US3679781A - Molding plastic coated nitrocellulose - Google Patents
Molding plastic coated nitrocellulose Download PDFInfo
- Publication number
- US3679781A US3679781A US867384A US3679781DA US3679781A US 3679781 A US3679781 A US 3679781A US 867384 A US867384 A US 867384A US 3679781D A US3679781D A US 3679781DA US 3679781 A US3679781 A US 3679781A
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- US
- United States
- Prior art keywords
- molding
- grains
- charge
- coated
- propellant
- Prior art date
- Legal status (The legal status 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 status listed.)
- Expired - Lifetime
Links
- 238000000465 moulding Methods 0.000 title claims abstract description 23
- 239000000020 Nitrocellulose Substances 0.000 title claims abstract description 17
- 229920001220 nitrocellulos Polymers 0.000 title claims abstract description 17
- 229920003023 plastic Polymers 0.000 title claims description 9
- 239000004033 plastic Substances 0.000 title claims description 9
- 239000002360 explosive Substances 0.000 claims abstract description 14
- 239000004449 solid propellant Substances 0.000 claims abstract description 13
- 239000003380 propellant Substances 0.000 claims description 29
- 238000000034 method Methods 0.000 claims description 24
- 239000011230 binding agent Substances 0.000 claims description 21
- TZRXHJWUDPFEEY-UHFFFAOYSA-N Pentaerythritol Tetranitrate Chemical group [O-][N+](=O)OCC(CO[N+]([O-])=O)(CO[N+]([O-])=O)CO[N+]([O-])=O TZRXHJWUDPFEEY-UHFFFAOYSA-N 0.000 claims description 10
- 239000000203 mixture Substances 0.000 claims description 9
- 238000010438 heat treatment Methods 0.000 claims description 7
- 239000007787 solid Substances 0.000 claims description 7
- 238000000748 compression moulding Methods 0.000 claims description 6
- 239000011248 coating agent Substances 0.000 claims description 5
- 238000000576 coating method Methods 0.000 claims description 5
- 238000001035 drying Methods 0.000 claims description 3
- 229920001169 thermoplastic Polymers 0.000 claims description 3
- 239000004416 thermosoftening plastic Substances 0.000 claims description 3
- 239000011118 polyvinyl acetate Substances 0.000 abstract description 10
- 229920002689 polyvinyl acetate Polymers 0.000 abstract description 10
- 238000004519 manufacturing process Methods 0.000 abstract description 3
- 238000011084 recovery Methods 0.000 abstract description 3
- 230000037452 priming Effects 0.000 abstract description 2
- 230000006835 compression Effects 0.000 abstract 1
- 238000007906 compression Methods 0.000 abstract 1
- 150000004655 tetrazenes Chemical class 0.000 description 5
- DOIRQSBPFJWKBE-UHFFFAOYSA-N dibutyl phthalate Chemical compound CCCCOC(=O)C1=CC=CC=C1C(=O)OCCCC DOIRQSBPFJWKBE-UHFFFAOYSA-N 0.000 description 4
- 239000006185 dispersion Substances 0.000 description 4
- 239000002904 solvent Substances 0.000 description 4
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 3
- 239000000460 chlorine Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000004615 ingredient Substances 0.000 description 3
- 229960001765 mannitol hexanitrate Drugs 0.000 description 3
- 239000004014 plasticizer Substances 0.000 description 3
- 229920002972 Acrylic fiber Polymers 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 229920002301 cellulose acetate Polymers 0.000 description 2
- 235000019441 ethanol Nutrition 0.000 description 2
- DGMJZELBSFOPHH-KVTDHHQDSA-N mannite hexanitrate Chemical compound [O-][N+](=O)OC[C@@H](O[N+]([O-])=O)[C@@H](O[N+]([O-])=O)[C@H](O[N+]([O-])=O)[C@H](O[N+]([O-])=O)CO[N+]([O-])=O DGMJZELBSFOPHH-KVTDHHQDSA-N 0.000 description 2
- 229920000642 polymer Polymers 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- XTFIVUDBNACUBN-UHFFFAOYSA-N 1,3,5-trinitro-1,3,5-triazinane Chemical compound [O-][N+](=O)N1CN([N+]([O-])=O)CN([N+]([O-])=O)C1 XTFIVUDBNACUBN-UHFFFAOYSA-N 0.000 description 1
- POAOYUHQDCAZBD-UHFFFAOYSA-N 2-butoxyethanol Chemical compound CCCCOCCO POAOYUHQDCAZBD-UHFFFAOYSA-N 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- PXGOKWXKJXAPGV-UHFFFAOYSA-N Fluorine Chemical compound FF PXGOKWXKJXAPGV-UHFFFAOYSA-N 0.000 description 1
- 230000001476 alcoholic effect Effects 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 229910052731 fluorine Inorganic materials 0.000 description 1
