO Standardized Agreement Solid Propellant Smoke Classification) . STANAG 6016 is incorporated herein by reference in its entirety. The smoke effluent is calculated by a number of thermo-chemical codes that are well known in the industry. For example, STANAG 6016 classifications "AA" and "AC" correspond to the definitions of minimum smoke and reduced smoke, respectively. The "smoke-free", "nearly smoke free" and/or "substantially smoke free" terms as used herein are synonymous with the definition of minimum smoke (i.e., code AA) .
To meet these requirements (i.e. , smoke free— minimum smoke in accordance with STANAG 6016; high energy output and safety—in accordance with Insensitive Ammunitions Requirements formalized as MIL-STD-2105B) attempts have been made to develop non-double base propellant compositions that are smoke free, yet safe for handling. For example, ammonium nitrate, metal nitrate, alkali earth metal nitrate, ammonium perchlorate and metal perchlorate propellant compositions and the like have been used. However, these propellant compositions present several problems. Metal nitrates, typically, produce solid particles upon combustion. These solid particles form a visible smoke referred to as "primary smoke" which is undesirable. Ammonium or metal perchlorates produce hydrogen chloride during combustion. Hydrogen chloride reacts with moisture in the ambient air to yield a liquid/gas aerosol. The aerosol forms another visible smoke referred to as "secondary smoke". Either "primary smoke" or "secondary smoke" formed as an effluent from the combustion of a propulsive propellant composition negates the advantage of surprise. The smoke trail aids opposing forces in destroying or otherwise countering the incoming missile. In addition, such effluent smoke points to the launch position. During battle, such smoke places launch personnel in greater danger of potentially successful retaliation, e.g., by counter battery fire. Ammonium nitrate as a propellant ingredient may produce a propellant that does not produce primary or secondary smoke upon combustion. However, ammonium nitrate presents other drawbacks as a propellant component. Principally, it is recognized that ammonium nitrate undergoes several crystal phase changes at various well-recognized temperatures. Pure ammonium nitrate undergoes a series of structural and volumetric crystal phase transformations over typical operating temperature ranges. In pure ammonium nitrate, structural crystal phase transitions are observed at about -18°C, 32.3°C, 84.2°C and 125.2°C, respectively. The phase transition at about 32.3°C is particularly troublesome. A large volumetric change (about 3.7%) in the crystal phase of ammonium nitrate is observed when the temperature cycles above and below about 32.3°C (i.e., transition between phase IV (below 32.3°C) and phase III (above 32.3°C)). As the ammonium nitrate cycles between phase IV and phase III, it expands and contracts. Repeated cycling through the phase IV to phase III transition temperature (i.e., about 32.3°C) is associated with ammonium nitrate grain growth and destruction of grain integrity. The result is that there is porosity and loss in mechanical strength of ammonium nitrate based propellant compositions.
As used herein, the term "age-stabilized" refers to a state of ammonium nitrate wherein the crystal phase III-IV and volumetric changes associated with thermal cycling are substantially reduced. Thus, the shelf-life of an ammonium nitrate propellant composition is considerably increased from about 1-2 years to about 5-20 years or more. Further, the term "strengthened", as used herein, refers to a state of ammonium nitrate propellant wherein the tensile strength of the propellant is increased without unduly sacrificing elongation or, alternatively, is accompanied by an increase in elongation. The strengthened ammonium nitrate propellant composition is substantially resistant to physical destruction of the propellant. As also used herein, the term "safe" refers to an ammonium nitrate propellant composition that meets or exceeds the insensitive ammunition requirements promulgated in MIL- STD-2105B wherein the tendency to violent deflagration or explosion is substantially reduced and the shelf-life is substantially increased from about 1-2 years to about 5-20 years or more. Further, the term "safe" is used herein to refer to an ammonium nitrate propellant composition wherein the tendency to form grain fissures due to crystal phase changes is substantially reduced or altogether eliminated. It is feared that non-strengthened/non-age- stabilized ammonium nitrate propellant compositions that have been stored (e.g., either in munitions or in vehicle air bag restraint devices) for more than about 1 to 2 years may have undergone several crystal phase changes to the extent that the physical integrity of the propellant has been compromised and the propellant will no longer perform in the desired manner. Consequently, the useful shelf-life of prior art ammonium nitrate propellant compositions is disadvantageously shortened. Thus, it is desirable to formulate a smoke-free (or substantially smoke free) yet safe ammonium nitrate propellant composition having an extended shelf-life.
Typically, a propulsive or gas generating device containing a propellant composition requires a shelf-life from about 5 to about 20 years or more. The shelf-life of the device is largely dependent on the shelf-life of the propellant composition contained therein. Typically, a desirable shelf-life for a munition (propulsive) propellant composition or a vehicle air bag (gas producing) propellant composition is about 5 or more years, preferably, from about 7 to 20 years. In order to obtain longer shelf-life ammonium nitrate propellant compositions, efforts have been directed at solving the crystal phase stabilization problem (i.e., of ammonium nitrate) . For example, various patents and publications suggest the use of KN03, KF, metal dinitramide, or metal oxides such as MgO, NiO, CuO and/or ZnO as additives that yield phase stabilized ammonium nitrate. See, for example U.S. Patent No. 4,158,583 to Anderson; U.S. Patent No. 5,076,868 to Doll et al.; U.S. Patent 5,271,778 to Bradford et al.; U.S. Patent No. 5,292,387 to Highsmith et al; and U.S. Patent No. 4,552,736 to Mishra; U.S. Patent No. 5,545,272 to Poole et al. See also, Choi, C.S., and Prask, H.J., Phase Transitions in Ammonium Nitrate, J. Appl. Cryst. , Vol. 13, pp. 403-409 (1980).
However, various problems are associated with the use of the aforementioned phase stabilizing additives. For example, the use of potassium nitrate leads to the formation of large amounts of undesirable residue as combustion products. See U.S. Patent 4,552,736 to Mishra. When KF is used, it must be added to the molten phase (I) of ammonium nitrate. Thereafter, the KF modified ammonium nitrate is cooled. The requirement for melting ammonium nitrate before adding KF is cumbersome, expensive and time consuming. In addition, the effluent of a device using such a propellant is corrosive, smoky (with an enhanced radar cross section) and toxic. The use of the metal oxides also has several drawbacks. For example, solid particulates are formed upon combustion when MgO, NiO, CuO and/or ZnO are used. Solid particulates, as previously noted, contribute to the formation of primary smoke which is undesirable. Additionally, NiO is carcinogenic. Further, NiO and CuO present environmental hazards. In addition, both NiO and ZnO are only marginally effective. That is, once exposed to moisture, these oxides are no longer effective ammonium nitrate phase stabilizers. Further, NiO and ZnO increase the detonatability of the ammonium nitrate which is undesirable. Additionally, manufacturing propellant compositions including NiO and/or ZnO is more expensive. Similarly, the use of metal dinitra ides (see '387 to Highsmith et al.) also leads to the formation of primary smoke upon combustion. Thus, none of the known ammonium nitrate phase stabilizers are entirely satisfactory for forming a safe, age-stabilized and smoke-free ammonium nitrate propellant composition having a long shelf-life.
The occurrence of phase III in ammonium nitrate depends on the presence of water, e.g., down to as little as about 0.1% by weight of the ammonium nitrate. See Choi et al., J. Appl. Cryst., Vol. 13, p. 403 (1980). In particular, according to the '736 patent to Mishra, supra , (at column 2, lines 66-68) , a high moisture content is said to favor III-IV phase transitions. Further, according to U.S. Patent No. 4,486,396 to Kjohl et al., (at column 1, lines 30-32), these phase transitions render the ammonium nitrate less stable to thermal cycling.
U.S. Patent No. 5,061,511 to Baczuk ('511) suggests the use of aluminum silicate molecular sieves (having a pore size of less than about 10 angstroms) as a stabilizer in propellant compositions such as single base or double base propellant. In particular, the '511 patent is directed to propellant compositions that give off gases during the aging process. These propellant compositions include nitrocellulose and nitroglycerin, high energy fluorine containing propellants, single or double base nitrate ester propellants and composite propellants such as ammonium perchlorate/Al with rubber binders. The undesirable gases given off by these propellants during aging include N2, C02, CO, N0X and F2. Likewise, U.S. Patent No. 4,045,261 to Baczuk ('261) suggests the use of a molecular sieve (having a pore size of 10 angstroms or more) as part of a stabilization system for a urethane cross-linked double base propellant composition to scavenge nitric acid. Since ammonium nitrate is not a propellant of the class described by Baczuk (i.e., See '511) and it does not give off the N2, C02, CO, N0X or F2 gases (i.e., see '511) during aging, there is no expectation that molecular sieves in general, much less those having a pore size of 10 angstroms or less would stabilize ammonium nitrate.
Similarly, since ammonium nitrate is not a urethane cross- linked double base propellant (i.e., see '261), there is, likewise, no expectation that molecular sieves, e.g., having a pore size of 10 angstroms or more, would stabilize ammonium nitrate against volumetric crystal phase changes.
