US3031347A - Slow burning solid composite propellant - Google Patents
Slow burning solid composite propellant Download PDFInfo
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- US3031347A US3031347A US209507A US20950751A US3031347A US 3031347 A US3031347 A US 3031347A US 209507 A US209507 A US 209507A US 20950751 A US20950751 A US 20950751A US 3031347 A US3031347 A US 3031347A
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- C—CHEMISTRY; METALLURGY
- C06—EXPLOSIVES; MATCHES
- C06B—EXPLOSIVES OR THERMIC COMPOSITIONS; MANUFACTURE THEREOF; USE OF SINGLE SUBSTANCES AS EXPLOSIVES
- C06B45/00—Compositions or products which are defined by structure or arrangement of component of product
- C06B45/04—Compositions 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
- C06B45/06—Compositions 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
- C06B45/10—Compositions 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
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- the principal object of my. invention is to provide a solid propellant charge capable of burning at an unusu ally slow burning rate.
- a further object is to'produce such a slow burning propellant which burns" in a substantially smokeless man-
- a further related object is to produce such a slow burning and smokeless propellant capable of developing a satisfactory specific impulse preferably above 200 lbs. see/lb. when burned at 1000 psi.
- a solid propellant charge or grain is burned within the chamber to. generate alargevolume of gas under pressure.
- the gas escapesin the form of a high velocity jet through theexhaust nozzle,.producing the reaction force.
- a solid propellant commonly comprises a fuel having mixed with it the oxidizer required. for its combustion.
- Many solid propellant charges heretofore known burn at a higher rate than isoften desired for long burning charges such as are frequently required in motors for jetassisted take-off or for sustaining flight.
- Disadvantages of employing such special techniques are that the resulting intricate structureofthe grain or charge oftenrequires an unduly greatincrease in the weight ofthe chamber; furthermore, the grain so produced is generally structurally weak.
- the burning rate of the propellant can be afiected 'is'the coarseness of the oxidizerparticles.
- the fuel in the propellant should be one which contains reduced oxygen atoms in the molecule; and by the term reduced oxygen, I mean oxygen atoms included in the molecule whichare linked directly only to a carbon or a hydrogen atom.
- reduced oxygen I mean oxygen atoms included in the molecule whichare linked directly only to a carbon or a hydrogen atom.
- the use of a fuel component having reduced oxygen in the molecule decreases the amount of oxidizer which would otherwise have to be added to the fuel to oxidize the carbon and hydrogen atoms to the proper degree.
- a second criterion is that the oxygen in the fuel must be the equivalent of at least one-fifth of the weight of the combined carbon and hydrogen in the fuel.
- a third, and somewhat related requirement is that the oxygen in the propellant charge must be sufiicient to burn all of the carbon in the charge to CO and to convert at least one-third of all the hydrogen in the propellant to water.
- the amount of oxygen cannot be permitted to be substantially less than this critical amount for if less oxygen than this be present there will result carbon in the discharge which would produceundesirable smoke.
- a fourth requirement of the propellant is that no oxidizer should be used in it which forms any solid particles duringcombustion, for such solid particles would form the undesirable smoke. This requirement excludes metallic salts as oxidizers.
- a fifth requirement is that the oxidizers which are used must be limited to the group consisting of cellulose nitrate, nitroguanidine, guanidine nitrate, ammonium nitrate, ammonium perchlorate, and mixtures of any of these; with the added proviso that if ammonium perchlorate be used as the oxidizer, it cannot be allowed to exceed about 60% by Weight of the propellant mixture. Thus, if ammonium perchlorate be selected as the oxidizer, and if more than the 60% oxidizer be desiredfor the propellant, the excess must be made up by one or more of the-other of the five named oxidizers.
- a sixth requirement is that the fuelcomponent of ⁇ the propellant must amount to at least, 15% by weight of the finished propellant itself.
- the fuel component of the propellant should furthermore be a monomer which polymerizes by addition polymerization, that is, polymerization without the formation of any by-products such as water.
- unsaturated monomers useful in the practice of my invention are unsaturated polyesters, comprising the condensation product of an. alcoholand an organic carboxylic acid, lower alkyl alkenoates such as methyl acrylate, methyl methacrylate, n-butyl acrylate, diethylene glycol diacrylate, and butanediol-l,3-diacrylate; lower alkenyl alkenoates such as diallyl maleate, and diallyl fumarate; lower alkenyl alkanoates such as vinyl acetate; lower alkenyl phthalates such as diallyl phthalate; phenyl substituted alkenes such as styrene; as well as other unsaturated compounds, such as diallyl diglycollate and diethylene glycol bis-(allyl carbonate).
- lower alkyl alkenoates such as methyl acrylate, methyl methacrylate, n-butyl acrylate, diethylene glycol diacrylate, and butanediol
- polyesters that may be used in the practice of this invention are the condensation products obtained by reacting a polyhydric alcohol, a saturated dicarboxylic acid and anunsaturated dicarboxylic acid. These resinsihave been described in detail in copending application of Joseph Philipson, Serial No. 200,881, filed December 14,1950, now Patent No. 2,941,976, issued June 21, 1960', and assigned to the same assignee as the present application.
- polyester resins that are suitable for this purpose are as follows:
- resin A A condensation product made by reacting 4 moles of sebacic acid, one mole of maleic anhydride and 5 moles of propylene glycol. This resin will hereafter be referred to as resin A.
- This resin will hereafter he referred to as resin B.
- resin C A condensation product formed by reacting 7 moles of adipic acid, 3 moles of maleic anhydride and 12 moles of diethylene glycol. This resin will be referred to hereafter as resin C.
- resin D A condensation product formed by reacting 1 mole of diethylene glycol, 0.9 mole of adipic acid and 0.1 mole maleic anhydride. This resin will be referred to hereafter as resin D.
- resin E A condensation product formed by reacting 1 mole polypropylene glycol (425 molecular weight), 0.9 mole adipic acid and 0.1 mole maleic anhydride. This resin will be referred to hereafter as resin E.
- This resin will hereafter he referred to as resin F.
- This resin Will hereafter be designated as resin G.
- This resin will hereafter be referred to as resin H.
- resin I A condensation product formed by reacting 8 moles of adipic acid, 2 moles of maleic anhydride and 10.5 moles of diethylene glycol. This resin will hereafter be referred to as resin I.
- This resin will hereafter be referred to as resin K.
