US2715574A - Process of making spherical powder grains - Google Patents

Process of making spherical powder grains Download PDF

Info

Publication number
US2715574A
US2715574A US231647A US23164751A US2715574A US 2715574 A US2715574 A US 2715574A US 231647 A US231647 A US 231647A US 23164751 A US23164751 A US 23164751A US 2715574 A US2715574 A US 2715574A
Authority
US
United States
Prior art keywords
solvent
lacquer
globules
medium
grains
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
Application number
US231647A
Inventor
Gilbert R Cox
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Olin Corp
Original Assignee
Olin Corp
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 Olin Corp filed Critical Olin Corp
Priority to US231647A priority Critical patent/US2715574A/en
Application granted granted Critical
Publication of US2715574A publication Critical patent/US2715574A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C06EXPLOSIVES; MATCHES
    • C06BEXPLOSIVES OR THERMIC COMPOSITIONS; MANUFACTURE THEREOF; USE OF SINGLE SUBSTANCES AS EXPLOSIVES
    • C06B21/00Apparatus or methods for working-up explosives, e.g. forming, cutting, drying
    • C06B21/0033Shaping the mixture
    • C06B21/0066Shaping the mixture by granulation, e.g. flaking

Definitions

  • This invention relates to the manufacture of propellent powders and more particularly to a process of manufacturing substantially spherical grains of smokeless powder.
  • nonsolvent medium dissolved in or miscible with the solvent will be included within the lacquer globules when the globules are formed.
  • some non-solvent may remain therein and the resulting powder grains have a porous internal structure.
  • Schaefer in the aforesaid patent discloses a method of controlling the porosity of the powder grain wherein the non-solvent medium without the globules is differentiated from the non-solvent medium within the globules in order to cause relative migration of the non-solvent medium within and without the globules.
  • Such difierentiation can be accomplished by ineluding in the non-solvent medium some salt such as sodium sulfate.
  • some salt such as sodium sulfate.
  • solvents such as methyl ethyl ketone, having increasingly greater solvency for the non-solvent medium, such as water, are utilized for the lacquer vehicle.
  • An object of this invention is to provide an improved method of making substantially non-porous spherical powder grains when a solvent is employed in which the non-solvent medium is partially soluble. Another object is to provide a novel method of controlling the porosity of substantially spherical powder grains. A still further and more specific object of this invention is to provide a process of controlling the quantity of non-solvent medium included in the globules of lacquer utilized in the I! manufacture of substantially spherical powder grains. Still another object of this invention is to provide a process of manufacturing substantially spherical powder grains even when solvents substantially miscible with the non-solvent medium are utilized.
  • this invention contemplates a process of controlling the porosity of the spherical powder grains wherein the quantity of non-solvent medium within the globules of lacquer formed in the process is controlled by limiting the miscibility of the lacquer vehicle with the non-solvent medium by includii g a non-solvent diluent substantially miscible with the smokeless powder base solvent and substantially immiscible with the non-solvent medium in the lacquer vehicle.
  • Solvents and non-solvent diluents having a boiling point less than that of the non-solvent medium are preferred.
  • the non-solvent medium is water, solvents and non-solvent diluents having boiling points between about 50 C. and about 100 C. have been found particularly desirable.
  • the actual composition of the lacquer vehicle which will give optimum results will of course vary with the solubility of the non-solvent medium in the smokeless powder base solvent utilized and the powder grain density desired.
  • methyl ethyl ketone for example, is utilized as the solvent and water as the nonsolvent medium, as little as about 5% non-solvent diluent is sufiicient to produce high density powder having a specific gravity of 1.4 or more.
  • Vehicles comprising as much as about toluene have been utilized to advantage in making high density powder from a smokeless powder base having a nitrogen content of about 12.6%.