Nevertheless, since water is associated with the undesirable crystal phase changes of ammonium nitrate, Kjohl et al., supra , used porous additives which could absorb water to stabilize ammonium nitrate. They further discovered that the presence of water absorbing porous particles resulted in no movement of water in the ammonium nitrate particles and that, during thermal cycling, swelling of ammonium nitrate was observed only to a small extent. Kjohl et al., however, state that the porous particles should be added to the ammonium nitrate after the ammonium nitrate is dried. Finally, they state that not any type of porous particle is suitable for stabilizing ammonium nitrate. For example, according to Kjohl et al., silicates of the molecular sieve type can bind water, but it has been found difficult to give such particles the required particle size and binding to the ammonium nitrate particles. In effect, Kjohl et al. conclude that molecular sieves performed poorly in stabilizing ammonium nitrates (see column 3, lines 18-23).
Thus, there is still an existing need to provide a safe, age-stabilized and/or strengthened ammonium nitrate propellant composition having a long shelf-life that is substantially smoke free upon combustion as well as a method for making the same.
SUMMARY OF THE INVENTION
It is therefore an object of the present invention to provide a safe, age-stabilized, substantially smoke-free ammonium nitrate propellant composition that has a long shelf-life (e.g., up to about 20 years or more) and to provide a method of making the same.
It is another object of the present invention to provide a strengthened, substantially smoke-free ammonium nitrate propellant composition that has a long shelf-life and to provide a method for making the same. It is a still further object of the present invention to provide a strengthened and age-stabilized, substantially smoke-free ammonium nitrate propellant composition that has a long shelf-life and to provide a method of making the same.
Surprisingly these and other objects are accomplished by the addition of silicates of the molecular sieve type to ammonium nitrate before grinding the ammonium nitrate present in the propellant composition. These objects are accomplished by an age-stabilized ammonium nitrate propellant composition comprising ammonium nitrate, a silicate molecular sieve and a binder. In addition, the process for forming a safe, age-stabilized ammonium nitrate propellant composition comprises the steps of providing a quantity of ammonium nitrate, adding a sufficient quantity of a silicate molecular sieve to absorb water from the ammonium nitrate, grinding the ammonium nitrate with the molecular sieve, maintaining contact between the ammonium nitrate and the sieve, then adding at least a binder (except any curing agent e.g., isocyanate curing agent), maintaining contact between the ground molecular sieve and the other ingredients and finally adding a curing agent, if any, to yield the safe, age-stabilized ammonium nitrate propellant composition having a long shelf-life. Alternatively, these and other objects are accomplished by the addition of a strengthening agent to a mixture of ammonium nitrate and at least a binder to yield a strengthened propellant composition. Further, a molecular sieve may also be added to the strengthened ammonium nitrate propellant to yield an enhanced, strengthened and age- stabilized ammonium nitrate propellant composition.
Additionally, an age-stabilized ammonium nitrate composition may be formed by adding a molecular sieve to ammonium nitrate (e.g., at least about 1 gram of a molecular sieve per pound of ammonium nitrate) and then grinding the mixture. Thereafter, the mixture may be safely stored without deleterious changes for an extended period of time in a sealed container.
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The following detailed description is provided to aid those skilled in the art in practicing the present invention. However, it should not be construed to unduly limit the scope of the invention. Variations and modifications in the embodiments discussed may be made by those of ordinary skill in the art without departing from the invention.
According to the present invention, there are at least three embodiments of the ammonium nitrate propellant composition. The first embodiment of the present invention relates to an age-stabilized ammonium nitrate propellant composition. The second embodiment relates to a strengthened ammonium nitrate propellant composition. The third embodiment relates to an age-stabilized and strengthened ammonium nitrate propellant composition. Further, each embodiment may be used, with certain modifications, as a gas producing ammonium nitrate propellant composition or as a propulsive ammonium nitrate propellant composition. The gas producing ammonium nitrate propellant compositions are designed to be used in vehicle air bag restraint systems and the like wherein gas production is paramount. The propulsive ammonium nitrate propellant compositions are designed to be used in rockets and other munitions wherein energy output is paramount.
In the first (i.e., age-stabilized) embodiment, the substantially smoke-free ammonium nitrate propellant composition comprises ammonium nitrate, a molecular sieve and a binder. Optionally, the first embodiment may contain one or more of a variety of additives. These additives include, but are not limited to, a nitroplasticizer (e.g., nitramines and/or nitrate esters which are in a liquid phase when added, typically, at room temperature such as at about 25°C) , an energetic additive (e.g., nitramines which are in a solid phase when added, typically, at room temperature) , a nitrate ester stabilizer, a curing agent, a cure accelerator, an opacifier and a polymer protector (i.e., an antioxidant) . In the first embodiment, the ammonium nitrate may be present as fines, prills, granules and the like. The size of the ammonium nitrate may vary between about 5 microns and about 5,000 microns (or any value therebetween) in thickness. However, a particle thickness is, preferably, from about 5 microns to about 400 microns and, most preferably, from about 30 to about 50 microns.
In the first embodiment, the amount of ammonium nitrate included is dependent upon the application for which the propellant composition is designed. For example, in propulsive applications, additives that increase the energy output (e.g., nitroplasticizers and/or energetic additives) of the first embodiment are preferably included therein. On the other hand, if designed for gas producing applications, such nitroplasticizers and/or energetic additives are often omitted from the first embodiment. However, nitroplasticizers and/or energetic additives may be optionally included therein. The amount of ammonium nitrate included in the first embodiment is varied depending upon the presence or absence of nitroplasticizers and/or energetic additives therein. Unless otherwise specifically indicated, the percent by weight values of the various propellant components denoted below refer to a percent of the total weight of the propellant composition. In the first embodiment, when used for gas producing applications, the ammonium nitrate (when a nitroplasticizer and/or energetic additive is added) is present in an amount of at least about 60%. When nitroplasticizers and energetic additives are omitted from the first embodiment designed for gas producing applications, the amount of ammonium nitrate present may range from about 65% to about 85%.
However, for propulsive applications of the first embodiment, when combined with optional nitroplasticizers and/or energetic additives, the amount of ammonium nitrate added may range from about 40% to about 80% (or any value therebetween) . In the absence of such nitroplasticizers and energetic additives, the amount of ammonium nitrate added to the first embodiment designed for propulsive applications ranges from about 65% to about 85%.
Further, as noted, the first embodiment of the invention contains a molecular sieve. One type of molecular sieve is an aluminosilicate type molecular sieve, commonly referred to as a zeolite molecular sieve. See, for example, Breck, D.W., Crystalline Molecular Sieves, Journal of Chemical Education, Vol. 41, p. 678 (December 1964) . See UOP, Product Information Sheet, Union Carbide Molecular Sieves, Molecular Sieve Type 4A. See also, LINDE® Molecular Sieves Data, LINDE® Molecular Sieve Type 4A. See also,
Cotton, F.A. and Wilkinson, G. , Advanced Inorganic Chemistry- A Comprehensive Text, pp. 390-392, 4th Ed., John Wiley and Sons (New York 1980) . Typical zeolites have the formula Mex/n( (A102)x(Si02)y) Z H20 wherein Me = metal cation, and x, y and n are integers. Z is zero or a positive real number. Z indicates the number of waters of hydration associated with a given zeolite. Typically, y/x varies from about 1 to about 5. An exemplary type A synthetic zeolite has the formula Na12 ( (A102)12 (Si02)12) 27H20. As noted by Cotton & Wilkinson, supra , a molecular sieve is obtained by heating a zeolite to about 350°C under a vacuum to remove the water of hydration. Thus, once water is removed from a typical molecular sieve such as Na12 ( (Al12Si12048) 27H20, a type A zeolite with anhydrous cubic microcrystals is formed. For a particular molecular sieve to be appropriate for use in the first embodiment, it must have two properties. It must be a more active absorber of water than any other component (e.g., the ammonium nitrate, the binder etc.) of the ammonium nitrate propellant composition with the exception of the curing agent (i.e., in the presence of water, e.g., isocyanate curing agents typically react rapidly therewith) . Further, the molecular sieve must retain the absorbed water molecules so that the water is not available to any other component of the ammonium nitrate propellant composition, especially the ammonium nitrate. Thus, the retention of the water in the molecular sieve/water adduct must be extremely robust.
In particular, without being bound by theory, it is believed that the water molecules must not be simply adsorbed onto the surface of the molecular sieve. It is believed that molecular sieves hold the water molecules within the pores present in the sieve. Further, without being bound by theory, it is believed that the water molecules may at first be adsorbed onto the surface of the molecular sieve. However, after a short period of time (e.g., up to about 48 hours) , the water molecules are transported to the interior of the molecular sieve via its pores. Again without being bound by theory, it is believed that if the sieve has an adequate pore dimension (e.g., typically about 13 angstroms or less such as from about 3 to about 13 angstroms or any value therebetween) , then the water can be absorbed into the interior of the sieve. Thus, the other components of the ammonium nitrate propellant composition (e.g., binders, nitroplasticizers, energetic additives, nitrate ester stabilizers, curing agents, cure catalysts, opacifiers and/or anti-oxidants) are sterically isolated from the absorbed water.