- the condensation process by which the above polyesters are formed is briefly as follows: The ingredients comprising the saturated diearboxylic acid, the saturated diol and the unsaturated dicarboxylic acid are mixed together and heated to a temperature of approximately 140 C. until the water formed by the reaction is substantially driven off. This process is carried out in an atmosphere of inert gas such as nitrogen, carbon dioxide, helium, etc. When the water has been substantially removed the reaction product may then be subjected to higher temperatures not exceeding 250 C. The preferred temperature range for the final stage of the condensation is between 200 and 230 C. The condensation is continued until the polyester has reached a desired degree of polymerization as determined either by an acid number or by measuring the viscosity of the polyester. The preferred degree of polymerization of the application described above is between 5 and 100. The resulting product is generally a viscous liquid which when cooled may be stored until it is ready to be copolymerized.
- All of these resins are capable of copolymerizing with a vinyl or diallyl type of compound such as methyl acrylate, methyl methacrylate, styrene, vinyl acetate, diethylene glycol-bis-(allyl carbonate), diallyl maleate, diallyl fumarate, dialyl diglycollate.
- a vinyl or diallyl type of compound such as methyl acrylate, methyl methacrylate, styrene, vinyl acetate, diethylene glycol-bis-(allyl carbonate), diallyl maleate, diallyl fumarate, dialyl diglycollate.
- the oxidizers contemplated by this invention should be capable of burning without the formation of appreciable solid particles, and they should be characterized by a relatively slow rate at which they give up their oxygen.
- oxidizers which meet these requirements are nitrates, perchlorates of non-metallic basic materials, and nitro compounds containing sufficient oxygen, which form no solid oxidation products on combustion.
- ammonium perchlorate is normally regarded as a fairly slow burning oxidizer for most propellant compositions, its use in propellant compositions heretofore compounded resulted in burning rates faster than the maximum burning rate for slow burning propellants according to the present invention, which by definition is 0.15 in./sec. at 1000 p.s.i. chamber pressure. But ammonium perchlorate may be used in limited quantities or it may be mixed with others of the above-listed oxidizers to produce a propellant having the required slow burning rate.
- the amount of ammonium perchlorate to be used in any case should not exceed a maximum of about 60% by weight based on the weight of the propellant. If additional oxidizer is then required it should be one of the slower burning oxidizer substances mentioned above such as ammonium nitrate, guanidine nitrate or nitroguanidine.
- This mixture had a burning rate of .127 in./sec. at
- This mixture had a1burning rate of,.1 34 in./sec. at 1000 psi.
- Methyl methaerylate 5 This mixture had a burning. ratebf .125. in./sec. at
- ResinlA 40 35 n-Butyl acrylate 60
- The. manner in which .the above propellants are formed is by copolymerizing theingredients shown above.
- the soluton is polymerized by the use of heat and/or polym erization catalysts in-a--manner that-is well known in the art.
- The" temperatures; in whichcopolymcrization takes place is' generally inthe rangeubetween C. to 100 C.
- the catalysts which are normally employed are the than 0.15 in./ sec.
- organicperoxides or peresters such as tertiary butyl hydroperoxide, l hydroxycyclohexyl hydroperoxide 1, methyl ethyl ketone peroxide, benzoyl peroxide, cumene hydroperoxide, lauryl peroxide, methyl amyl ketone peroxide, etc.
- organic peresters are t-butyl perbenzoate, di-t-butyl. diperphthalate, etc.
- a catalyst it is generally employed in amounts ranging between 0.5 to 2.0% by weight based on the weight of the substances to be polymerized. The normal amount usually employed is about 1% by weight. Copolymerization is continued until the sample taken from the polymerized batch shows the desired tensile strength.
- the propellants according to my invention are capable of developing-thrust for an extended period of time since the rate at which the oxidizers give oif, their oxygen is relatively slow.
- the incorporation with the above type oxidizers of fuels with reduced oxygen in an amount equal to or greater than one-fifth the Weight of the carbon and the hydrogen atoms in the fuel results in propellants which burn with a linear rate of not more Without the presence of reduced oxygen in the resins the propellant charges containing the above oxidizers possibly would not burn at all, and if they did burn, solid carbon (smoke) would be present in the exhaust gases.
- My.inventionv has made possible a series of propellant charges which are useful where a reasonable amount of thrust is to be applied over an extended period of time, such as, for example, in jet assisted take-0E, sustaining rockets or aircraft devices.
- a solid, slow burning, propellant composition consistingof a, cured intimate mixture of a solid, non-metallic, inorganic oxidizing salt selected from the group consisting of ammonium perchlorate, ammonium nitrate, andmixtures thereof, in an amount of from about 72% tov 45%-by weight of the total propellantw formulation; from about 5% to 22% by Weight of an oxygen rich additive selected from the group consisting of guanidine nitrate,.nitro guanidine, cellulose nitrate, andmixtures thereof; aud from about 23% to, 36% by weight of a polymerized resin fuel comprising the addition polymerization product of monomer selected from the group consisting of unsaturated polyester resins consisting of the.
- condensation product of saturated polyhydroxy alcohol and polybasic carboxylic acid a mixture of phenyl substituted lower alkene and an unsaturated polyester resin consisting of the condensation product of saturated polyhydrox-y alcohol and polybasic carboxylic acid, lowor alkyl esters of lower alkenoic acids, diethylene glycol bis-(allyl carbonate), lower alkenyl esters of lower alkenoic acids, lower alkenyl esters of lower alkanoic acids, lower alkenyl phthalates, diallyl diglycollate, and mixtures thereof, provided that the amount of ammonium perchlorate present in said propellant composition shall in no event exceed 60% by Weight of the total propellant composition.
- a slow burning solid propellant composition comprising a cured intimate mixture of about 40% by weight based. on the weight of the total propellant of ammonium perchlorate 8% by weight based on the Weight of the total propellant of'cellulose nitrate, 20% by weight based on the Weight of the total propellant of ammonium nitrate, 32% by weightbased on the weight-of the total propellant of a polymerized fuel comprising 45%- by weight basedv on the weight of the total fuel of cliethylene glycol bis-(allylcarbonate), 50% by- Weight based on the weight of the total; fuel of methyl acrylate, and 5% by weight based on the weight of the total fuel of methyl methacrylate.
- a slow burningsolidipropellant composition comprising a cured intimate mixture of about35% by weight based on the weight of'the total, propellant of ammonium perchlorate, 10% by weight based onthe weight of. the total propellant of' guanidine nitrate; 10% by Weight based on the weight of the total propellant of ammonium nitrate, 9% by weight based on the weight of the total propellant of cellulose nitrate, and 36% by weight based on the weight of the total propellant of a polymerized fuel comprising 45% by weight based on the weight of the total fuel of diethylene glycol bis-(allyl carbonate), 50% by weight based on the weight of the total fuel of methyl acrylate and by weight based on the weight of the total fuel of methyl methacrylate.