- 239000011737 fluorine Substances 0.000 description 1
- 229910002804 graphite Inorganic materials 0.000 description 1
- 239000010439 graphite Substances 0.000 description 1
- 231100001261 hazardous Toxicity 0.000 description 1
- 238000011031 large-scale manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- OKKJLVBELUTLKV-UHFFFAOYSA-N methanol Natural products OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 1
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 1
- UZGLIIJVICEWHF-UHFFFAOYSA-N octogen Chemical compound [O-][N+](=O)N1CN([N+]([O-])=O)CN([N+]([O-])=O)CN([N+]([O-])=O)C1 UZGLIIJVICEWHF-UHFFFAOYSA-N 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 229920002554 vinyl polymer Polymers 0.000 description 1
Classifications
-
- 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
- C06B45/105—The resin being a polymer bearing energetic groups or containing a soluble organic explosive
-
- C—CHEMISTRY; METALLURGY
- C06—EXPLOSIVES; MATCHES
- C06B—EXPLOSIVES OR THERMIC COMPOSITIONS; MANUFACTURE THEREOF; USE OF SINGLE SUBSTANCES AS EXPLOSIVES
- C06B21/00—Apparatus or methods for working-up explosives, e.g. forming, cutting, drying
- C06B21/0033—Shaping the mixture
- C06B21/005—By a process involving melting at least part of the ingredients
-
- 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
- C06B45/18—Compositions or products which are defined by structure or arrangement of component of product comprising a coated component
- C06B45/20—Compositions or products which are defined by structure or arrangement of component of product comprising a coated component the component base containing an organic explosive or an organic thermic component
- C06B45/22—Compositions or products which are defined by structure or arrangement of component of product comprising a coated component the component base containing an organic explosive or an organic thermic component the coating containing an organic compound
Definitions
- This invention relates in general to solid propellant charges and an improved method of molding such charges. More specifically, the invention relates to a hot molding method of compression molding a solid propellant charge.
- a further advantage of the hot molding process of the present invention is that it does not require collodion (nitrocellulose dissolved in ether-alcohol) so that the hot molding process is considerably less hazardous than the cold molding process disclosed in the Quinlan U.S. Pat. No. 3,282,751.
- the present invention permits the addition of other ingredients, e.g., high explosives such as PETN, RDX, HMX, and tetrazene to the charge by coating the ingredients and then compression molding all the ingredients together under suitable heat and pressure into the desired configuration and dimensions.
- primer mixes have been molded in similar fashion.
- Another object of the invention is to provide a method of hot molding propellant charges to consistent and accurate configuration and dimensions.
- Another object of the invention is to provide a high strength, molded, unitary propellant charge.
- the polyvinyl acetate polymer solution most frequently used consisted of Borden Companys Lemac 7, 20 percent plasticized by the addition of dibutyl phthalate to the alcoholic solution of the polymer;
- binders such as acrylic plastic and cellulose acetate, which are compatible with nitrocellulose can be used in place of polyvinyl acetate.
- the plastic should preferably not have any fluorine or chlorine, which upon ignition would form an acid that would be corrosive to the gun barrel.
- a binder content of about 1.2 percent polyvinyl acetate (by weight) has been found practical for most nitrocellulose propellants. Binder is applied from a suitable solvent solution, methyl or ethyl alcohol or other suitable solvent which has little or no solvent effect on nitrocellulose. A solvent solution of 10-20 percent concentration is preferred.
- a quantity of high explosive preferably PETN, preferably equal to the binder content is used.
- PETN preferably equal to the binder content
- other explosives such as RDX, HMX, or tetrazene may be used.
- the quantity of PETN can be decreased-or even eliminated altogether.