As noted, for the molecular sieve to successfully age-stabilize ammonium nitrate, it is required that the molecular sieve have a pore size sufficient to absorb and ultimately retain water. Thereby, the absorbed water becomes unavailable to the ammonium nitrate and the other components of the propellant composition. Typically, a pore size sufficient for this purpose is about 13 angstroms or less. Preferably, the pore size is from about 3 to about 13 angstroms or any value therebetween. More preferably, the pore size is from about 3 to about 5 angstroms. The most preferred pore size is about 4 angstroms. Examples of molecular sieves compatible with the first embodiment of the invention include, but are not limited to, molecular sieves type 3A, 4A, 5A and 13X, respectively. These sieves are made by various companies, including Union Carbide (N.Y., N.Y.) which sells its molecular sieves under the trademark LINDE®. Molecular Sieve 4A is a sodium form of the type A crystal structure. It is an alkali metal alumino-silicate. The type 4A sieve will absorb molecules with critical diameters up to about 4 angstroms.
In the first embodiment of the propellant composition, the molecular sieve is present in an amount from about 0.02% to about 6% (or any value therebetween). Preferably, the molecular sieve is present from about 0.2% to about 0.4% and, most preferably, from about 0.20% to about 0.22%. The preferred molecular sieve is the type 4A sieve. Binders compatible with the first embodiment of the present invention include, but are not limited to, thermoplastic elastomers (e.g., Finaprene™, Kraton™ or mixtures thereof) and a cure hardening material. Examples of cure hardening materials include, but are not limited to, a hydroxy terminated polybutadiene (HTPB) , hydroxy terminated polyether (HTPE) , polyglycol adipate (PGA) , glycidylazide polymer (GAP), poly bis-3 , 3 '-azido ethyl oxetane (BAMO) , poly-3-nitratomethyl-3-methyl oxetane (PNMMO) , polyethylene glycol (PEG) , polypropylene glycol (PPG) , cellulose acetate (CA) or mixtures thereof. An exemplary binder is a mixture of 7 parts by weight of BAMO and 3 parts by weight of PNMMO. However, the preferred binder is PGA. It is noted that other binders well-known in the art may be used.
Because nitroplasticizers are incompatible with HTPB (i.e., they are insoluble in one another), preferably, they are not combined in any of the embodiments of the propellant composition. When HTPB is the binder of choice, energetic additives (e.g., solid phase nitramines such as RDX, HMX) and/or other plasticizers such as dioctyl adipate (e.g., in an amount of about 3 to about 10% or any value therebetween) may be used. Other plasticizers compatible with HTPB are well known to those skilled in the art and may be used therewith.
The thermoplastic elastomeric binders compatible with the first, i.e., age-stabilized, embodiment of the present invention are those that have melting points or plasticized melting points above the expected use and storage temperatures of the propellant compositions. Typically, the use and storage temperatures range from about -65°F to about 200°F. Further, the thermoplastic elastomers must melt in their plasticized state below the decomposition temperature of ammonium nitrate and/or any nitroplasticizer present therein. In the first embodiment, the binder is present from about 3% to about 40% (or any value therebetween) , preferably, from about 5% to about 30%. Further, as previously noted, the first embodiment may additionally contain an energetic additive (i.e., a solid phase component that increases energy output, e.g., some nitramines) and/or a nitroplasticizer (i.e., a liquid phase component that increases energy output, e.g., some nitrate esters and some nitramines) . Typical nitroplasticizers compatible with the age-stabilized ammonium nitrate propellant composition (i.e., the first embodiment) of the present invention include, but are not limited to, tri ethylol ethane trinitrate (TMETN) , triethylene glycol dinitrate (TEGDN) , triethylene glycol trinitrate (TEGTN) , butanetriol trinitrate (BTTN) , diethyleneglycol dinitrate (DEGDN) , ethyleneglycol dinitrate (EGDN) , nitroglycerine (NG) , diethylene glycerin trinitrate (DEGTN) , dinitroglycerine (DNG) , nitrobenzene (NB) , N-butyl-2- nitratoethylnitramine (BNEN) , methy1-2-nitratoethylnitramine
(MNEN) , ethyl-2-nitratoethylnitramine (ENEN) or mixtures thereof. The preferred nitroplasticizer is a 50-50 by weight mixture of TMETN and TEGDN. In the first embodiment, the nitroplasticizer is optionally present up to about 40% by weight. Examples of energetic additives compatible with the first embodiment include, but are not limited to, dinitroxydiethylnitramine (DNDEN) , cyclotrimethylene trinitramine (RDX) , cyclotetramethylene tetranitramine (HMX) or mixtures thereof. The preferred energetic additives are RDX, HMX or mixtures thereof. In the first embodiment, they are preferably present up to about 40%. As other similar nitroplasticizers and energetic additives become commercially available, they can be included in this list as one of ordinary skill in the art would recognize.
Because nitroplasticizers and energetic additives tend to increase the energy output, flame temperature and explosive nature of an ammonium nitrate propellant composition, these materials are not always included within the first embodiment of the invention when used for gas producing applications, rather they may be optionally included therein. In the gas producing applications, the nitroplasticizer and/or energetic additive may be present (i.e., as an optional additive) in an amount of up to about 35%. Conversely, it is desirable to use nitroplasticizers and/or energetic additives in the propulsive applications of the first embodiment wherein increased energy output is paramount. In the propulsive munitions applications, the nitroplasticizer and/or energetic additive is typically present in an amount from about 5% to about 40% or any value therebetween. The amounts of the binder plus any nitroplasticizer and energetic additive must total at least about 20% to form a physically acceptable first embodiment and, preferably, from about 20% to about 35%. As used herein "physically acceptable" means a composition that can be formed into various desirable shapes, (e.g., grains, etc.) and which can be maintained in those shapes. When a nitroplasticizer which is a nitrate ester is included in the first embodiment, it is preferred that a nitrate ester stabilizer be added as well. When a nitroplasticizer is not used or when an energetic additive (e.g., a nitramine such as RDX, HMX or mixtures thereof), without a nitroplasticizer, is included in the propellant composition, the nitrate ester stabilizer may be omitted from the propellant composition. Thus, in the first embodiment according to the present invention, the nitrate ester stabilizer may be present in an amount of up to about 3%, more preferably, from about 0.1% to about 2% and, most preferably, from about 0.35% to about 0.5%. Nitrate ester stabilizers compatible with the first embodiment of the present invention include, but are not limited to, N-methyl- 4-nitroaniline (MNA) , 2-nitrodiphenylamine (NDA) , ethyl centralite (EC) or mixtures thereof. The preferred nitrate ester stabilizer is a mixture of MNA and NDA, preferably, in a weight ratio of about 1:1.
Curing agents compatible with the first embodiment of the present invention include, but are not limited to, hexamethylene diisocyanate (HMDI) , isophorone diisocyanate (IPDI) , toluene diisocyanate (TDI) , trimethylxylene diisocyanate (TMDI) , dimeryl diisocyanate (DDI) , diphenylmethane diisocyanate (MDI) , naphthalene diisocyanate (NDI) , dianisidine diisocyanate (DADI) , phenylene diisocyanate (PDI) , xylylene diisocyanate (MXDI) , other diisocyanates, triisocyanates, higher isocyanates than the triisocyanates, polyfunctional isocyanates (e.g., Desmodur N 100) , other polyfunctional isocyanates or mixtures thereof. It is preferred that the isocyanate have at least two reactive isocyanate groups. If there are no binder ingredients with a functionality that is greater than 2, then the curative functionality (e.g., number of reactive isocyanate groups per molecule of isocyanate curing agent) must be greater than 2.0. The amount of the curing agent is determined by the desired stoichiometry (i.e., stoichiometry between curable binder and curing agent) . The curing agent is present in an amount of up to about 5%. However, if a curable binder (e.g., binder having reactive hydroxy1 groups such as HTPB) is used, the curing agent is present from about 0.5% to about 5%.
When a curing agent is used, a cure catalyst is preferably added to the propellant composition. The cure catalyst is used to accelerate the curing reaction between the curable binder and the curing agent. Cure catalysts compatible with the first embodiment of the present invention include, but are not limited to, a tin dilaurate (e.g., an alkyl tin dilaurate, butyl tin dilaurate, isopropyl tin dilaurate etc.), metal acetylacetonate, triphenyl bismuth, maleic anhydride, magnesium oxide or mixtures thereof. A preferred cure catalyst is an equal % by weight mixture (i.e., 33 1/3%) of each of triphenyl bismuth, maleic anhydride and magnesium oxide. The cure catalyst is present up to about 0.3% by weight. Further, one opacifier which is compatible with the first embodiment is carbon black. The opacifier is present up to about 2%. Those skilled in the art are aware of other opacifiers that may be used.
Antioxidants may also be added to the first embodiment of the present invention. Antioxidants compatible with the first embodiment of the present invention include, but are not limited to, 2, 2 '-bis (4-methyl-6-tert- butylphenol) , 4,4 '-bis (4-methyl-6-tert-butylphenol) or mixtures thereof. Other antioxidants well known in the art are within the scope of the present invention. The antioxidant is present in an amount of up to about 1%.
Turning now to an alternate embodiment (i.e., the second embodiment, also referred to as the strengthened embodiment) of the invention, the propellant composition comprises ammonium nitrate, a strengthening agent and a binder. The ammonium nitrate component included in this embodiment is the same as that previously described with respect to the first embodiment.