- a slow burning solid propellant composition comprising a cured intimate mixture of about 50% by weight based on the weight of the total propellant of ammonium perchlorate, 7% by weight based on the weight of the total propellant of cellulose nitrate, 15% by weight based on the weight of the total propellant of nitro guanidine, 28% by weight of a polymerized fuel comprising 45% by weight based on the weight of the total fuel of diethylene glycol bis-(allyl carbonate), 50% by weight based on the weight of the total fuel of methyl acrylate, and 5% by weight based on the weight of the total fuel of methyl methacrylate.
- a slow burning solid propellant composition comprising a cured intimate mixture of about 50% by weight based on the weight of the total propellant of ammonium perchlorate, 5% by weight based on the weight of the total propellant of cellulose nitrate, 5% by weight based on the weight of the total propellant of guanidine nitrate, 5% by weight based on the weight of the total propellant of nitro guanidine, and 35% by weight based on the weight of the total propellant of a polymerized fuel comprising 50% by weight based on the weight of the total fuel of methylacrylate, 10% by weight based on the weight of the total fuel of styrene, and 40% by weight based on the weight of the total fuel of a condensation product obtained by reacting 7 moles of adipic acid, 3 moles of maleic anhydride and 12 moles of diethylene glycol.
- a solid, slow burning, propellant composition consisting essentially of a cured intimate mixture of from about 45% to 72%, by weight, of solid non-metallic inorganic oxidizing salt selected from the group consisting of ammonium nitrate, ammonium perchlorate, and mixtures thereof; from about 5% to 22%, by weight, of a mixture of guanidine nitrate and cellulose nitrate; and from about 23 to 36% by weight, of the total propellant composition of the addition polymerization product of a mixture of diethylene glycol bis-(allyl carbonate) and lower alkyl ester of lower alkenoic acid, provided that the ammonium perchlorate present in said propellant composition shall in no event exceed 60% by weight of the total propellant composition.
- a solid, slow burning, propellant composition consisting essentially of a cured intimate mixture of from about 45% to 72%, by weight of a solid non-metallic inorganic oxidizing salt selected from the group consisting of ammonium nitrate, ammonium perchlorate, and mixtures thereof; from about 5% to 22%, by weight, of a mixture of nitro guanidine and cellulose nitrate; and from about 23% to 36%, by weight, of the total propellant composition of the addition polymerization product of a mixture of diethylene glycol bis-(allyl carbonate) and lower alkyl ester of lower alkenoic acid, provided that the ammonium perchlorate present in said propellant composition shall in no event exceed 60% by weight of the total propellant composition.
- a solid, slow burning, propellant composition consisting essentially of a cured intimate mixture of from about 45% to 72%, by weight, of a solid non-metallic inoragnic ovidizing salt selected from the group consisting of ammonium nitrate, ammonium perchlorate, and mixtures thereof; from about 5% to 22%, by weight, of nitro guanidine; and from about 23% to 36%, by weight, of the total propellant composition of an unsaturated polyester resin consisting of the condensation product of saturated polyhydric alcohol and polybasic carboxylic acid heteropolymerized with a mixture of phenyl substituted lower alkene and lower alkyl ester of lower alkenoic acid, provided that the ammonium perchlorate present in said propellant composition shall in no event exceed 60% by weight of the total propellant composition.
- a solid, slow burning, propellant composition consisting essentially of a cured intimate mixture of from about 45% to 72%, by weight, of a solid non-metallic inorganic oxidizing salt selected from the group consisting of ammonium nitrate, ammonium perchlorate, and mixtures thereof; from about 5% to 22%, by weight, of a mixture of cellulose nitrate, guanidine nitrate and nitro guanidine; and from about 23% to 36%, by Weight, of the total propellant composition of an unsaturated polyester resin consisting of the condensation product of saturated polyhydric alcohol and polybasic carboxylic acid heteropolymerized with a mixture of phenyl substituted lower alkene and lower alkyl ester of lower alkenoic acid, provided that the ammonium perchlorate present in said propellant composition shall in no event exceed 60% by weight of the total propellant composition.
- a solid non-metallic inorganic oxidizing salt selected from the group consisting of ammonium nit
- a solid, slow burning, propellant composition consisting essentially of a cured intimate mixture of a solid non-metallic inorganic oxidizing salt selected from the group consisting of ammonium nitrate, ammonium perchlorate, and mixtures thereof in an amount of from about 72% to 45%, by weight; from about 5% to 22%, by weight of nitro guanidine; and from about 23% to 36%, by weight, of the total propellant composition of unsaturated polyester resin consisting of the condensation product of saturated polyhydric alcohol and polybasic carboxylic acid heteropolymerized with lower alkyl ester of lower alkenoic acid, provided that the ammonium perchlorate present in said propellant composition shall in no event exceed 60% by weight of the total propellant composition.
- a solid, slow burning, propellant composition consisting essentially of a cured intimate mixture of a solid non-metallic inorganic oxidizing salt selected from the group consisting of ammonium nitrate, ammonium perchlorate, and mixtures thereof in an amount of from about 72% to 45%, by weight; fro mabout 5% to 22%, by weight, of a mixture of cellulose nitrate, guanidine nitrate and nitro guanidine; and from about 23% to 36%, by weight, of the total propellant composition of unsaturated polyester resin consisting of the condensation product of saturated polyhydric alcohol and polybasic carboxylic acid heteropolymerized with lower alkyl ester of lower alkenoic acid, provided that the ammonium perchlorate present in said propellant composition shall in no event exceed 60% by weight of the total propellant composition.
- a solid non-metallic inorganic oxidizing salt selected from the group consisting of ammonium nitrate, ammonium perchlorate, and
- a solid, slow burning, propellant composition consisting essentially of a cured intimate mixture of from about 45% to 72%, by weight, of solid non-metallic inorganic oxidizing salt selected from the group consisting of ammonium nitrate, ammonium perchlorate, and mixtures thereof; from about 5% to 22%, by weight, of cellulose nitrate; and from about 23% to 36%, by weight, of the total propellant composition of the addition polymerization product of a mixture of diethylene glycol bis-(allyl carbonate) and lower alkyl ester of lower alkenoic acid, provided that the ammonium perchlorate present in said propellant composition shall in no event exceed 60% by weight of the total propellant composition.