  • Amounts of non-solvent diluents of from about 5% to 20% may be utilized in the manufacture of high density powder from either pyro or gun-cotton grades of smokeless powder base; in order to obtain optimum results, the non-solvent diluent should be mixed with the smokeless powder base solvent prior to forming the lacquer. In most instances a ratio of about 2.5 to 6 parts vehicle to 1 part smokeless powder base forms a lacquer having the proper physical properties.
  • Approximately 65 parts nitrocellulose of about 12.6% nitrogen content are suspended in about 900 parts water.
  • About 380 parts lacquer vehicle containing about methyl ethyl ketone saturated with water and about 5% toluene are added and the resulting mixture agitated until the nitrocellulose is completely dissolved.
  • About 35 parts gum arabic dissolved in about parts water are added and agitation continued until the lacquer is completely dispersed in the water phase and the individual globules thus formed become substantially spherical.
  • Approximately 35 parts sodium sulfate dissolved in about 80 parts water are then added and the lacquer vehicle removed from the lacquer globules by distillation while maintained in suspension in the water by means of gentle agitation.
  • the solidified grains are later dewatered by filtering and oven drying. High density owder grains having a specific gravity between about 1.5 and 1.6 are produced in accordance with this process.
  • ethyl formate isopropyl acetate, diethyl ketone and the like can be utilized in the foregoing embodiment.
  • other non-solvent diluents such as the liquid hydrocarbons xylene, benzene, pentane, hexane, heptane, octane, nonane, decane, undecane or dodecane or other compatible water immiscible diluents such as isopropyl ether, propyl ether, cyclohexane, methylcyclohexane, or the like can be utilized instead of toluene.
  • stabilizers such as diphenylamine, ethyl centralite and the like, deterrents such as dinitrotoluene, dibutylphthalate and the like and other modifying agents such as lead compounds, cyclotrimethylenetrinitramine, carbon black and the like may be included in the lacquer in accordance with the usual practice.
  • lacquer vehicle consists of methyl ethyl ketone saturated with water
  • low density powder grains having a specific gravity of about 1.3, 1.4 or less are produced.
  • the invention accomplishes its objects and provides an improved method of producing substantially non-porous powder grains and a method of controlling the porosity of spherical powder grains wherein the quantity of non-solvent medium within the lacquer globules formed in the manufacture of spherical grains of powder is regulated.
  • the process for making substantially non-porous powder grains from a lacquer containing a solvent which is at least partially miscible with the nonsolvent medium which comprises reducing the quantity of non-solvent medium dispersed within the lacquer globules by including a volatile liquid non-solvent diluent substantially miscible with the solvent and substantially immiscible with the non-solvent medium and differentiating the non-solvent medium without the globules from that within the globules.
  • substantially spherical powder grains by the process which involves dispersing globules of a smokeless powder base lacquer in a non-solvent medium and thereafter solidifying the globules while thus dispersed, the step of providing resulting powder grains with low porosity which comprises the inclusion in said lacquer of a volatile non-solvent diluent which is substantially miscible with the solvent in said lacquer and which reduces the solubility of said non-solvent medium in said lacquer.
  • the process for making substantially non-porous powder grains from a lacquer containing a solvent at least partially miscible with the non-solvent medium which comprises reducing the quantity of non-solvent medium dispersed within the lacquer globules by including therein a volatile liquid non-solvent for the smokeless powder base which is substantially miscible with the solvent and substantially immiscible with the non-solvent medium.
  • the process for shaping and solidifying smokeless powder base lacquer into substantially spherical grains of propellent powder having a predetermined porosity which comprises dissolving the smokeless powder base in a volatile solvent for the smokeless powder base which is at at least partially miscible with the suspending medium and is mixed with a volatile liquid non-solvent which is substantially miscible therewith and reduces the solubility of the suspending medium in the solvent, and thereafter removing the vehicle from the lacquer globules while they are thus suspended.