Preferred strengthening agents compatible with the second embodiment of the present invention include, but are not limited to, azodicarbonamide, dicyandiamide, oxamide or mixtures thereof. The most preferred strengthening agent is azidocarbonamide. In the second embodiment of the present propellant composition, the strengthening agent is present in an amount from about 2% to about 20%. Preferably, the strengthening agent is present from about 3% to about 12% and, most preferably, from about 8% to about 12%. Optional additives compatible with the second embodiment include, but are not limited to, a curing agent, a cure accelerator, a nitroplasticizer, an energetic additive, a nitrate ester stabilizer, an opacifier, and/or an antioxidant. The binders, nitroplasticizers, energetic additives, nitrate ester stabilizers, curing agents, cure catalysts, opacifiers and/or anti-oxidants compatible with the first embodiment are equally compatible with the second embodiment. Further, the amounts of ammonium nitrate, nitroplasticizer, energetic additive, nitrate ester stabilizer, curing agent, cure catalyst, opacifier and/or anti-oxidant described with respect to the first embodiment are equally applicable to the second embodiment.
The binder included in the second embodiment is present in an amount from about 3% to about 40% or any value therebetween. The binder is preferably present in the subject embodiment in an amount from about 3% to about 20%. Further, in the second embodiment, the binder plus any nitroplasticizer and energetic additive must total at least about 20% to form a physically acceptable second embodiment and, preferably, from about 20% to about 35%. It should be noted that the second embodiment does not contain a molecular sieve.
The addition of a strengthening agent to a propellant composition reduces its impulse. To compensate for the loss of impulse, nitroplasticizers and/or energetic additives are added. Typically, ammonium nitrate propellant compositions lose their detonatable characteristic when the impulse is less than or equal to about 229 lb.force- seconds/lb.masΞ. However, if a sufficient amount of one or more nitroplasticizers and/or energetic additives is added to an ammonium nitrate propellant composition containing a strengthening agent, then the advantages of the strengthening agent are obtained without loss of impulse. The effect of adding a strengthening agent to the following ammonium nitrate propellant compositions (Table I) yielded the results (Table II) indicated below: Table I
Figure imgf000022_0001
As previously noted, unless indicated otherwise, all components are indicated as a percent by weight of the total weight of the propellant composition. Further, all components of the propellant composition add to a total of 100% by weight.
Table II
10 to
15
Figure imgf000023_0001
20
25
As shown in Table II, as the percentage of strengthening agent is increased to 15%, both the maximum stress and percent elongation are increased from the control values. Increased maximum stress and percent elongation indicate a tougher propellant composition more resistant to premature deflagration or explosion from unplanned stimuli such as impact with multiple fragments, e.g., bullets and the like. The maximum stress and elongation measurements were made according to test procedures described in Chemical Propulsion Information Agency (CPIA) Publication 21, Section 4.3.2 (Supplement) using a class C specimen. CPIA Publication 21 is incorporated herein by reference in its entirety.
Now referring to the third embodiment of the invention, (i.e., an age-stabilized/strengthened propellant composition) , this embodiment comprises ammonium nitrate, a molecular sieve, a strengthening agent and a binder. The same ammonium nitrates, molecular sieves, strengthening agents, binders, nitroplasticizers, energetic additives, nitrate ester stabilizers, curing agents, cure catalysts, opacifiers and/or anti-oxidants compatible with the first and/or second embodiments are equally compatible with the third embodiment. Further, unless indicated otherwise below, the amounts of ammonium nitrate, nitroplasticizer, energetic additive, nitrate ester stabilizer, curing agent, cure catalyst, opacifier and/or anti-oxidant described with respect to the first and/or second embodiments are equally applicable to the third embodiment. It should be noted that the third embodiment contains both a molecular sieve and a strengthening agent in accordance with the first and second embodiments, respectively. The amounts of strengthening agent added to the second embodiment are equally applicable to this third embodiment. Likewise, the amounts of the molecular sieve added to the first embodiment are equally applicable to the third embodiment. Lastly, in the third embodiment, the binder is present in an amount from about 5% to about 30%. The binder plus any nitroplasticizer and energetic additive must total at least about 20% to form a physically acceptable third embodiment and, preferably, from about 20% to about 35%.
Hereinafter, methods for forming the various embodiments of the composition of the present invention are described in detail. Initial drying of all components is accomplished according to typical industry practices, which are well known in the art. For example, the ammonium nitrate is dried (e.g., in an oven) at approximately 110°C for about 16 hours to remove surface water. Appropriate initial drying methods for all the propellant components are well known to those skilled in the art. As previously indicated herein and as indicated immediately below, for embodiments containing a molecular sieve (e.g., the first and third embodiments), significant additional drying is accomplished with the molecular sieve.
Before the other components of the propellant composition are added, at least a portion of the molecular sieve to be ultimately added is mixed with the ammonium nitrate. For example, after initial drying, the molecular sieve is added to the extent of at least about 1 gram per pound of ammonium nitrate. Then the mixture of the ammonium nitrate and the molecular sieve may be allowed to stand for a first aging period. The first aging period is up to about 48 hours or longer, preferably, from about 0.25 hour to about 16 hours and, most preferably, as close to zero as possible.
If the mixture of the molecular sieve and the ammonium nitrate is exposed to the ambient air (i.e., including the moisture therein) , it is preferably ground immediately after mixing (i.e., the first aging period is zero minutes or nearly so) . If, however, the mixture is held in a sealed container (i.e., with limited exposure to ambient air and the moisture therein) , then the mixture may be maintained indefinitely without grinding. For example, the first aging period may be up to about 48 hours (or more) such as from about 4 to about 16 hours. However, it is preferred to grind the mixture immediately (or, for example, as soon as it is practical to do so on a production or assembly line) after mixing to yield a first mixture. Though not bound by theory, it is believed that grinding (the mixture) allows the molecular sieve to be in closer physical proximity to the ammonium nitrate and the water associated with it. Thereby, it is further believed that grinding allows the molecular sieve to more effectively and efficiently absorb (and retain) water away from the ground ammonium nitrate.
Grinding is accomplished by ball milling, fluid energy milling or micropulverizing. Other grinding methods well known in the art may also be used. Further, so long as it is compatible as feed stock for the particular grinding method to be used, the particle characteristics (e.g., particle thickness, particle size, particulate for —grains, prills, crystals size etc.) of the ammonium nitrate are not critical. The size of the ammonium nitrate should be, as previously noted, from about 5 microns to about 400 microns, preferably, from about 30 microns to about 50 microns in thickness. After both grinding then aging (or just grinding if first aging period = zero hours) , the remaining components of the propellant composition (except for any curing agent) are added to the first mixture to yield a second mixture. Thereafter, the second mixture is allowed to stand for a second aging period.
The second aging period allows the molecular sieve to absorb (and retain) a sufficient amount of the water present to age-stabilize the second mixture. The second aging period is up to about 48 hours or longer, preferably, from about 0.25 hour to about 24 hours and, most preferably, from about 16 to about 24 hours. Lastly, the curing agent, if any, (e.g., isocyanate curing agent) is optionally added to the second mixture to complete and form the final age- stabilized ammonium nitrate propellant composition or the final age-stabilized/strengthened propellant composition.
The propellant composition of Example 8, infra , was prepared wherein the first aging period was set to zero hours and the second aging period was set to zero, 2 hours and 48 hours, respectively. The effect of varying the second aging period on hardness (Shore A) , ultimate tensile strength (psi) and elongation at break (%) for the propellant composition of Example 8, infra , is given in Table III below.
Table III
Figure imgf000027_0001
Elongation is an indication of elasticity. It indicates the length through which the propellant composition can be stretched before it breaks. An increase in tensile strength with a concurrent increase in elongation indicates an increase in "toughness" . The increase in "toughness" indicates that less damage will occur in bullet or fragment impact scenarios. Less damage means less surface area to burn and therefore the reaction to unplanned stimuli (e.g., bullet or fragment impact) will be less violent. The aging periods significantly increase the shelf-life (e.g., to 20 years or more) of the ammonium nitrate propellant composition.
For those propellant compositions not containing a molecular sieve, but including a strengthening agent (e.g., the second embodiment) , the ammonium nitrate is ground by ball milling, fluid energy milling or micropulverizing. Other grinding methods well known in the art may also be used. Thereafter, the ground ammonium nitrate is mixed with the remainder of the other components of the propellant composition, including the strengthening agent. As noted, an increase in the elasticity and the maximum stress of a propellant composition indicates that the propellant composition is less prone to cracking, etc. , and less prone to violent deflagration or premature explosion. Having described the invention, the following examples are provided to illustrate specific applications thereof, including the best mode now known to perform the invention. These specific examples are not intended to limit the scope of the invention described herein.