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Description
April 24, 1962 J. PHILIPSON 3,031,347-
SLOW BURNING SOLID COMPOSITE PROPELLANT Filed Feb. 5, 1951 BURNING RATE, r, IN/SEC 9 O 8 6 a CHAMBER PRESSURE, Pc, PSIA IN V EN TOR. JOSEPH PHIL IPSO/V Jim Q AT TORNE 3,031,347 SLGW BURNING SOLEDCOMPOSITE PROPELLANT JsephPhilipson,Temple City, ,Calif., assignor, by mesne assignments, to, Aerojet-General Corporation, Cincinnati, Ohio, a corporation of Ohio Filed'Feb. 5, 1951, Ser. No. 209,507 12 Claims. (Cl. 14948) This invention relates to jet propulsion and. more particularly to solid propellant materials useful in rocket or jet propulsion motors.
The principal object of my. invention is to provide a solid propellant charge capable of burning at an unusu ally slow burning rate.
A further object is to'produce such a slow burning propellant which burns" in a substantially smokeless man- A further related object is to produce such a slow burning and smokeless propellant capable of developing a satisfactory specific impulse preferably above 200 lbs. see/lb. when burned at 1000 psi.
In the operation of certain types of rocket motors, a solid propellant charge or grain is burned within the chamber to. generate alargevolume of gas under pressure. The gas escapesin the form of a high velocity jet through theexhaust nozzle,.producing the reaction force.
A solid propellant commonly comprises a fuel having mixed with it the oxidizer required. for its combustion. Many solid propellant charges heretofore known burn at a higher rate than isoften desired for long burning charges such as are frequently required in motors for jetassisted take-off or for sustaining flight. In some cases it might be possible to approximate the performance of such a slow burning charge by use of previously knownpropellants; but this would normally require resort to some special technique such as a substantial lowering of the specific impulse of the propellant-or employing acomplex grain configuration. Disadvantages of employing such special techniques are that the resulting intricate structureofthe grain or charge oftenrequires an unduly greatincrease in the weight ofthe chamber; furthermore, the grain so produced is generally structurally weak.
One factor by which the burning rate of the propellant can be afiected 'is'the coarseness of the oxidizerparticles. The coarser theparticle of oxidizer the slower will be the burning rate. Increasing the coarseness of the oxidizer, however, should not be allowed to interfere with the castability of a cast propellant; and the oxidizer cannot be coarsened to the point where the oxidizer will settle out in the liquid mixture before polymerization has taken place.
A slow burning propellant according to my invention is defined as one havinga burning rate not exceeding 0.15 of an inch'per second at l000 p.s.i. chamber pressure. Furthermore, when the log burning rate is plottedagainst the log chamber pressure-the slope n. of the curve, determined by the equation 1'=CP (in. which;;r=the linear burningrate. in inches/sec. C=a constant P =the chamber pressure in p.s.i.)
shall beequal to or less than 0.5. A typical curve for a satisfactory propellant is shown in the graph.
According to-my invention, I-provide asmokelesspropellant. charge. thatconformstothe above requirementsv by compounding the propellants withfuels, which are capable of supplying a portion of the oxygen required for the oxidation ofthe carbon and hydrogen atoms in the finished propellantcharge;.andasoxidizer, substances that yield their oxygen at arelatively slow rateandfurthermore form no solid oxidation products.
3,h3l,347 Patented Apr. 24, 1962 In accordance with my invention, I provide a solid propellant material which can be made into a solid grain or charge of conventional size and shape, without any unusual configurations, and possessed of good physicalcharr asteristics of strength, consistency and the like.
I have accomplished my invention by the discovery of particular qualities and characteristics of the components of the propellant. One of the requirements which I have discovered is that the fuel in the propellant should be one which contains reduced oxygen atoms in the molecule; and by the term reduced oxygen, I mean oxygen atoms included in the molecule whichare linked directly only to a carbon or a hydrogen atom. The use of a fuel component having reduced oxygen in the molecule decreases the amount of oxidizer which would otherwise have to be added to the fuel to oxidize the carbon and hydrogen atoms to the proper degree.
A second criterion is that the oxygen in the fuel must be the equivalent of at least one-fifth of the weight of the combined carbon and hydrogen in the fuel.
A third, and somewhat related requirement is that the oxygen in the propellant charge must be sufiicient to burn all of the carbon in the charge to CO and to convert at least one-third of all the hydrogen in the propellant to water. The amount of oxygen cannot be permitted to be substantially less than this critical amount for if less oxygen than this be present there will result carbon in the discharge which would produceundesirable smoke.
A fourth requirement of the propellant is that no oxidizer should be used in it which forms any solid particles duringcombustion, for such solid particles would form the undesirable smoke. This requirement excludes metallic salts as oxidizers.
A fifth requirement is that the oxidizers which are used must be limited to the group consisting of cellulose nitrate, nitroguanidine, guanidine nitrate, ammonium nitrate, ammonium perchlorate, and mixtures of any of these; with the added proviso that if ammonium perchlorate be used as the oxidizer, it cannot be allowed to exceed about 60% by Weight of the propellant mixture. Thus, if ammonium perchlorate be selected as the oxidizer, and if more than the 60% oxidizer be desiredfor the propellant, the excess must be made up by one or more of the-other of the five named oxidizers.
A sixth requirement is that the fuelcomponent of{ the propellant must amount to at least, 15% by weight of the finished propellant itself.
The fuel component of the propellant should furthermore be a monomer which polymerizes by addition polymerization, that is, polymerization without the formation of any by-products such as water.
Examples of unsaturated monomers useful in the practice of my invention are unsaturated polyesters, comprising the condensation product of an. alcoholand an organic carboxylic acid, lower alkyl alkenoates such as methyl acrylate, methyl methacrylate, n-butyl acrylate, diethylene glycol diacrylate, and butanediol-l,3-diacrylate; lower alkenyl alkenoates such as diallyl maleate, and diallyl fumarate; lower alkenyl alkanoates such as vinyl acetate; lower alkenyl phthalates such as diallyl phthalate; phenyl substituted alkenes such as styrene; as well as other unsaturated compounds, such as diallyl diglycollate and diethylene glycol bis-(allyl carbonate).
The polyesters that may be used in the practice of this invention are the condensation products obtained by reacting a polyhydric alcohol, a saturated dicarboxylic acid and anunsaturated dicarboxylic acid. These resinsihave been described in detail in copending application of Joseph Philipson, Serial No. 200,881, filed December 14,1950, now Patent No. 2,941,976, issued June 21, 1960', and assigned to the same assignee as the present application.