Description

2,715,574 PROCESS OF MAKING SPHERICAL POWDER GRAINS Gilbert R. Cox, Creve Coeur, Mo., assignor to Olin Mathieson Chemical Corporation, a corporation of Virginia No Drawing. Application June 14, 1951, Serial No. 231,647
14 Claims. (Cl. 52-20) This invention relates to the manufacture of propellent powders and more particularly to a process of manufacturing substantially spherical grains of smokeless powder.
Heretofore, spherical grains of smokeless powder have been made in accordance with the process disclosed in U. S. Patent 2,027,114, granted January 7, 193 6, to Olsen, Tibbitts and Kerone, in which globules of lacquer, composed of a smokeless powder base and a solvent, are suspended in a non-solvent medium and the globules solidified while thus suspended. As pointed out by Schaefer in U. S. Patent 2,160,626, there is often a tendency in the foregoing process for the non-solvent medium in which the globules are suspended to diffuse into the globules or to becomes emulsified therein. In addition, if the solvent is not entirely immiscible with the non-solvent medium, nonsolvent medium dissolved in or miscible with the solvent will be included within the lacquer globules when the globules are formed. As the solvent is removed from the globules of lacquer by vaporization, some non-solvent may remain therein and the resulting powder grains have a porous internal structure. Schaefer in the aforesaid patent discloses a method of controlling the porosity of the powder grain wherein the non-solvent medium without the globules is differentiated from the non-solvent medium within the globules in order to cause relative migration of the non-solvent medium within and without the globules. Such difierentiation can be accomplished by ineluding in the non-solvent medium some salt such as sodium sulfate. However, it becomes increasingly more ditlicult to make substantially non-porous or high density powder grains in accordance with such a process when solvents, such as methyl ethyl ketone, having increasingly greater solvency for the non-solvent medium, such as water, are utilized for the lacquer vehicle.
An object of this invention is to provide an improved method of making substantially non-porous spherical powder grains when a solvent is employed in which the non-solvent medium is partially soluble. Another object is to provide a novel method of controlling the porosity of substantially spherical powder grains. A still further and more specific object of this invention is to provide a process of controlling the quantity of non-solvent medium included in the globules of lacquer utilized in the I! manufacture of substantially spherical powder grains. Still another object of this invention is to provide a process of manufacturing substantially spherical powder grains even when solvents substantially miscible with the non-solvent medium are utilized.
The foregoing objects as well as others which will become apparent from the following description are accomplished in accordance with this invention, generally stated, by suspending globules of lacquer containing a smokeless powder base, a solvent therefor and a non-solvent diluent miscible with the solvent in a nonsolvent medium which is substantially immiscible with the non-solvent diluent, and then solidifying said globules while thus suspended. More specifically this invention contemplates a process of controlling the porosity of the spherical powder grains wherein the quantity of non-solvent medium within the globules of lacquer formed in the process is controlled by limiting the miscibility of the lacquer vehicle with the non-solvent medium by includii g a non-solvent diluent substantially miscible with the smokeless powder base solvent and substantially immiscible with the non-solvent medium in the lacquer vehicle. While no definite theory is known which com plete'ly explains the function of the non-solvent diluent in the lacquer vehicle, the solubility of the nonsolvent medium in the smokeless powder base solvent is reduced by the addition of a non-solvent diluent, and, generally, the more the diluent added the less the solubility. It is also appreciated that thenon-solvent diluent might also affect the interfacial tension of the solvent and nonsolvent medium. With the employment of the diluent, the non-solvent medium without the globules may be differentiated from that within the globules as disclosed by ,Schaefer in U. S. 2,160,626 in order to obtain even higher density powder grains.
Solvents and non-solvent diluents having a boiling point less than that of the non-solvent medium are preferred. It the non-solvent medium is water, solvents and non-solvent diluents having boiling points between about 50 C. and about 100 C. have been found particularly desirable. The actual composition of the lacquer vehicle which will give optimum results will of course vary with the solubility of the non-solvent medium in the smokeless powder base solvent utilized and the powder grain density desired. When methyl ethyl ketone, for example, is utilized as the solvent and water as the nonsolvent medium, as little as about 5% non-solvent diluent is sufiicient to produce high density powder having a specific gravity of 1.4 or more. Vehicles comprising as much as about toluene have been utilized to advantage in making high density powder from a smokeless powder base having a nitrogen content of about 12.6%. Amounts of non-solvent diluents of from about 5% to 20% may be utilized in the manufacture of high density powder from either pyro or gun-cotton grades of smokeless powder base; in order to obtain optimum results, the non-solvent diluent should be mixed with the smokeless powder base solvent prior to forming the lacquer. In most instances a ratio of about 2.5 to 6 parts vehicle to 1 part smokeless powder base forms a lacquer having the proper physical properties.
In order to further explain and clarify this invention, following is a typical embodiment thereof wherein a lacquer vehicle comprising a non-solvent diluent is used to advantage in the production of non-porous or high density spherical powder grains:
Approximately 65 parts nitrocellulose of about 12.6% nitrogen content are suspended in about 900 parts water. About 380 parts lacquer vehicle containing about methyl ethyl ketone saturated with water and about 5% toluene are added and the resulting mixture agitated until the nitrocellulose is completely dissolved. About 35 parts gum arabic dissolved in about parts water are added and agitation continued until the lacquer is completely dispersed in the water phase and the individual globules thus formed become substantially spherical. Approximately 35 parts sodium sulfate dissolved in about 80 parts water are then added and the lacquer vehicle removed from the lacquer globules by distillation while maintained in suspension in the water by means of gentle agitation. The solidified grains are later dewatered by filtering and oven drying. High density owder grains having a specific gravity between about 1.5 and 1.6 are produced in accordance with this process.