- the molded propellant charge will have a lower quickness and burning rate since the binder does act as a deterrent to ignition and burnmg.
- the temperature at which the propellant-binder mix is molded and the pressure used are related since a low temperature can be used with a high pressure and visa versa.
- primer mix has also been hot molded into discs in accordance with the technique of the present invention.
- a mix of percent tetrazene and 20 percent mannitol hexanitrate has been successfully hot molded.
- the tetrazene-mannitol hexanitrate mix was heated to the temperature range used with nitrocellulose, the percentage of polyvinyl acetate was increased to 2 percent, and the pressure used was 10,000 p.s.i. Tetrazene pellets were also formed by the same technique.
- plasticizers such as DuPont Elvacet or Borden Company's 804 PL plasticizer with dibutyl phthalate 15-25 percent
- plasticization being accomplished by stirring 20-30 minutes after the addition of the required water and plasticizer to the commercial dispersion (55 percent polyvinyl solids by weight) to bring the plasticized solids content to the desired concentration (30-35 percent).
- concentrations can be used if the dispersion is sprayed hot F.
- An ideal process would consist of hot spraying into heated tumbling barrel or other suitable mixes. This would permit rapid drying of the ovated propellant.
- a method of molding a solid propellent charge comprising the steps of:
- a method of molding a solid primer charge comprising the steps of:
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Crystallography & Structural Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Dispersion Chemistry (AREA)
- Molecular Biology (AREA)
- Casting Or Compression Moulding Of Plastics Or The Like (AREA)
- Compositions Of Macromolecular Compounds (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
Abstract
A hot-molded solid propellant or priming charge and the method of making the charge. Nitrocellulose grains are coated with plasticized polyvinyl acetate and then heated and compression molded whereupon the hot molded components retain their geometry and dimensional recovery is negligible. High explosive can be added to the charge prior to molding in order to improve quickness and burning rate of the charge.
Description
O United States Patent 51 3,679,78 1 Olson et al. 1 July 25, 1972 [54] MOLDING PLASTIC COATED [56] References Cited NITROCELLULOSE UNITED STATES PATENTS 2,2 8 41 ..I49 12 [72] Inventors: Theodore A. Olson, Trumbull; John J. 3 3 2x3 I Scanlon, Monroe, both of Conn. 3:235:42) 2/l966 Murphy N 7 Assigneez Remington Arms Company, Inc. 3,470,273 9/l969 Gordon et al ..264/3 B 'd ,C
n gepon Primary Examiner-Leland A. Sebastian [22] Filed: Oct. 17, 1969 Attorney-John H. Lewis, Jr. and Nicholas Skovran [21} Appl. No.: 867,384 [57] ABSTRACT 77 v e s V V A hot-molded solid propellant or priming charge and the [52] US. Cl. ..264/3 R, 149/1 1, 449/12, mehod of making the charge Nitrocellulose grains are coated 149/92, 149/100, 264/ E with plasticized polyvinyl acetate and then heated and com- [Sl] Int. Cl. p ession molded whereupon the hot molded components Field of Search 264/3 retain their geometry and dimensional recovery is negligible. 264/3 R High explosive can be added to the charge prior to molding in order to improve quickness and burning rate of the charge.
5 Claims, No Drawings MOLDING PLASTIC COATED NITROCELLUIDSE This invention relates in general to solid propellant charges and an improved method of molding such charges. More specifically, the invention relates to a hot molding method of compression molding a solid propellant charge.
The recent interest in caseless ammunition has resulted in increased efiorts to provide molded propellant charges which are easy and economical to manufacture, safe to store and handle, and ballistically suitable for the purposes intended. The advantages and objectives of caseless ammunition are well documented in the prior art and need not be repeated here. Among the more pertinent recent patents in this field are U.S. Pat. No. 3,212,440 issued to J. B. Quinlan et al. on Oct. 19, 1965, and U.S. Pat. No. 3,282,751, issued to J. B. Quinlan et al. on Nov. 1, 1966.
A second, somewhat similar field of interest in which molded propellant charges are very important is the expendable cartridge case concept as disclosed in such U.S. patent applications as Ser. No. 686,508, filed by J. J. Scanlon on Nov. 29, 1967, now U.S. Pat. No. 3,485,170, and Ser. No. 755,649, filed by M. W. Kordas et al., on Aug. 27, 1968. The present invention was developed for this type of expendable cartridge.