EXAMPLES The following propellant compositions were prepared using the components in the quantities indicated below. However, where indicated the examples are prophetic. It should be noted that in all the prophetic examples, a nitrate ester plasticizer and a cure catalyst are included where appropriate as previously explained. Further, all components in each formulation add up to a total of 100% by weight. Prophetic examples 9, 10, 11 and 12 indicate age-stabilized and mildly strengthened propellant compositions with a slight loss in propellant composition impulse. Prophetic examples 13, 14, 15 and 16 indicate age-stabilized and moderately strengthened propellant compositions with a moderate loss in propellant composition impulse. Prophetic examples 17, 18, 19 and 20 indicate age-stabilized and strongly strengthened propellant compositions with a significant loss in propellant composition impulse. Other minor components that may be included in all prophetic examples include opacifiers, nitrate ester stabilizers, anti-oxidants and cure catalysts. These minor ingredients enhance age-stabilization, ballistic uniformity, accelerate curing and the like well known in the art. Example 1 (Age-Stabilized) Chemical Component Relative Percentage by Weight
Polyglycol Adipate 6.12 Trimethylolethane Trinitrate 11.00
Triethyleneglycol Dinitrate 11.00
N-Methyl-4-Nitroaniline 0.37
Trifunctional Isocyanate 1.32
Carbon Black 2.00 Ammonium Nitrate 67.97
Molecular Sieve 4A 0.22
Example 2 (Age-Stabilized) Chemical Component Relative percentage by Weight
Dioctyl Adipate 6.60
Carbon Black 2.00
Isophorone Diisocyanate 1.30
Ammonium Nitrate 75.80 Molecular Sieve 4A 0.22
Hydroxyterminated Polybutadiene 14.10
Prophetic Example 3
(Age-Stabilized) Chemical Component Relative percentage by Weight
Dioctyl Adipate 2-6%
Carbon black 0.05-0.4%
Hydroxyterminated Polybutadiene 9-14%
Isophorone Diisocyanate 1-3% Molecular Sieve 3A, 4A, 5A, 13X or mixtures thereof 0.2-0.4!
Ammonium Nitrate 70-85
Prophetic Example 4 (Age-Stabilized)
Chemical Component Relative percentage by weight Dioctyl Adipate 2-6% Carbon Black 0.05-0.4%
Hydroxyterminated Polyether 9-14%
Isophorone Diisocyanate 1-3%
Molecular Sieve 3A, 4A, 5A, 13X or mixtures thereof 0.2-0.4%
Ammonium Nitrate 70-85%
Prophetic Example 5
(Age-Stabilized) Chemical Component Relative percentage by weight
Polyglycol Adipate 5-8%
Nitroplasticizers 20-24%
Trifunctional Isocyanate 1-3%
Carbon Black 0.05-0.4% Molecular Sieve 3A, 4A, 5A, 13X or mixtures thereof 0.2-0.4%
Ammonium Nitrate 65-75%
Prophetic Example 6 (Age-Stabilized)
Chemical Component Relative percentage by weight
Hydroxyterminated Polyether 5-8%
Nitroplasticizers 20-25%
Trifunctional Isocyanate 1-3% Carbon Black 0.05-0.4%
Molecular Sieve 3A, 4A, 5A, 13X or mixtures thereof 0.2-0.4%
Ammonium Nitrate 65-74%
Example 7
(Age-Stabilized & Strengthened) Chemical Component Relative Percentage by Weight
Polyglycol Adipate 6.12
Trimethylolethane Trinitrate 11.00 Carbon Black 2.00
Triethyleneglycol Dinitrate 11.00
N-Methyl-4-Nitroaniline 0.37 Ammonium Nitrate 63.97
Trifunctional Isocyanate 1.32
Molecular Sieve 4A 0.22
Dicyandiamide 4.00 A first mixture was prepared according to Example
21, infra . All components (except the curing agent) in the amounts, as indicated immediately above, were combined in a propellant mixer and mixed for 15 minutes without vacuum. The mixing was then stopped and the mixture held at 140°F for 18 hours with the mix bucket sealed. Then the curing agent was added and then mixed therein under vacuum for 15 minutes. The mixer was then scraped down and the propellant mixed under vacuum for another 15 minutes. This mixture was then pressure cast into a block mold or into motors. The propellant composition was then cured within 48 hours at 140°F.
The addition of 4% dicyandiamide to the above propellant composition more than doubled the tensile strength and also significantly increased the strain capability (i.e., the elongation) thereof.
Example 8 (Age-Stabilized) Chemical Component Relative Percentage By Weight Polyglycol Adipate 6.12
Trimethylolethane Trinitrate 11.00
Carbon Black 2.00
Triethyleneglycol Dinitrate 11.00
N-Methyl-4-Nitroaniline 0.37 Ammonium Nitrate 67.97
Trifunctional Isocyanate 1.32
Molecular Sieve 4A 4.00
Prophetic Example 9 (Age-Stabilized & Mildly Strengthened)
Chemical Component Relative Percentage By Weight
Hydroxyterminated Polyether 5-8% Nitroplasticizers 20-25%
Trifunctional Isocyanate 1-3%
Carbon Black 0.05-0.4%
Molecular Sieve 3A, 4A, 5A, 13X or mixtures thereof 0.2-0.4%
Ammonium Nitrate 68-71%
Azodicarbonamide 3-8%
Prophetic Example 10 (Age-Stabilized & Mildly Strengthened)
Chemical Component Relative Percentage By Weight
Polyglycol Adipate 5-8%
Nitroplasticizers 20-24%
Trifunctional Isocyanate 1-3% Carbon Black 0.05-0.4%
Molecular Sieve 3A, 4A, 5A, 13X or mixtures thereof 0.2-0.4%
Ammonium Nitrate 68-71%
Dicyandiamide 3-8%
Prophetic Example 11
(Age-Stabilized & Mildly Strengthened)
Chemical Component Relative Percentage By Weight
Hydroxyterminated Polyether 5-8% Nitroplasticizers 20-25%
Trifunctional Isocyanate 1-3%
Carbon Black 0.05-0.4%
Molecular Sieve 3A, 4A, 5A, 13X or mixtures thereof 0.2-0.4% Ammonium Nitrate 68-71%
Azodicarbonamide 3-8%
Prophetic Example 12 (Age-Stabilized & Mildly Strengthened) Chemical Component Relative Percentage By Weight
Polyglycol Adipate 5-8%
Nitroplasticizers 20-25% Trifunctional Isocyanate 1-3%
Carbon Black 0 . 05-0 . 4%
Molecular Sieve 3A, 4A, 5A, 13X or mixtures thereof 0 . 2-0 . 4% Ammonium Nitrate 68 -71% Azodicarbonamide 3 -8%
Prophetic Example 13
(Age-Stabilized & Moderately Strengthened) Chemical Component Relative Percentage By Weight
Hydroxyterminated Polyether 5-8%
Nitroplasticizers 20-25%
Trifunctional Isocyanate 1-3%
Carbon Black 0.05-0.4% Molecular Sieve 3A, 4A, 5A, 13X or mixtures thereof 0.2-0.4%
Ammonium Nitrate 65-70%
Azodicarbonamide 8-12%
Prophetic Example 14
(Age-Stabilized & Moderately Strengthened)
Chemical Component Relative Percentage By Weight
Polyglycol Adipate 5-8%
Nitroplasticizers 20-25% Trifunctional Isocyanate 1-3%
Carbon Black 0.05-0.4%
Molecular Sieve 3A, 4A, 5A, 13X or mixtures thereof 0.2-0.4%
Ammonium Nitrate 65-70% Dicyandiamide 8-12%
Prophetic Example 15 (Age-Stabilized & Moderately Strengthened) Chemical Component Relative Percentage By Weight Hydroxyterminated Polyether 5-8%
Nitroplasticizers 20-25%
Trifunctional Isocyanate 1-3% Carbon Black 0.05-0.4%
Molecular Sieve 3A, 4A, 5A, 13X or mixtures thereof 0.2-0.4%
Ammonium Nitrate 65-70% Dicyandiamide 8-12%
Prophetic Example 16
(Age-Stabilized & Moderately Strengthened)
Chemical Component Relative Percentage By Weight Polyglycol Adipate 5-8%
Nitroplasticizers 20-25%
Trifunctional Isocyanate 1-3%
Carbon Black 0.05-0.4%
Molecular Sieve 3A, 4A, 5A, 13X or mixtures thereof 0.2-0.4'
Ammonium Nitrate 65-70%
Azodicarbonamide 8-12%
Prophetic Example 17 (Age-Stabilized & Strongly Strengthened)
Chemical Component Relative Percentage By Weight
Hydroxyterminated Polyether 5-8%
Nitroplasticizers 20-25%
Trifunctional Isocyanate 1-3% Carbon Black 0.05-0.4%
Molecular Sieve 3A, 4A, 5A, 13X or mixtures thereof 0.2-0.4%
Ammonium Nitrate 54-65%
Azodicarbonamide 12-16%
Prophetic Example 18
(Age-Stabilized & Strongly Strengthened)
Chemical Component Relative Percentage By Weight
Polyglycol Adipate 5-8% Nitroplasticizers 20-25%
Trifunctional Isocyanate 1-3%
Carbon Black 0.05-0.4% Molecular Sieve 3A, 4A, 5A, 13X or mixtures thereof 0.2-0.4%
Ammonium Nitrate 54-65%
Dicyandiamide 12-16%
Prophetic Example 19
(Age-Stabilized & Strongly Strengthened)
Chemical Component Relative Percentage By Weight
Hydroxyterminated Polyether 5-8% Nitroplasticizers 20-25%
Trifunctional Isocyanate 1-3%
Carbon Black 0.05-0.4%
Molecular Sieve 3A, 4A, 5A, 13X or mixtures thereof 0.2-0.4% Ammonium Nitrate 54-65%
Dicyandiamide 12-16%
Prophetic Example 20
(Age-Stabilized & Strongly Strengthened) Chemical Component Relative Percentage By Weight
Polyglycol Adipate 5-8%
Nitroplasticizers 20-25%
Trifunctional Isocyanate 1-3%
Carbon Black 0.05-0.4% Molecular Sieve 3A, 4A, 5A, 13X or mixtures thereof 0.2-0.4%
Ammonium Nitrate 54-65%
Azodicarbonamide 12-16%
Example 21
(First mixture) One pound of ammonium nitrate (AN) was dried at 230 °F for 16 hours. One gram of 3A molecular sieve was added and the mixture ground in a ball mill for 10 minutes. This produced a first mixture of AN with an average particle size of about 50 microns. The first mixture is best used immediately, but can be stored in a sealed container for at least about one year.
Example 22 (Composition 7019-A with no age-stabilization)
Cellulose acetate (4.0 grams) was dissolved in 25 ml of acetone. AN was ground according to Example 21 without molecular sieve being added. Ground AN (60 grams) and RDX (36 grams) were dry blended by tumbling in a mix bucket. The mixed dry material was then added to the cellulose acetate/acetone solution and hand stirred. Acetone was added as necessary to form a thick paste. The paste was then formed into sheets or extruded into strands or made into granules by screening while still damp. In the preferred form, 7019-A was formed into sheets about 0.030 inches thick, then dried in a vacuum oven at 140°F. The sheets were then broken into smaller pieces and then screened through a 5 mesh screen.
Example 23
(Composition 7019-A with age-stabilization) The procedure followed was the same as Example 22 except that the AN was ground with molecular sieve according to Example 21.
Example 24 (Strengthened Propellant Composition) The same procedure as in Example 7 was followed except that the molecular sieve was omitted from the composition. The amount of binder was increased by 0.22% by weight. Otherwise the procedure followed was identical to Example 7.
Example 25 (Age Stabilized Composition)
The same procedure as in Example 7 was followed except that the strengthening agent was omitted from the composition. The amount of binder was increased by 4.0% by weight. Otherwise the procedure followed was identical to Example 7.
Prophetic Example 26 (Hi-Temp/AN composition with age-stabilization)
Mix Hi-Temp® (100 grams) and a first mixture (100 grams—made according to Example 21) by tumbling in a mixing bucket. Then add just enough acetone to wet the particles and cause the ingredients to stick together. Dry the mixture at 140°F under vacuum. Screen through a 5 mesh screen and store sealed in a sealed container.