Some specific examples of large numbers of polyester resins that are suitable for this purpose are as follows:
A condensation product made by reacting 4 moles of sebacic acid, one mole of maleic anhydride and 5 moles of propylene glycol. This resin will hereafter be referred to as resin A.
A condensation product made by reacting 7 moles of adipic acid, 3 moles of maleic anhydride and 11 moles of diethylene glycol or ethylene glycol. This resin will hereafter he referred to as resin B.
A condensation product formed by reacting 7 moles of adipic acid, 3 moles of maleic anhydride and 12 moles of diethylene glycol. This resin will be referred to hereafter as resin C.
A condensation product formed by reacting 1 mole of diethylene glycol, 0.9 mole of adipic acid and 0.1 mole maleic anhydride. This resin will be referred to hereafter as resin D.
A condensation product formed by reacting 1 mole polypropylene glycol (425 molecular weight), 0.9 mole adipic acid and 0.1 mole maleic anhydride. This resin will be referred to hereafter as resin E.
A condensation product formed by reacting 1 mole polypropylene glycol (425 molecular weight), 0.8 mole adipic acid and 0.2 mole maleic anhydride. This resin will hereafter he referred to as resin F.
A condensation product formed by reacting 1 mole polyethylene glycol (300 molecular weight), 0.9 mole adipic acid, and 0.1 mole maleic anhydride. This resin Will hereafter be designated as resin G.
A condensation product formed by reacting 1 mole polyethylene glycol (300 molecular weight), 0.8 mole adipic acid, and 0.2 mole maleic anhydride. This resin will hereafter be referred to as resin H.
A condensation product formed by reacting 8 moles of adipic acid, 2 moles of maleic anhydride and 10.5 moles of diethylene glycol. This resin will hereafter be referred to as resin I.
A condensation product formed by reacting 8 moles of adipic acid, 2 moles maleic anhydride and 12 moles of diethylene glycol. This reaction will hereafter be referred to as resin J.
A condensation product formed by reacting moles of diethylene glycol, 4.5 moles adipic acid, 4.5 moles of azelaic acid and 1 mole maleic anhydride. This resin will hereafter be referred to as resin K.
The condensation process by which the above polyesters are formed is briefly as follows: The ingredients comprising the saturated diearboxylic acid, the saturated diol and the unsaturated dicarboxylic acid are mixed together and heated to a temperature of approximately 140 C. until the water formed by the reaction is substantially driven off. This process is carried out in an atmosphere of inert gas such as nitrogen, carbon dioxide, helium, etc. When the water has been substantially removed the reaction product may then be subjected to higher temperatures not exceeding 250 C. The preferred temperature range for the final stage of the condensation is between 200 and 230 C. The condensation is continued until the polyester has reached a desired degree of polymerization as determined either by an acid number or by measuring the viscosity of the polyester. The preferred degree of polymerization of the application described above is between 5 and 100. The resulting product is generally a viscous liquid which when cooled may be stored until it is ready to be copolymerized.
All of these resins are capable of copolymerizing with a vinyl or diallyl type of compound such as methyl acrylate, methyl methacrylate, styrene, vinyl acetate, diethylene glycol-bis-(allyl carbonate), diallyl maleate, diallyl fumarate, dialyl diglycollate.
The oxidizers contemplated by this invention should be capable of burning without the formation of appreciable solid particles, and they should be characterized by a relatively slow rate at which they give up their oxygen.
Among the oxidizers which meet these requirements are nitrates, perchlorates of non-metallic basic materials, and nitro compounds containing sufficient oxygen, which form no solid oxidation products on combustion.
Examples of this class of substances are cellulose nitrate, guanidine nitrate, nitro guanidine, ammonium nitrate, and amonium perchlorate. While ammonium perchlorate is normally regarded as a fairly slow burning oxidizer for most propellant compositions, its use in propellant compositions heretofore compounded resulted in burning rates faster than the maximum burning rate for slow burning propellants according to the present invention, which by definition is 0.15 in./sec. at 1000 p.s.i. chamber pressure. But ammonium perchlorate may be used in limited quantities or it may be mixed with others of the above-listed oxidizers to produce a propellant having the required slow burning rate. To avoid high burning rates, the amount of ammonium perchlorate to be used in any case should not exceed a maximum of about 60% by weight based on the weight of the propellant. If additional oxidizer is then required it should be one of the slower burning oxidizer substances mentioned above such as ammonium nitrate, guanidine nitrate or nitroguanidine.
The following formulations set forth examples of propellant combinations which fall within the scope of this invention and will burn at the desired rate:
Example 1 Percent by Weight Ammonium perchlorate Cellulose nitrate Ammonium nitrate Fuel:
Diethylene glycol bis-(allyl carbonate). Methyl acrylate Methyl methaerylate to a 0000 This mixture had a burning rate of .115 in./sec. at
1000 p.s.i.
Example 2 Percent by weight Ammonium perchlorate 40 Cellulose nitrate 9 Ammonium nitrate 15 Fuel:
Diethylene glycol bis-(allyl carbonate) 45 Methyl acrylate 50 36 Methyl methacrylate 5 This mixture had a burning rate of .115 in./sec. at
' 1000 p.s.i.
Example 3 Percent by weight Ammonium perchlorate Ammonium nitrate Guanidine nitrate Cellulose nitr Fuel:
Diethylene glycol bis-(allyl carbonate) 45 HHCA? GOOD! Methyl acrylate Methyl methacrylate...
This mixture had a burning rate of .127 in./sec. at
This mixture had a1burning rate of,.1 34 in./sec. at 1000 psi.
Example 6.
Percent by Weight Ammonium perchlorate: 57 Ammonium nitratel5 Cellulose nitrate 5. 5 Fuel:
Diethylene glycol bis-(allyl carbonate). 45
Methyl aerylate 50 t 22. 5
Methyl methaerylate 5 This mixture had a burning. ratebf .125. in./sec. at
1000 p.s.i.
Example 7 Percent by weight Ammonium perchlor te 5Q Nitro mi'miriine 15 Fuel:
Resin 4O Styrene 10 35 Methylacrylate 50 Example 8 Percent by weight Ammonium perchlorate 50 Cellulose nitrate Guanidine nitr 5 Nitm nanidine 5 Fuel:
Rosin G 40 Styrene i 35 Methylacrylate 50 Example 9 Percent by weight Ammonium perchlorate 50 Nitro nanidine Fuelz' Resin A 40 35 n-Butyl acrylate 60 Example 10 0 Percent by weight Ammonium perchlorate 50 C'ellulosenitr 5 Guanidinenitrate. 5 Nine. Qnsmidine 5 Fuel:
ResinlA; 40 35 n-Butyl acrylate 60 The. manner in which .the above propellants are formed is by copolymerizing theingredients shown above. The soluton is polymerized by the use of heat and/or polym erization catalysts in-a--manner that-is well known in the art. The" temperatures; in whichcopolymcrization takes place is' generally inthe rangeubetween C. to 100 C.