One of the deficiencies of the type of wet molding process disclosed in the Quinlan et al. U.S. Pat. No. 3,282,751 cited above is that it is very difficult to reproduce dimensions of the molded article. Because of this, the molded article must be machined or otherwise brought to the desired dimensions. Obviously, such a method leaves much to be desired in a mass production operation. With the present invention, it is possible to stamp propellant charges quickly and efi'lciently like bullets. The hot molded components retain their geometry and recovery is negligible. A further advantage of the hot molding process of the present invention is that it does not require collodion (nitrocellulose dissolved in ether-alcohol) so that the hot molding process is considerably less hazardous than the cold molding process disclosed in the Quinlan U.S. Pat. No. 3,282,751. The present invention permits the addition of other ingredients, e.g., high explosives such as PETN, RDX, HMX, and tetrazene to the charge by coating the ingredients and then compression molding all the ingredients together under suitable heat and pressure into the desired configuration and dimensions.
In addition to solid propellant charges being molded according to the present invention, primer mixes have been molded in similar fashion.
It is an object of this invention to provide an improved molded propellant charge of higher loading density.
Another object of the invention is to provide a method of hot molding propellant charges to consistent and accurate configuration and dimensions.
Another object of the invention is to provide a high strength, molded, unitary propellant charge.
Other objects and advantages will be obvious after reading the specification and the appended claims.
An acceptable proceSS which has been followed to produce molded propellant charges according to this invention is as follows:
1. Using a tumbling barrel, uniformly coat single base, unglazed or uncoated, i.e., with no graphite, nitrocellulose propellant grains with PETN (about 5 minutes) preferably using a quantity of PETN equal to the projected binder content;
2. Spray or drop on the PETN-coated propellant grains while in motion a sufficient quantity of plasticized polyvinyl acetate in alcohol solution to effect the required binder content. Tumble for about 5 minutes. Dry the mixture in any wellknown manner;
The polyvinyl acetate polymer solution most frequently used consisted of Borden Companys Lemac 7, 20 percent plasticized by the addition of dibutyl phthalate to the alcoholic solution of the polymer;
3. Heat the PETN and polyvinyl acetate coated propellant mixture to a temperature between from about 180 F. to about 230 F and 4. Compression-mold the heated propellant charge under pressure of about 6,000 p.s.i. to about 10,000 p.s.i. to its final configuration and dimensions.
Other binders, such as acrylic plastic and cellulose acetate, which are compatible with nitrocellulose can be used in place of polyvinyl acetate. In general, the plastic should preferably not have any fluorine or chlorine, which upon ignition would form an acid that would be corrosive to the gun barrel. A binder content of about 1.2 percent polyvinyl acetate (by weight) has been found practical for most nitrocellulose propellants. Binder is applied from a suitable solvent solution, methyl or ethyl alcohol or other suitable solvent which has little or no solvent effect on nitrocellulose. A solvent solution of 10-20 percent concentration is preferred.
To offset the deterrent effect of the binder, a quantity of high explosive, preferably PETN, preferably equal to the binder content is used. As mentioned above, other explosives such as RDX, HMX, or tetrazene may may be used. Obviously, if the molded propellant charge does not require the same quickness and/or burning rate as the original unmolded propellant grains, the quantity of PETN can be decreased-or even eliminated altogether. However, in this case, i.e., with no PETN or other suitable high explosive added, the molded propellant charge will have a lower quickness and burning rate since the binder does act as a deterrent to ignition and burnmg.
It should be appreciated that the temperature at which the propellant-binder mix is molded and the pressure used are related since a low temperature can be used with a high pressure and visa versa.
As mentioned above, primer mix has also been hot molded into discs in accordance with the technique of the present invention. A mix of percent tetrazene and 20 percent mannitol hexanitrate has been successfully hot molded. Although the tetrazene-mannitol hexanitrate mix was heated to the temperature range used with nitrocellulose, the percentage of polyvinyl acetate was increased to 2 percent, and the pressure used was 10,000 p.s.i. Tetrazene pellets were also formed by the same technique.
The process outlined above is suitable for laboratory purposes. However, for large scale production, water dispersions would be preferred and the binder solids content held to that concentration which can be efiectively sprayed.