Claims

CLAIMS What is claimed is:
1. An age-stabilized ammonium nitrate propellant composition comprising ammonium nitrate, a molecular sieve having pores and a binder, wherein said pores are of a size sufficient to absorb and retain a sufficient amount of water from said ammonium nitrate to provide to said composition a shelf-life of at least about 5 years and wherein said composition is substantially smoke free upon combustion.
2. The composition of claim 1 wherein said molecular sieve is present in an amount up to about 6% by weight of a total weight of said composition, wherein said binder is present in an amount from about 3% to about 40% of said total weight, wherein said molecular sieve has a pore size of about 13 angstroms or less and wherein said ammonium nitrate is present in an amount from about 40% to about 85% by weight of said total weight.
3. The composition of claim 2 wherein said pore size is from about 3 angstroms to about 13 angstroms and said binder is selected from the group consisting of a thermoplastic elastomer, a cure hardening material and mixtures thereof.
4. The composition of claim 1 wherein said molecular sieve is a type A zeolite.
5. The composition of claim 3 further comprising a strengthening agent in an amount up to about 20% of said total weight.
6. The composition of claim 5 wherein said strengthening agent is selected from the group consisting of azodicarbonamide, dicyandiamide, oxamide and mixtures thereof.
7. The composition of claim 6 further comprising a material selected from the group consisting of a nitroplasticizer, an energetic additive and mixtures thereof, wherein said nitroplasticizer is selected from the group consisting of a nitrate ester, a nitramine and mixtures thereof, wherein said material is present in an amount up to about 35% by weight of said total weight and wherein the sum of said nitroplasticizer, said energetic additive and said binder is at least about 20% of said total weight.
8. The composition of claim 7 wherein said energetic additive is a nitramine selected from the group consisting of cyclotetra ethylene tetranitramine, cyclotrimethylene trinitramine, dinitroxydiethylnitramine and mixtures thereof.
9. The composition of claim 8 wherein said nitroplasticizer is said nitrate ester and said composition further comprises a nitrate ester stabilizer in an amount from about 0.1% to about 2% of said total weight.
10. The composition of claim 9 wherein said nitrate ester is selected from the group consisting of trimethylol ethane trinitrate, triethylene glycol dinitrate, triethylene glycol trinitrate, butanetriol trinitrate, diethyleneglycol dinitrate, ethyleneglycol dinitrate, nitroglycerine, diethylene glycerin trinitrate, dinitroglycerine, nitrobenzene, N-buty1-2-nitratoethylnitramine, meth l-2- nitratoethylnitramine, ethy1-2-nitratoethylnitramine and mixtures thereof.
11. The composition of claim 10 wherein said nitrate ester stabilizer is selected from the group consisting of N-methyl- 4-nitroaniline, 2-nitrodiphenylamine, ethyl centralite and mixtures thereof.
12. The composition of claim 11 further comprising a curing agent present in an amount from about 0.5 to about 5% and wherein said binder is a cure hardening material.
5 13. The composition of claim 12 wherein said cure hardening material is selected from the group consisting of a hydroxy terminated polybutadiene, hydroxy terminated polyether, polyglycol adipate, glycidylazide polymer, poly bis-3,3'- azidomethyl oxetane, poly-3-nitratomethy1-3-methyl oxetane,
10 polyethylene glycol, polypropylene glycol, cellulose acetate and mixtures thereof and wherein said curing agent is selected from the group consisting of hexamethylene diisocyanate, isophorone diisocyanate, toluene diisocyanate, trimethylxylene diisocyanate, dimeryl diisocyanate,
15 diphenylmethane diisocyanate, naphthalene diisocyanate, dianisidine diisocyanate, phenylene diisocyanate, xylylene diisocyanate, other diisocyanates, triisocyanates, higher isocyanates than the triisocyanates, polyfunctional isocyanates and mixtures thereof.
20
14. The composition of claim 13 further comprising a cure catalyst in an amount of up to about 0.3% of said total weight.
25 15. The composition of claim 14 wherein said cure catalyst is selected from the group consisting of triphenyl bismuth, maleic anhydride, magnesium oxide, a tin dilaurate, metal acetylacetonate and mixtures thereof.
30 16. The composition of claim 15 further comprising an opacifier in an amount of up to about 2% of said total weight.
17. The composition of claim 16 wherein said opacifier is 35 carbon black.
18. The composition of claim 17 further comprising an antioxidant in an amount of up to about 1% of said total weight and wherein said antioxidant is selected from the group consisting of 2,2'-bis (4-methyl-6-tert-butylphenol) ,
5 4, 4 '-bis (4-methyl-6-tert-butylphenol) and mixtures thereof.
19. An age-stabilized ammonium nitrate propellant composition comprising ammonium nitrate from about 40% to about 85%, a molecular sieve having a pore size from about 3
10 angstroms to about 13 angstroms in an amount from about 0.2% to about 0.4%, a binder from about 3% to about 40% based on a total weight of said composition and wherein said composition is substantially smoke free upon combustion.
15 20. The composition of claim 19 further comprising at least one of a nitroplasticizer up to about 25%, an energetic additive up to about 25%, a nitrate ester stabilizer up to about 3%, a curing agent up to about 3%, a cure catalyst up to about 0.3%, an opacifier up to about 2% and an anti-
20 oxidant up to about 1% based on said total weight.
21. The composition of claim 20 wherein said molecular sieve has a formula Na12 ( (A102) 12 (Si02) 12) 27H20, said binder is a hydroxyterminated polytbutadiene, said nitrate ester
25 stabilizer is N-methyl-4-nitroaniline, said curing agent is isophorone diisocyanate, said cure catalyst is selected from the group consisting of triphenyl bismuth, maleic anhydride, magnesium oxide, a tin dilaurate, metal acetylacetonate and mixtures thereof, said opacifier is carbon black, said anti-
30 oxidant is selected from the group consisting of 2, 2 '-bis (4- methyl-6-tert-butylphenol) , 4,4'-bis (4-methyl-6-tert-butyl phenol) and mixtures thereof and said energetic additive is selected from the group consisting of dinitroxydiethylnitramine, cyclotrimethylene trinitramine,
35 cyclotetramethylene tetranitramine and mixtures thereof.
22. A process of forming an age-stabilized propellant composition, said process comprising the steps of:
(a) providing a quantity of ammonium nitrate;
(b) mixing a molecular sieve having pores with said 5 ammonium nitrate to form a mixture;
(c) allowing said mixture to stand for a first aging period;
(d) thereafter, grinding said mixture to yield a first mixture; and
10 (e) thereafter, adding at least a binder to said first mixture to form a second mixture, said binder being added in a sufficient amount to permit formation of said second mixture into a desired shape wherein said composition is substantially smoke free upon
15 combustion.
23. The process of claim 22 wherein said first aging period has a duration of up to about 48 hours.
20 24. The process of claim 22 wherein said mixing step further comprises adding said molecular sieve having a pore size of between about 3 angstroms to about 13 angstroms, wherein said molecular sieve is present in an amount up to about 6% of a total weight of said propellant composition and wherein said
25 ammonium nitrate is present from about 40% to about 85% of said total weight.
25. The process of claim 24 wherein said adding step further comprises adding to said first mixture in addition to said 30 binder at least one of a material selected from the group consisting of strengthening agents, nitroplasticizers, energetic additives, nitrate ester stabilizers, opacifiers, cure catalysts and antioxidants to yield said second mixture.
35 26. The process of claim 25 further comprising the steps of: (a) allowing said second mixture to stand for a second aging period up to about 48 hours; and (b) thereafter, adding a curing agent to said second mixture.
27. A strengthened ammonium nitrate propellant composition 5 comprising ammonium nitrate, a strengthening agent and a binder.
28. The composition of claim 26 wherein said strengthening agent is selected from the group consisting of
10 azodicarbonamide, dicyandiamide, oxamide and mixtures thereof, wherein said strengthening agent is present in an amount from about 2% to about 20% by weight of a total weight of said composition, wherein said ammonium nitrate is present in an amount from about 40% to about 85% by weight of said
15 total weight and wherein said binder is present in an amount from about 3% to about 40% by weight of said total weight.