The catalysts which are normally employed are the than 0.15 in./ sec.
organicperoxides or peresters such as tertiary butyl hydroperoxide, l hydroxycyclohexyl hydroperoxide 1, methyl ethyl ketone peroxide, benzoyl peroxide, cumene hydroperoxide, lauryl peroxide, methyl amyl ketone peroxide, etc. Examples of the organic peresters are t-butyl perbenzoate, di-t-butyl. diperphthalate, etc. When a catalyst is used it is generally employed in amounts ranging between 0.5 to 2.0% by weight based on the weight of the substances to be polymerized. The normal amount usually employed is about 1% by weight. Copolymerization is continued until the sample taken from the polymerized batch shows the desired tensile strength.
The propellants according to my invention are capable of developing-thrust for an extended period of time since the rate at which the oxidizers give oif, their oxygen is relatively slow. In addition'the incorporation with the above type oxidizers of fuels with reduced oxygen in an amount equal to or greater than one-fifth the Weight of the carbon and the hydrogen atoms in the fuel, results in propellants which burn with a linear rate of not more Without the presence of reduced oxygen in the resins the propellant charges containing the above oxidizers possibly would not burn at all, and if they did burn, solid carbon (smoke) would be present in the exhaust gases.
My.inventionvhas made possible a series of propellant charges which are useful where a reasonable amount of thrust is to be applied over an extended period of time, such as, for example, in jet assisted take-0E, sustaining rockets or aircraft devices.
I claim:
1. A solid, slow burning, propellant composition consistingof a, cured intimate mixture of a solid, non-metallic, inorganic oxidizing salt selected from the group consisting of ammonium perchlorate, ammonium nitrate, andmixtures thereof, in an amount of from about 72% tov 45%-by weight of the total propellantw formulation; from about 5% to 22% by Weight of an oxygen rich additive selected from the group consisting of guanidine nitrate,.nitro guanidine, cellulose nitrate, andmixtures thereof; aud from about 23% to, 36% by weight of a polymerized resin fuel comprising the addition polymerization product of monomer selected from the group consisting of unsaturated polyester resins consisting of the. condensation product of saturated polyhydroxy alcohol and polybasic carboxylic acid, a mixture of phenyl substituted lower alkene and an unsaturated polyester resin consisting of the condensation product of saturated polyhydrox-y alcohol and polybasic carboxylic acid, lowor alkyl esters of lower alkenoic acids, diethylene glycol bis-(allyl carbonate), lower alkenyl esters of lower alkenoic acids, lower alkenyl esters of lower alkanoic acids, lower alkenyl phthalates, diallyl diglycollate, and mixtures thereof, provided that the amount of ammonium perchlorate present in said propellant composition shall in no event exceed 60% by Weight of the total propellant composition.
2. A slow burning solid propellant composition comprising a cured intimate mixture of about 40% by weight based. on the weight of the total propellant of ammonium perchlorate 8% by weight based on the Weight of the total propellant of'cellulose nitrate, 20% by weight based on the Weight of the total propellant of ammonium nitrate, 32% by weightbased on the weight-of the total propellant of a polymerized fuel comprising 45%- by weight basedv on the weight of the total fuel of cliethylene glycol bis-(allylcarbonate), 50% by- Weight based on the weight of the total; fuel of methyl acrylate, and 5% by weight based on the weight of the total fuel of methyl methacrylate.
3. A slow burningsolidipropellant composition comprising a cured intimate mixture of about35% by weight based on the weight of'the total, propellant of ammonium perchlorate, 10% by weight based onthe weight of. the total propellant of' guanidine nitrate; 10% by Weight based on the weight of the total propellant of ammonium nitrate, 9% by weight based on the weight of the total propellant of cellulose nitrate, and 36% by weight based on the weight of the total propellant of a polymerized fuel comprising 45% by weight based on the weight of the total fuel of diethylene glycol bis-(allyl carbonate), 50% by weight based on the weight of the total fuel of methyl acrylate and by weight based on the weight of the total fuel of methyl methacrylate.
4. A slow burning solid propellant composition comprising a cured intimate mixture of about 50% by weight based on the weight of the total propellant of ammonium perchlorate, 7% by weight based on the weight of the total propellant of cellulose nitrate, 15% by weight based on the weight of the total propellant of nitro guanidine, 28% by weight of a polymerized fuel comprising 45% by weight based on the weight of the total fuel of diethylene glycol bis-(allyl carbonate), 50% by weight based on the weight of the total fuel of methyl acrylate, and 5% by weight based on the weight of the total fuel of methyl methacrylate.
5. A slow burning solid propellant composition comprising a cured intimate mixture of about 50% by weight based on the weight of the total propellant of ammonium perchlorate, 5% by weight based on the weight of the total propellant of cellulose nitrate, 5% by weight based on the weight of the total propellant of guanidine nitrate, 5% by weight based on the weight of the total propellant of nitro guanidine, and 35% by weight based on the weight of the total propellant of a polymerized fuel comprising 50% by weight based on the weight of the total fuel of methylacrylate, 10% by weight based on the weight of the total fuel of styrene, and 40% by weight based on the weight of the total fuel of a condensation product obtained by reacting 7 moles of adipic acid, 3 moles of maleic anhydride and 12 moles of diethylene glycol.
6. A solid, slow burning, propellant composition consisting essentially of a cured intimate mixture of from about 45% to 72%, by weight, of solid non-metallic inorganic oxidizing salt selected from the group consisting of ammonium nitrate, ammonium perchlorate, and mixtures thereof; from about 5% to 22%, by weight, of a mixture of guanidine nitrate and cellulose nitrate; and from about 23 to 36% by weight, of the total propellant composition of the addition polymerization product of a mixture of diethylene glycol bis-(allyl carbonate) and lower alkyl ester of lower alkenoic acid, provided that the ammonium perchlorate present in said propellant composition shall in no event exceed 60% by weight of the total propellant composition.