For example, commercial dispersions such as DuPont Elvacet or Borden Company's 804 PL plasticizer with dibutyl phthalate 15-25 percent) or other compatible plasticizer can be effectively sprayed in concentrations of 30-35 percent plasticized solids by weight, plasticization being accomplished by stirring 20-30 minutes after the addition of the required water and plasticizer to the commercial dispersion (55 percent polyvinyl solids by weight) to bring the plasticized solids content to the desired concentration (30-35 percent). Higher concentrations can be used if the dispersion is sprayed hot F.) An ideal process would consist of hot spraying into heated tumbling barrel or other suitable mixes. This would permit rapid drying of the ovated propellant.
Although the laboratory work in hot molding propellant charges was done by heating the binder-coated propellant grains in an oven, it should be understood that the present hot molding process is not intended to be so limited. Thus, other methods of heating the propellant grains such as dielectric or ultrasonic heating can be used within the scope of this application.
What is claimed is:
l. A method of molding a solid propellent charge comprising the steps of:
l. coating individual unglazed powder grains of a single base nitrocellulose propellant with a plasticized thermoplastic binder, said binder constituting about 1.2 percent by weight of the final propellant charge and being compatible, non-acid forming plastic material selected from the group consisting of acrylic plastic, polyvinyl acetate, and cellulose acetate;
2. heating the binder-coated nitrocellulose propellant grains to a temperature of between about 180 F. to about 230 3. compression molding the heated and plastic bindercoated propellant grains under pressure of between about 6,000 psi to about 10,000 psi into the desired configuration and dimensions.
2. A method of molding a solid propellant charge as recited in Claim 1 wherein said nitrocellulose propellant grains are uniformly coated with a high explosive prior to being coated with said plastic binder so as to increase the quickness of the solid propellant charge.
3. A method of molding a solid propellant charge as recited in Claim 2 wherein said high explosive is PETN.
4. A method of molding a solid primer charge comprising the steps of:
l. coating grains of a primer mix comprising about percent tetrazene and about 20 percent mannitol hexanitrate with about 2 percent plasticized polyvinyl acetate binder by weight;
2. heating the coated explosive grains to a temperature of between about to about 230 F and 3. compression molding the heated explosive grains under about 10,000 p.s.i. pressure into the desired configuration.
5. A method of molding a solid propellant charge as recited in claim 1 in which the coating step comprises the distributing of the desired quantity of plasticized thermoplastic binder on to the nitrocellulose grains followed by tumbling of the coated propellant grains and finally drying of the mixture.
Claims (8)
- 2. heating the binder-coated nitrocellulose propellant grains to a temperature of between about 180* F. to about 230* F;
- 2. A method of molding a solid propellant charge as recited in Claim 1 wherein said nitrocellulose propellant grains are uniformly coated with a high explosive prior to being coated with said plastic binder so as to increase the quickness of the solid propellant charge.
- 2. heating the coated explosive grains to a temperature of between about 180* to about 230* F., and
- 3. compression molding the heated explosive grains under about 10,000 p.s.i. pressure into the desired configuration.
- 3. A method of molding a solid propellant charge as recited in Claim 2 wherein said high explosive is PETN.
- 3. compression molding the heated and plastic binder-coated propellant grains under pressure of between about 6,000 psi to about 10,000 psi into the desired configuration and dimensions.