29. The composition of claim 28 wherein said binder is selected from the group consisting of a thermoplastic
20 elastomer, a cure hardening material and mixtures thereof.
30. The composition of claim 29 further comprising a molecular sieve in an amount up to about 6% of said total weight and wherein said molecular sieve has a pore size of
25 between about 3 angstroms to about 13 angstroms.
31. The composition of claim 30 wherein said molecular sieve is a type A zeolite.
30 32. The composition of claim 31 further comprising at least one of an energetic additive and a nitroplasticizer, said nitroplasticizer selected from the group consisting of a nitrate ester, a nitramine and mixtures thereof, wherein said nitroplasticizer is present in an amount of up to about 35%
35 by weight of said total weight, wherein said energetic additive is present in an amount of up to about 35% of said total weight and wherein a sum of said nitroplasticizer, said energetic additive and said binder is at least about 20% of said total weight.
33. The composition of claim 32 wherein said nitroplasticizer is a nitramine selected from the group consisting of N-buty1-2-nitratoethylnitramine, methyl-2- nitratoethylnitramine, ethy1-2-nitratoethylnitramine and mixtures thereof .
34. The composition of claim 32 wherein said nitroplasticizer is a nitrate ester and wherein said composition further comprises a nitrate ester stabilizer in an amount from about 0.1% to about 2% of said total weight.
35. The composition of claim 34 wherein said nitrate ester is selected from the group consisting of trimethylol ethane trinitrate, triethylene glycol dinitrate, triethylene glycol trinitrate, butanetriol trinitrate, diethyleneglycol dinitrate, ethyleneglycol dinitrate, nitroglycerine, diethylene glycerin trinitrate, dinitroglycerine, nitrobenzene and mixtures thereof.
36. The composition of claim 35 wherein said nitrate ester stabilizer is selected from the group consisting of N-methyl- 4-nitroaniline, 2-nitrodiphenylamine, ethyl centralite and mixtures thereof.
37. The composition of claim 36 further comprising a curing agent present in an amount from about 0.5 to about 5% and wherein said binder is said cure hardening material.
38. The composition of claim 37 wherein said binder is a hydroxyterminated polybutadiene and said curing agent is selected from the group consisting of hexamethylene diisocyanate, isophorone diisocyanate, toluene diisocyanate, trimethylxylene diisocyanate, dimeryl diisocyanate, diphenylmethane diisocyanate, naphthalene diisocyanate, dianisidine diisocyanate, phenylene diisocyanate, xylylene diisocyanate, other diisocyanates, triisocyanates, higher isocyanates than the triisocyanates, polyfunctional isocyanates and mixtures thereof. 5
39. The composition of claim 38 further comprising a cure catalyst in an amount of up to about 0.3% of said total weight.
10 40. The composition of claim 39 wherein said cure catalyst is selected from the group consisting of triphenyl bismuth, maleic anhydride, magnesium oxide, a tin dilaurate, metal acetylacetonate and mixtures thereof.
15 41. The composition of claim 40 further comprising an opacifier, said opacifier being present in an amount of up to about 2% of said total weight.
42. The composition of claim 41 wherein said opacifier is 20 carbon black.
43. The composition of claim 42 further comprising an antioxidant in an amount of up to about 1% of said total weight and wherein said antioxidant is selected from the
25 group consisting of 2,2'-bis (4-methyl-6-tert-butylphenol) , 4,4'-bis(4-methyl-6-tert-butylphenol) and mixtures thereof.
44. A strengthened ammonium nitrate propellant composition comprising ammonium nitrate from about 40% to about 85%, a
30 strengthening agent from about 2% to about 20% and a binder from about 3% to about 40% based on a total weight of said composition.
45. The composition of claim 44 further comprising at least 35 one of up to about 25% of a nitroplasticizer, up to about 25% of an energetic additive, up to about 3% of a nitrate ester stabilizer, up to about 3% of a curing agent, up to about
0.3% of a cure catalyst, up to about 2% of an opacifier, and up to about 1% of an anti-oxidant, wherein said binder is selected from the group consisting of thermoplastic elastomer, a cure hardening material and mixtures thereof, said energetic additive is selected from the group consisting of cyclotrimethylene trinitramine, cyclotetramethylene tetranitramine, dinitroxyethylnitramine and mixtures thereof, said nitroplasticizer is selected from the group consisting of a nitrate ester, a nitramine and mixtures thereof, said nitrate ester stabilizer is N-methyl-4-nitroaniline, said curing agent is isophorone diisocyanate, said cure catalyst is selected from the group consisting of triphenyl bismuth, maleic anhydride, magnesium oxide, a tin dilaurate, metal acetylacetonate and mixtures thereof, said opacifier is carbon black, said anti-oxidant is selected from the group consisting of 2 ,2'-bis (4-methyl-6-tert-butylphenol) , 4,4'- bis (4-methyl-6-tert-butyl phenol) and mixtures thereof and said strengthening agent is selected from the group consisting of azodicarbonamide, dicyandiamide, oxamide and mixtures thereof.
46. A process of forming a strengthened propellant composition, said process comprising the steps of:
(a) providing a quantity of ammonium nitrate; (b) optionally, grinding said ammonium nitrate;
(c) adding a strengthening agent and at least a binder to said ammonium nitrate to form a primary mixture, said binder being added in a sufficient amount to form said primary mixture into a desired shape.
47. The process of claim 46 wherein said composition is substantially smoke free upon combustion.
48. The process of claim 46 wherein said strengthening agent is selected from the group consisting of azodicarbonamide, dicyandiamide, oxamide and mixtures thereof, wherein said strengthening agent is present in an amount of up to about 20% of a total weight of said composition and wherein said ammonium nitrate is present from about 40% to about 85% of said total weight.
5 49. The process of claim 48 wherein said adding step further comprises adding to said primary mixture in addition to said binder and said strengthening agent at least one of a member selected from the group consisting of a molecular sieve, a nitroplasticizer, an energetic additive, a nitrate ester 10 stabilizer, an opacifier, a cure catalyst and an antioxidant to yield a secondary mixture.
50. The process of claim 49 further comprising the step of adding a curing agent to said secondary mixture.
15
51. A strengthened and age-stabilized ammonium nitrate propellant composition comprising ammonium nitrate from about 40% to about 85%, a molecular sieve having a pore size from about 3 angstroms to about 13 angstroms in an amount from
20 about 0.02% to about 6%, a strengthening agent from about 2% to about 20% and a binder from about 3% to about 40% based on a total weight of said composition wherein said composition is substantially smoke free upon combustion.
25 52. The composition of claim 51 further comprising at least one of a nitroplasticizer up to about 25%, an energetic additive up to about 25%, a nitrate ester stabilizer up to about 3%, a curing agent up to about 3%, a cure catalyst up to about 0.3%, an opacifier up to about 2% and an anti-
30 oxidant up to about 1%, wherein said molecular sieve has the formula Na12 ( (A102) 12 (Si02) 12) 27H20, said binder is a thermoplastic elastomer, a cure hardening material or mixtures thereof, said energetic additive is selected from the group consisting of dinitroxydiethylnitramine,
35 cyclotrimethylene trinitramine, cyclotetramethylene tetranitramine and mixtures thereof, said nitroplasticizer is selected from the group consisting of a nitrate ester, a nitramine and mixtures thereof, said nitrate ester stabilizer is n-methyl-4-nitroaniline, said curing agent is isophorone diisocyanate, said cure catalyst is selected from the group consisting of triphenyl bismuth, maleic anhydride, magnesium oxide, a tin dilaurate, metal acetylacetonate and mixtures thereof, said opacifier is carbon black, said anti-oxidant is selected from the group consisting of 2 , 2 '-bis (4-methyl-6- tert-butylphenol) , 4, 4'-bis (4-methyl-6-tert-butyl phenol) and mixtures thereof and said strengthening agent is selected from the group consisting of azodicarbonamide, dicyandiamide, oxamide and mixtures thereof.
53. An age-stabilized ammonium nitrate composition comprising ammonium nitrate and a molecular sieve having a pore size of about 13 angstroms or less, wherein said composition is substantially smoke free upon combustion.
54. The composition of claim 53 wherein said ammonium nitrate and said molecular sieve is pulverized.
PCT/US1996/018874 1996-11-26 1996-11-26 Ammonium nitrate propellants with molecular sieve WO1998023558A1 (en)