7. A solid, slow burning, propellant composition consisting essentially of a cured intimate mixture of from about 45% to 72%, by weight of a solid non-metallic inorganic oxidizing salt selected from the group consisting of ammonium nitrate, ammonium perchlorate, and mixtures thereof; from about 5% to 22%, by weight, of a mixture of nitro guanidine and cellulose nitrate; and from about 23% to 36%, by weight, of the total propellant composition of the addition polymerization product of a mixture of diethylene glycol bis-(allyl carbonate) and lower alkyl ester of lower alkenoic acid, provided that the ammonium perchlorate present in said propellant composition shall in no event exceed 60% by weight of the total propellant composition.
8. A solid, slow burning, propellant composition consisting essentially of a cured intimate mixture of from about 45% to 72%, by weight, of a solid non-metallic inoragnic ovidizing salt selected from the group consisting of ammonium nitrate, ammonium perchlorate, and mixtures thereof; from about 5% to 22%, by weight, of nitro guanidine; and from about 23% to 36%, by weight, of the total propellant composition of an unsaturated polyester resin consisting of the condensation product of saturated polyhydric alcohol and polybasic carboxylic acid heteropolymerized with a mixture of phenyl substituted lower alkene and lower alkyl ester of lower alkenoic acid, provided that the ammonium perchlorate present in said propellant composition shall in no event exceed 60% by weight of the total propellant composition.
9. A solid, slow burning, propellant composition consisting essentially of a cured intimate mixture of from about 45% to 72%, by weight, of a solid non-metallic inorganic oxidizing salt selected from the group consisting of ammonium nitrate, ammonium perchlorate, and mixtures thereof; from about 5% to 22%, by weight, of a mixture of cellulose nitrate, guanidine nitrate and nitro guanidine; and from about 23% to 36%, by Weight, of the total propellant composition of an unsaturated polyester resin consisting of the condensation product of saturated polyhydric alcohol and polybasic carboxylic acid heteropolymerized with a mixture of phenyl substituted lower alkene and lower alkyl ester of lower alkenoic acid, provided that the ammonium perchlorate present in said propellant composition shall in no event exceed 60% by weight of the total propellant composition.
10. A solid, slow burning, propellant composition consisting essentially of a cured intimate mixture of a solid non-metallic inorganic oxidizing salt selected from the group consisting of ammonium nitrate, ammonium perchlorate, and mixtures thereof in an amount of from about 72% to 45%, by weight; from about 5% to 22%, by weight of nitro guanidine; and from about 23% to 36%, by weight, of the total propellant composition of unsaturated polyester resin consisting of the condensation product of saturated polyhydric alcohol and polybasic carboxylic acid heteropolymerized with lower alkyl ester of lower alkenoic acid, provided that the ammonium perchlorate present in said propellant composition shall in no event exceed 60% by weight of the total propellant composition.
11. A solid, slow burning, propellant composition consisting essentially of a cured intimate mixture of a solid non-metallic inorganic oxidizing salt selected from the group consisting of ammonium nitrate, ammonium perchlorate, and mixtures thereof in an amount of from about 72% to 45%, by weight; fro mabout 5% to 22%, by weight, of a mixture of cellulose nitrate, guanidine nitrate and nitro guanidine; and from about 23% to 36%, by weight, of the total propellant composition of unsaturated polyester resin consisting of the condensation product of saturated polyhydric alcohol and polybasic carboxylic acid heteropolymerized with lower alkyl ester of lower alkenoic acid, provided that the ammonium perchlorate present in said propellant composition shall in no event exceed 60% by weight of the total propellant composition.
12. A solid, slow burning, propellant composition consisting essentially of a cured intimate mixture of from about 45% to 72%, by weight, of solid non-metallic inorganic oxidizing salt selected from the group consisting of ammonium nitrate, ammonium perchlorate, and mixtures thereof; from about 5% to 22%, by weight, of cellulose nitrate; and from about 23% to 36%, by weight, of the total propellant composition of the addition polymerization product of a mixture of diethylene glycol bis-(allyl carbonate) and lower alkyl ester of lower alkenoic acid, provided that the ammonium perchlorate present in said propellant composition shall in no event exceed 60% by weight of the total propellant composition.
References Cited in the file of this patent UNITED STATES PATENTS 2,155,499 Lawson Apr. 25, 1939 2,165,263 Holm July 11, 1939 2,187,866 Spurlin et a1 Jan. 23, 1940 (Other references on following page) 9 UNITED STATES PATENTS Ellis Sept. 9, 1941 Fuller Nov. 6, 1945 Pearsall Feb. 25, 1947 Fuller June 22, .1948 Kropa June 22, 1948 Singleton et a1 June 14, 1949 Carr Aug. 16, 1949 Geckler Aug. 23, 1949 FOREIGN PATENTS Great Britain Mar. 1, 1926 Great Britain July 22, 1946 OTHER REFERENCES McLarren: Rocket Engine Fuels, Automotive and Aviation Industries, Aug. 15, 1946, pp. 20-23 incl. and p. 76.
Wheeler et 211.: Solid and Liquid Propellants, Journal of The Institute of Fuel, June 1947, No. 114, pp. 137-152 incl.
Hackhs Chemical Dictionary, 3rd edit., The Blakiston Co., Philadelphia, Pa., pp. 178, 575.
Bebie: Manual of Explosives, Military Pyrotechnics and Chemical Warfare Agents, The MacMillan Co., NY. (1943), pp. 43, 106-108.