- 4. A method of molding a solid primer charge comprising the steps of:
- 5. A method of molding a solid propellant charge as recited in claim 1 in which the coating step comprises the distributing of the desired quantity of plasticized thermoplastic binder on to the nitrocellulose grains followed by tumbling of the coated propellant grains and finally drying of the mixture.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US86738469A | 1969-10-17 | 1969-10-17 |
Publications (1)
Publication Number | Publication Date |
---|---|
US3679781A true US3679781A (en) | 1972-07-25 |
Family
ID=25349688
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US867384A Expired - Lifetime US3679781A (en) | 1969-10-17 | 1969-10-17 | Molding plastic coated nitrocellulose |
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US (1) | US3679781A (en) |
CA (1) | CA919433A (en) |
Cited By (20)
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---|---|---|---|---|
US4025591A (en) * | 1974-04-15 | 1977-05-24 | Jet Research Center, Inc. | Bonding explosive fillers with anaerobic curing binders |
US4115999A (en) * | 1975-03-13 | 1978-09-26 | The United States Of America As Represented By The Secretary Of The Navy | Use of high energy propellant in gas generators |
US4284592A (en) * | 1975-04-09 | 1981-08-18 | Imperial Metal Industries (Kynoch) Limited | Combustion inhibitors |
US4445948A (en) * | 1980-06-02 | 1984-05-01 | The United States Of America As Represented By The Secretary Of The Navy | Polymer modified TNT containing explosives |
FR2587328A1 (en) * | 1985-09-19 | 1987-03-20 | Poudres & Explosifs Ste Nale | Mixed propellent charges resistant to high temperature |
EP0238959A3 (en) * | 1986-03-27 | 1991-11-06 | Dynamit Nobel Aktiengesellschaft | Self-supporting propellant body and compact charge produced therefrom |
US5174837A (en) * | 1990-02-21 | 1992-12-29 | Societe Nationale Des Poudres Et Explosifs | Temperature-resistant, fragmentable propellent charges |
EP0679618A1 (en) * | 1994-04-30 | 1995-11-02 | Fraunhofer-Gesellschaft Zur Förderung Der Angewandten Forschung E.V. | Pyrotechnical charge for releasing stored gas from a pressure vessel |
US5567912A (en) * | 1992-12-01 | 1996-10-22 | The United States Of America As Represented By The Secretary Of The Army | Insensitive energetic compositions, and related articles and systems and processes |
US5719352A (en) * | 1993-04-22 | 1998-02-17 | The Kent Cartridge Manufacturing Co. Limited | Low toxicity shot pellets |
RU2337087C1 (en) * | 2007-01-25 | 2008-10-27 | Федеральное государственное унитарное предприятие "Научно-исследовательский институт полимерных материалов" | Method of solid ballistite propellant blank manufacture and device to implement it |
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RU2496759C1 (en) * | 2012-03-27 | 2013-10-27 | Федеральное казенное предприятие "Государственный научно-исследовательский институт химических продуктов" (ФКП "ГосНИИХП") | Pellet powder for 7,62 mm automatic cartridge |
RU2528984C2 (en) * | 2012-07-05 | 2014-09-20 | Федеральное казенное предприятие "Государственный научно-исследовательский институт химических продуктов" (ФКП "ГосНИИХП") | Modular throwing charge (versions) and method of its fabrication |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2235298A (en) * | 1935-06-10 | 1941-03-18 | Western Cartridge Co | Manufacture of smokeless powder |
US3173817A (en) * | 1962-10-31 | 1965-03-16 | Eastman Kodak Co | Granular explosive molding powder |
US3235420A (en) * | 1962-05-04 | 1966-02-15 | Du Pont | Process of making homogeneous particles comprising nitrocellulose mixtures |
US3470273A (en) * | 1966-06-10 | 1969-09-30 | Imp Metal Ind Kynoch Ltd | Top casting under pressure of rocket motor propellants |
-
1969
- 1969-10-17 US US867384A patent/US3679781A/en not_active Expired - Lifetime
-
1970
- 1970-04-24 CA CA081065A patent/CA919433A/en not_active Expired
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
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US2235298A (en) * | 1935-06-10 | 1941-03-18 | Western Cartridge Co | Manufacture of smokeless powder |
US3235420A (en) * | 1962-05-04 | 1966-02-15 | Du Pont | Process of making homogeneous particles comprising nitrocellulose mixtures |
US3173817A (en) * | 1962-10-31 | 1965-03-16 | Eastman Kodak Co | Granular explosive molding powder |