Instead of methyl ethyl ketone, other suitable solvents for the smokeless powder base such as ethyl acetate,
ethyl formate, isopropyl acetate, diethyl ketone and the like can be utilized in the foregoing embodiment. Likewise, other non-solvent diluents such as the liquid hydrocarbons xylene, benzene, pentane, hexane, heptane, octane, nonane, decane, undecane or dodecane or other compatible water immiscible diluents such as isopropyl ether, propyl ether, cyclohexane, methylcyclohexane, or the like can be utilized instead of toluene. If desired, other materials, for example, stabilizers such as diphenylamine, ethyl centralite and the like, deterrents such as dinitrotoluene, dibutylphthalate and the like and other modifying agents such as lead compounds, cyclotrimethylenetrinitramine, carbon black and the like may be included in the lacquer in accordance with the usual practice.
When the foregoing example is followed with the exception that the lacquer vehicle consists of methyl ethyl ketone saturated with water, low density powder grains having a specific gravity of about 1.3, 1.4 or less are produced.
From the foregoing description, it will be apparent to those skilled in the art that the invention accomplishes its objects and provides an improved method of producing substantially non-porous powder grains and a method of controlling the porosity of spherical powder grains wherein the quantity of non-solvent medium within the lacquer globules formed in the manufacture of spherical grains of powder is regulated.
While the foregoing embodiment has been described in detail, it is to be distinctly understood that various modifications of the procedure will occur to those skilled in the art and that the invention is not limited tothe specific embodiment hereinbefore set forth, except as indicated in the appended claims.
Having thus described the invention, what is claimed and desired to secure by Letters Patent is:
1. in the manufacture of powder grains by dispersing globules of smokeless powder base lacquer in a nonsolvent medium, the process of reducing the quantity of non-solvent medium dispersed Within said globules which comprises including in the lacquer a volatile liquid nonsolvent diluent which is substantially miscible with the lacquer solvent and substantially immiscible with the non-solvent medium.
2. In the manufacture of powder grains by dispersing globules of smokeless powder base lacquer in a nonsolvent medium, the process for making substantially non-porous powder grains from a lacquer containing a solvent which is at least partially miscible with the nonsolvent medium which comprises reducing the quantity of non-solvent medium dispersed within the lacquer globules by including a volatile liquid non-solvent diluent substantially miscible with the solvent and substantially immiscible with the non-solvent medium and differentiating the non-solvent medium without the globules from that within the globules.
3. The process of claim 1 wherein the lacquer has a boiling range between about 50 C. and 100 C. and the non-solvent medium is water.
4. The process of claim 1 wherein the solvent is methyl ethyl ketone, the non-solvent diluent toluene, and the non-solvent medium water.
5. The process of claim 4 wherein the non-solvent diluent is hexane.
6. The process of claim 2 wherein said globules are solidified in the presence of a protective colloid.
7. The process as set forth in claim 2 in which the amount of non-solvent diluent is within the range of about 5 per cent to about per cent of the lacquer vehicle.
8. The process as set forth in claim 7 in which the non-solvent medium without the globules is differentiated from that within the globules, and said globules are solidified in the presence of a protective colloid.
9. In the manufacture of substantially spherical powder grains by the process which involves dispersing globules of a smokeless powder base lacquer in a non-solvent medium and thereafter solidifying the globules while thus dispersed, the step of providing resulting powder grains with low porosity which comprises the inclusion in said lacquer of a volatile non-solvent diluent which is substantially miscible with the solvent in said lacquer and which reduces the solubility of said non-solvent medium in said lacquer.
10. The process of claim 9 in which said diluent is a liquid hydrocarbon and said medium is water.
11. in the manufacture of substantially spherical powder grains by a process which involves dispersing globules of a smokeless powder base lacquer in a non-solvent medium, the step which comprises including in said lacquer a volatile non-solvent diluent.
12. In the manufacture of powder grains by a process which involves dispersing globules of lacquer containing a smokeless powder and a solvent therefor in a non-solvent medium and thereafter solidifying the globules of lacquer while thus dispersed, the process for making substantially non-porous powder grains from a lacquer containing a solvent at least partially miscible with the non-solvent medium which comprises reducing the quantity of non-solvent medium dispersed within the lacquer globules by including therein a volatile liquid non-solvent for the smokeless powder base which is substantially miscible with the solvent and substantially immiscible with the non-solvent medium.
13. in the manufacture of powder grains by dispersing globules'of smokeless powder base lacquer in a nonsolvent medium partially miscible therewith and thereafter solidifying said globules, the method of reducing the miscibility of the lacquer with said medium which comprises including a volatile liquid non-solvent diluent in the lacquer.
14. In the manufacture of powder grains by suspending globules of a smokeless powder base lacquer in a non-solvent medium and solidifying the globules while thus suspended, the process for shaping and solidifying smokeless powder base lacquer into substantially spherical grains of propellent powder having a predetermined porosity which comprises dissolving the smokeless powder base in a volatile solvent for the smokeless powder base which is at at least partially miscible with the suspending medium and is mixed with a volatile liquid non-solvent which is substantially miscible therewith and reduces the solubility of the suspending medium in the solvent, and thereafter removing the vehicle from the lacquer globules while they are thus suspended.
References Cited in the file of this patent