Claims (1)
12. A SOLID SLOW BURNING PROPELLANT COMPOSITION CONSISTING ESSENTIALLY OF A CURED INTIMATE MIXTURE OF FROM ABOUT 45% TO 72% BY WEIGHT, OF SOLID NON-METALLIC INORGANIC OXIDIZING SALT SELECTED FROM THE GROUP CONSISTING OF AMMONIUM NITRATE, AMMONIUM PERCHLORATE, AND MIXTURES THEREOF; FROM ABOUT 5% TO 22%, BY WEIGHT, OF CELLULOSE NITRATE; AND FROM ABOUT 23% TO 36%, BY WEIGHT, OF THE TOTAL PROPELLANT COMPOSITION OF THE ADDITION POLYMERIZATION PRODUCT OF A MIXTURE OF DIETHYLENE GLYCOL BIS(ALLYL CARBONATE) AND LOWER ALKYL ESTER OF LOWER ALKENOIC ACID, PROVIDED THAT THE AMMONIUM PERCHLORATE PRESENT IN SAID PROPELLANT COMPOSITION SHALL IN NO EVENT EXCEED 60% BY WEIGHT OF THE TOTAL PROPELLAN COMPOSITION.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US209507A US3031347A (en) | 1951-02-05 | 1951-02-05 | Slow burning solid composite propellant |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US209507A US3031347A (en) | 1951-02-05 | 1951-02-05 | Slow burning solid composite propellant |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US3031347A true US3031347A (en) | 1962-04-24 |
Family
ID=22779007
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US209507A Expired - Lifetime US3031347A (en) | 1951-02-05 | 1951-02-05 | Slow burning solid composite propellant |
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Cited By (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3123507A (en) * | 1964-03-03 | Gas-generating compositions | ||
| US3180772A (en) * | 1961-12-04 | 1965-04-27 | Standard Oil Co | Ammonium nitrate propellant |
| US3197349A (en) * | 1963-02-15 | 1965-07-27 | Nitrochemie G M B H | Silicone propellant compositions containing nitroguanidine |
| US3234059A (en) * | 1963-11-18 | 1966-02-08 | Standard Oil Co | Igniter composition comprising pyrotechnic dispersion in solid propellant |
| DE1231146B (en) * | 1962-07-02 | 1966-12-22 | Thiokol Chemical Corp | Gas-generating mixture of substances |
| WO1996030716A1 (en) | 1995-03-31 | 1996-10-03 | Atlantic Research Corporation | An all pyrotechnic method of generating a particulate-free, non-toxic odorless and colorless gas |
| US5726382A (en) * | 1995-03-31 | 1998-03-10 | Atlantic Research Corporation | Eutectic mixtures of ammonium nitrate and amino guanidine nitrate |
| WO1998047836A2 (en) * | 1997-04-18 | 1998-10-29 | Atlantic Research Corporation | Ammonium perchlorate composition with chlorine scavenger |
| US5850053A (en) * | 1995-03-31 | 1998-12-15 | Atlantic Research Corporation | Eutectic mixtures of ammonium nitrate, guanidine nitrate and potassium perchlorate |
| US5985060A (en) * | 1998-07-25 | 1999-11-16 | Breed Automotive Technology, Inc. | Gas generant compositions containing guanidines |
| US5997666A (en) * | 1996-09-30 | 1999-12-07 | Atlantic Research Corporation | GN, AGN and KP gas generator composition |
| US20060272754A1 (en) * | 2002-11-14 | 2006-12-07 | Estes-Cox Corporation | Propellant composition and methods of preparation and use thereof |
| US20090184131A1 (en) * | 2006-05-04 | 2009-07-23 | Geiger Joerg | Pressure vessel containing polyethylene glycols and carbon dioxide as a propellant |
| US20090223611A1 (en) * | 2006-02-09 | 2009-09-10 | General Dynamics Ordnance And Tactical Systems- Canada Valleyfield Inc. | Black Powder Substitutes for Small Caliber Firearms |
| US20100286107A1 (en) * | 2007-10-05 | 2010-11-11 | Nektar Therapeutics | Oligomer-Corticosteroid Conjugates |
| US10018018B2 (en) | 2014-05-13 | 2018-07-10 | Baker Hughes, A Ge Company, Llc | System and method for providing a resilient solid fuel source in a wellbore |
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| US2165263A (en) * | 1939-07-11 | Macfie holm | ||
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3123507A (en) * | 1964-03-03 | Gas-generating compositions | ||
| US3180772A (en) * | 1961-12-04 | 1965-04-27 | Standard Oil Co | Ammonium nitrate propellant |
| DE1231146B (en) * | 1962-07-02 | 1966-12-22 | Thiokol Chemical Corp | Gas-generating mixture of substances |
| US3197349A (en) * | 1963-02-15 | 1965-07-27 | Nitrochemie G M B H | Silicone propellant compositions containing nitroguanidine |
| US3234059A (en) * | 1963-11-18 | 1966-02-08 | Standard Oil Co | Igniter composition comprising pyrotechnic dispersion in solid propellant |
| WO1996030716A1 (en) | 1995-03-31 | 1996-10-03 | Atlantic Research Corporation | An all pyrotechnic method of generating a particulate-free, non-toxic odorless and colorless gas |
| US5726382A (en) * | 1995-03-31 | 1998-03-10 | Atlantic Research Corporation | Eutectic mixtures of ammonium nitrate and amino guanidine nitrate |
| US5850053A (en) * | 1995-03-31 | 1998-12-15 | Atlantic Research Corporation | Eutectic mixtures of ammonium nitrate, guanidine nitrate and potassium perchlorate |
| US5997666A (en) * | 1996-09-30 | 1999-12-07 | Atlantic Research Corporation | GN, AGN and KP gas generator composition |
| WO1998047836A3 (en) * | 1997-04-18 | 1999-11-04 | Atlantic Res Corp | Ammonium perchlorate composition with chlorine scavenger |
| US5861571A (en) * | 1997-04-18 | 1999-01-19 | Atlantic Research Corporation | Gas-generative composition consisting essentially of ammonium perchlorate plus a chlorine scavenger and an organic fuel |
| WO1998047836A2 (en) * | 1997-04-18 | 1998-10-29 | Atlantic Research Corporation | Ammonium perchlorate composition with chlorine scavenger |
| US5985060A (en) * | 1998-07-25 | 1999-11-16 | Breed Automotive Technology, Inc. | Gas generant compositions containing guanidines |
| US20060272754A1 (en) * | 2002-11-14 | 2006-12-07 | Estes-Cox Corporation | Propellant composition and methods of preparation and use thereof |
| US20090223611A1 (en) * | 2006-02-09 | 2009-09-10 | General Dynamics Ordnance And Tactical Systems- Canada Valleyfield Inc. | Black Powder Substitutes for Small Caliber Firearms |
| US8133335B2 (en) | 2006-02-09 | 2012-03-13 | Mathieu Racette | Black powder substitutes for small caliber firearms |
| US20090184131A1 (en) * | 2006-05-04 | 2009-07-23 | Geiger Joerg | Pressure vessel containing polyethylene glycols and carbon dioxide as a propellant |
| US8240509B2 (en) * | 2006-05-04 | 2012-08-14 | Aerosol-Service Ag | Pressure vessel containing polyethylene glycols and carbon dioxide as a propellant |
| US20100286107A1 (en) * | 2007-10-05 | 2010-11-11 | Nektar Therapeutics | Oligomer-Corticosteroid Conjugates |
| US8796248B2 (en) | 2007-10-05 | 2014-08-05 | Nektar Therapeutics | Oligomer-corticosteroid conjugates |
| US11464788B2 (en) | 2007-10-05 | 2022-10-11 | Nektar Therapeutics | Oligomer-corticosteroid conjugates |
| US10018018B2 (en) | 2014-05-13 | 2018-07-10 | Baker Hughes, A Ge Company, Llc | System and method for providing a resilient solid fuel source in a wellbore |
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