US3470273A (en) * | 1966-06-10 | 1969-09-30 | Imp Metal Ind Kynoch Ltd | Top casting under pressure of rocket motor propellants |
Cited By (21)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4025591A (en) * | 1974-04-15 | 1977-05-24 | Jet Research Center, Inc. | Bonding explosive fillers with anaerobic curing binders |
US4115999A (en) * | 1975-03-13 | 1978-09-26 | The United States Of America As Represented By The Secretary Of The Navy | Use of high energy propellant in gas generators |
US4284592A (en) * | 1975-04-09 | 1981-08-18 | Imperial Metal Industries (Kynoch) Limited | Combustion inhibitors |
US4445948A (en) * | 1980-06-02 | 1984-05-01 | The United States Of America As Represented By The Secretary Of The Navy | Polymer modified TNT containing explosives |
FR2587328A1 (en) * | 1985-09-19 | 1987-03-20 | Poudres & Explosifs Ste Nale | Mixed propellent charges resistant to high temperature |
EP0238959A3 (en) * | 1986-03-27 | 1991-11-06 | Dynamit Nobel Aktiengesellschaft | Self-supporting propellant body and compact charge produced therefrom |
US5174837A (en) * | 1990-02-21 | 1992-12-29 | Societe Nationale Des Poudres Et Explosifs | Temperature-resistant, fragmentable propellent charges |
US5567912A (en) * | 1992-12-01 | 1996-10-22 | The United States Of America As Represented By The Secretary Of The Army | Insensitive energetic compositions, and related articles and systems and processes |
US5719352A (en) * | 1993-04-22 | 1998-02-17 | The Kent Cartridge Manufacturing Co. Limited | Low toxicity shot pellets |
US5623121A (en) * | 1994-04-30 | 1997-04-22 | Fraunhofer-Gesellschaft Zur Forderung Der Angewandten Forschung E.V. | Pyrotechnic charge for releasing enclosed pressurized gas |
EP0679618A1 (en) * | 1994-04-30 | 1995-11-02 | Fraunhofer-Gesellschaft Zur Förderung Der Angewandten Forschung E.V. | Pyrotechnical charge for releasing stored gas from a pressure vessel |
RU2337087C1 (en) * | 2007-01-25 | 2008-10-27 | Федеральное государственное унитарное предприятие "Научно-исследовательский институт полимерных материалов" | Method of solid ballistite propellant blank manufacture and device to implement it |
RU2338732C1 (en) * | 2007-02-19 | 2008-11-20 | Федеральное государственное унитарное предприятие "Научно-исследовательский институт полимерных материалов" | Production method of ballistite solid propellant charge components as thin-arched tubes and related device for implementation thereof |
RU2382019C1 (en) * | 2008-05-30 | 2010-02-20 | Общество с ограниченной ответственностью "Бизон" | Block propellant porous charge (versions) and method of its manufacturing |
RU2451002C1 (en) * | 2010-11-22 | 2012-05-20 | Федеральное государственное унитарное предприятие "Научно-исследовательский институт полимерных материалов" | Method of fabricating thin-layer powder-filled fuses |
RU2487110C1 (en) * | 2012-01-30 | 2013-07-10 | Федеральное казенное предприятие "Государственный научно-исследовательский институт химических продуктов" (ФКП "ГосНИИХП") | BALL PYROXYLIC POWDER FOR 5,6 mm SPORTING RIFLE RIM-FIRE CARTRIDGE |
RU2487109C1 (en) * | 2012-01-31 | 2013-07-10 | Федеральное казенное предприятие "Государственный научно-исследовательский институт химических продуктов" (ФКП "ГосНИИХП") | BALL PYROXILIC POWDER FOR 9 mm SPORTS PISTOL CARTRIDGE |
RU2487853C1 (en) * | 2012-02-20 | 2013-07-20 | Федеральное казенное предприятие "Государственный научно-исследовательский институт химических продуктов" (ФКП "ГосНИИХП") | PELLET POWDER FOR 7,62 mm RIFLE CARTRIDGE |
RU2495861C1 (en) * | 2012-03-27 | 2013-10-20 | Федеральное казенное предприятие "Государственный научно-исследовательский институт химических продуктов" (ФКП "ГосНИИХП") | Charge for 7,62 mm automatic rifle cartridge |
RU2496759C1 (en) * | 2012-03-27 | 2013-10-27 | Федеральное казенное предприятие "Государственный научно-исследовательский институт химических продуктов" (ФКП "ГосНИИХП") | Pellet powder for 7,62 mm automatic cartridge |
RU2528984C2 (en) * | 2012-07-05 | 2014-09-20 | Федеральное казенное предприятие "Государственный научно-исследовательский институт химических продуктов" (ФКП "ГосНИИХП") | Modular throwing charge (versions) and method of its fabrication |
Also Published As
Publication number | Publication date |
---|---|
CA919433A (en) | 1973-01-23 |
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