Claims (1)

1. IN THE MANUFACTURE OF POWDER GRAINS BY DISPERSING GLOBULES OF SMOKELESS POWDER BASE LAQUER IN A NONSOLVENT MEDIUM, THE PREOCESS OF REDUCING THE QUANTITY OF NON-SOLVENT MEDIUM DISPERSED WITHIN SAID GLOBULES WHICH COMPRISES INCLUDING IN THE LACQUER A VOLATILE LIQUID NONSOLVENT DILUENT WHICH IS SUBSTANTIALLY MISCIBLE WITH THE LACQUER SOLVENT AND SUBSTANTIALLY IMMISCIBLE WITH THE NON-SOLVENT MEDIUM.
US231647A 1951-06-14 1951-06-14 Process of making spherical powder grains Expired - Lifetime US2715574A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US231647A US2715574A (en) 1951-06-14 1951-06-14 Process of making spherical powder grains

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US231647A US2715574A (en) 1951-06-14 1951-06-14 Process of making spherical powder grains

Publications (1)

Publication Number Publication Date
US2715574A true US2715574A (en) 1955-08-16

Family

ID=22870103

Family Applications (1)

Application Number Title Priority Date Filing Date
US231647A Expired - Lifetime US2715574A (en) 1951-06-14 1951-06-14 Process of making spherical powder grains

Country Status (1)

Country Link
US (1) US2715574A (en)