Priority Applications (6)

Application Number Priority Date Filing Date Title
EP96946254A EP0946464A4 (en) 1996-11-26 1996-11-26 Ammonium nitrate propellants with molecular sieve
JP52657398A JP2002511829A (en) 1996-11-26 1996-11-26 Ammonium nitrate propellant containing molecular sieve
PCT/US1996/018874 WO1998023558A1 (en) 1996-11-26 1996-11-26 Ammonium nitrate propellants with molecular sieve
KR1019990704638A KR20000057253A (en) 1996-11-26 1996-11-26 Ammonium nitrate propellants with molecular sieve
CA002273335A CA2273335A1 (en) 1996-11-26 1996-11-26 Ammonium nitrate propellants with molecular sieve
NO19992497A NO313324B1 (en) 1996-11-26 1999-05-25 Ammonium nitrate propellant composition

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PCT/US1996/018874 WO1998023558A1 (en) 1996-11-26 1996-11-26 Ammonium nitrate propellants with molecular sieve

Publications (1)

Publication Number Publication Date
WO1998023558A1 true WO1998023558A1 (en) 1998-06-04

Family

ID=22256193

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/US1996/018874 WO1998023558A1 (en) 1996-11-26 1996-11-26 Ammonium nitrate propellants with molecular sieve

Country Status (5)

Country Link
EP (1) EP0946464A4 (en)
JP (1) JP2002511829A (en)
KR (1) KR20000057253A (en)
CA (1) CA2273335A1 (en)
WO (1) WO1998023558A1 (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1191005A2 (en) * 2000-09-22 2002-03-27 Nof Corporation Gas-generating compositions
US6517647B1 (en) 1999-11-23 2003-02-11 Daicel Chemical Industries, Ltd. Gas generating agent composition and gas generator
WO2004009516A1 (en) * 2002-07-24 2004-01-29 Nippon Kayaku Kabushiki Kaisha Waterproof granular explosive composition
KR100569184B1 (en) * 2004-04-02 2006-04-10 국방과학연구소 Solid propellent containing metal deactivator and preparation method thereof
CN105111033A (en) * 2015-08-20 2015-12-02 福建海峡科化股份有限公司 Porous granular ammonium nitrate fuel oil explosive and preparation method thereof
WO2019162575A1 (en) * 2018-02-22 2019-08-29 Jyväskylän Ammattikorkeakoulu Oy Oxidizer agent for a composition generating gas in a protection device of a vehicle, composition for generating gas, and a gas generator for a protection device of a vehicle

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6872265B2 (en) * 2003-01-30 2005-03-29 Autoliv Asp, Inc. Phase-stabilized ammonium nitrate
KR100763439B1 (en) * 2006-12-11 2007-10-04 국방과학연구소 Propellant composition for gas generator using phase stabilized ammonium nitrate and oxamide
KR100849324B1 (en) * 2007-04-16 2008-07-29 염숙행 The auto explosion type aerosol fire extinguisher method
KR101101218B1 (en) * 2008-09-26 2012-01-04 국방과학연구소 Gap/nitramine-based energetic propellant composition having excellent mechanical properties
US10415938B2 (en) 2017-01-16 2019-09-17 Spectre Enterprises, Inc. Propellant

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3715983A (en) * 1969-05-28 1973-02-13 Mobil Oil Corp Explosive fragmentation of porous solids
US5583315A (en) * 1994-01-19 1996-12-10 Universal Propulsion Company, Inc. Ammonium nitrate propellants

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2730814A (en) * 1953-03-25 1956-01-17 Commercial Solvents Corp Process for drying materials of high moisture diffusion resistance
US4158583A (en) * 1977-12-16 1979-06-19 Nasa High performance ammonium nitrate propellant
NO151037C (en) * 1982-09-14 1985-01-30 Norsk Hydro As STABILIZED AMMONIUM NITRATE OR AMMONIUM NITRATE-RICH PRODUCTS AND PROCEDURE FOR THE PRODUCTION OF SUCH PRODUCTS
US5271778A (en) * 1991-12-27 1993-12-21 Hercules Incorporated Chlorine-free solid rocket propellant for space boosters
US5292387A (en) * 1993-01-28 1994-03-08 Thiokol Corporation Phase-stabilized ammonium nitrate and method of making same
CN1078225A (en) * 1993-03-04 1993-11-10 赤峰市农业科学研究所 Zeolite ammonium nitrate compositions
CA2168033C (en) * 1993-08-04 2001-12-11 Donald R. Poole Low residue azide-free gas generant composition

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3715983A (en) * 1969-05-28 1973-02-13 Mobil Oil Corp Explosive fragmentation of porous solids
US5583315A (en) * 1994-01-19 1996-12-10 Universal Propulsion Company, Inc. Ammonium nitrate propellants

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See also references of EP0946464A4 *

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6517647B1 (en) 1999-11-23 2003-02-11 Daicel Chemical Industries, Ltd. Gas generating agent composition and gas generator
EP1191005A2 (en) * 2000-09-22 2002-03-27 Nof Corporation Gas-generating compositions
EP1191005A3 (en) * 2000-09-22 2003-11-26 Nof Corporation Gas-generating compositions
US6811626B2 (en) 2000-09-22 2004-11-02 Nof Corporation Gas-generating compositions
KR100783684B1 (en) * 2000-09-22 2007-12-07 니치유 가부시키가이샤 Gas-generating compositions
WO2004009516A1 (en) * 2002-07-24 2004-01-29 Nippon Kayaku Kabushiki Kaisha Waterproof granular explosive composition
CN100334043C (en) * 2002-07-24 2007-08-29 日本化药株式会社 Waterproof granular explosive composition
KR100569184B1 (en) * 2004-04-02 2006-04-10 국방과학연구소 Solid propellent containing metal deactivator and preparation method thereof
CN105111033A (en) * 2015-08-20 2015-12-02 福建海峡科化股份有限公司 Porous granular ammonium nitrate fuel oil explosive and preparation method thereof
WO2019162575A1 (en) * 2018-02-22 2019-08-29 Jyväskylän Ammattikorkeakoulu Oy Oxidizer agent for a composition generating gas in a protection device of a vehicle, composition for generating gas, and a gas generator for a protection device of a vehicle

Also Published As

Publication number Publication date
EP0946464A1 (en) 1999-10-06
KR20000057253A (en) 2000-09-15
JP2002511829A (en) 2002-04-16
CA2273335A1 (en) 1998-06-04
EP0946464A4 (en) 2000-12-06

Similar Documents

Publication Publication Date Title
US6059906A (en) Methods for preparing age-stabilized propellant compositions
US5348596A (en) Solid propellant with non-crystalline polyether/inert plasticizer binder
JP3370118B2 (en) Stable solid rocket propellant composition
NO894163L (en) ROCKET-propellant.
US6364975B1 (en) Ammonium nitrate propellants
US6805760B1 (en) High energy propellant with reduced pollution
US4216039A (en) Smokeless propellant compositions having polyester or polybutadiene binder system crosslinked with nitrocellulose
EP0946464A1 (en) Ammonium nitrate propellants with molecular sieve
EP0520104A1 (en) Non-self-deflagrating fuel compositions for high regression rate hybrid rocket motor application
US6024810A (en) Castable double base solid rocket propellant containing ballistic modifier pasted in an inert polymer
US4689097A (en) Co-oxidizers in solid crosslinked double base propellants (U)
US3878003A (en) Composite double base propellant with HMX oxidizer
US3732131A (en) Gun propellant containing nitroplasticized nitrocellulose and triaminoguanidine nitrate
US6790299B2 (en) Minimum signature propellant
GB2038796A (en) Multi-base propellants
US3951704A (en) Double-base propellants with combustion modifier
JPH0759694B2 (en) Propellant composition containing binder / filling adhesive
WO1995009824A1 (en) Bamo/ammo propellant formulations
US3943209A (en) High volumetric energy smokeless solid rocket propellant
US4239073A (en) Propellants in caseless ammunition
KR102633762B1 (en) Insensitive smokeless solid propellant composition comprising N-Guanylurea dinitramide
NO313324B1 (en) Ammonium nitrate propellant composition
US4388126A (en) Multi-component propellant charges
US3996080A (en) Ballistic modifiers
JPH0648879A (en) Multi-composition firing chemical

Legal Events

Date Code Title Description
AK Designated states

Kind code of ref document: A1

Designated state(s): CA JP KR NO

AL Designated countries for regional patents

Kind code of ref document: A1

Designated state(s): AT BE CH DE DK ES FI FR GB GR IE IT LU MC NL PT SE

DFPE Request for preliminary examination filed prior to expiration of 19th month from priority date (pct application filed before 20040101)
121 Ep: the epo has been informed by wipo that ep was designated in this application
ENP Entry into the national phase

Ref document number: 2273335

Country of ref document: CA

WWE Wipo information: entry into national phase

Ref document number: 1019997004638

Country of ref document: KR

WWE Wipo information: entry into national phase

Ref document number: 1996946254

Country of ref document: EP

WWP Wipo information: published in national office

Ref document number: 1996946254

Country of ref document: EP

WWP Wipo information: published in national office

Ref document number: 1019997004638

Country of ref document: KR

WWR Wipo information: refused in national office

Ref document number: 1019997004638

Country of ref document: KR