Cited By (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2915519A (en) * 1954-09-28 1959-12-01 Atlantic Res Corp Processing cellulose nitrate
US2931801A (en) * 1954-08-13 1960-04-05 Atlantic Res Corp Cellulose nitrate
US2931800A (en) * 1954-08-13 1960-04-05 Atlantic Res Corp Cellulose nitrate product
US2935414A (en) * 1958-05-22 1960-05-03 Olin Mathieson Nitrocellulose lacquers
US3236702A (en) * 1964-04-08 1966-02-22 Hercules Powder Co Ltd Manufacture of densified spheroidal fine particle nitrocellulose
US3284253A (en) * 1963-08-27 1966-11-08 Hercules Inc Densified nitrocellulose-hydrocarbon product and process of manufacture
US3325572A (en) * 1966-05-24 1967-06-13 Hercules Inc Process for preparing small, densified nitrocellulose particles
US3325571A (en) * 1966-01-25 1967-06-13 Hercules Inc Process for the manufacture of smokeless powder
US3325315A (en) * 1965-12-14 1967-06-13 Hercules Inc Manufacture of densified spheroidal nitrocellulose of high viscosity at casting temperatures
US3341515A (en) * 1964-07-28 1967-09-12 Hercules Inc Manufacture of hydrocarbon-wet, densified nitrocellulose
US3346675A (en) * 1966-09-08 1967-10-10 Hercules Inc Method of preparing small particle nitrocellulose
RU2622129C1 (en) * 2015-12-28 2017-06-13 Федеральное казенное предприятие "Государственный научно-исследовательский институт химических продуктов" (ФКП "ГосНИИХП") Method of producing ball powder
RU2653029C1 (en) * 2017-02-17 2018-05-04 Федеральное казенное предприятие "Государственный научно-исследовательский институт химических продуктов" (ФКП "ГосНИИХП") Method for obtaining large-dispersed spherical powder
RU2800299C1 (en) * 2022-08-05 2023-07-19 Федеральное казенное предприятие "Государственный научно-исследовательский институт химических продуктов" Method for producing spherical powder

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2027114A (en) * 1932-03-12 1936-01-07 Western Cartridge Co Manufacture of smokeless powders
US2160626A (en) * 1936-01-02 1939-05-30 Western Cartridge Co Explosive
US2213255A (en) * 1936-01-06 1940-09-03 Western Cartridge Co Explosive
US2292469A (en) * 1939-09-25 1942-08-11 Western Cartridge Co Smokeless powder
US2394449A (en) * 1942-12-12 1946-02-05 Olin Ind Inc Manufacture of explosives

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2027114A (en) * 1932-03-12 1936-01-07 Western Cartridge Co Manufacture of smokeless powders
US2160626A (en) * 1936-01-02 1939-05-30 Western Cartridge Co Explosive
US2213255A (en) * 1936-01-06 1940-09-03 Western Cartridge Co Explosive
US2292469A (en) * 1939-09-25 1942-08-11 Western Cartridge Co Smokeless powder
US2394449A (en) * 1942-12-12 1946-02-05 Olin Ind Inc Manufacture of explosives

Cited By (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2931801A (en) * 1954-08-13 1960-04-05 Atlantic Res Corp Cellulose nitrate
US2931800A (en) * 1954-08-13 1960-04-05 Atlantic Res Corp Cellulose nitrate product
US2915519A (en) * 1954-09-28 1959-12-01 Atlantic Res Corp Processing cellulose nitrate
US2935414A (en) * 1958-05-22 1960-05-03 Olin Mathieson Nitrocellulose lacquers
US3284253A (en) * 1963-08-27 1966-11-08 Hercules Inc Densified nitrocellulose-hydrocarbon product and process of manufacture
US3236702A (en) * 1964-04-08 1966-02-22 Hercules Powder Co Ltd Manufacture of densified spheroidal fine particle nitrocellulose
US3341515A (en) * 1964-07-28 1967-09-12 Hercules Inc Manufacture of hydrocarbon-wet, densified nitrocellulose
US3325315A (en) * 1965-12-14 1967-06-13 Hercules Inc Manufacture of densified spheroidal nitrocellulose of high viscosity at casting temperatures
US3325571A (en) * 1966-01-25 1967-06-13 Hercules Inc Process for the manufacture of smokeless powder
US3325572A (en) * 1966-05-24 1967-06-13 Hercules Inc Process for preparing small, densified nitrocellulose particles
US3346675A (en) * 1966-09-08 1967-10-10 Hercules Inc Method of preparing small particle nitrocellulose
RU2622129C1 (en) * 2015-12-28 2017-06-13 Федеральное казенное предприятие "Государственный научно-исследовательский институт химических продуктов" (ФКП "ГосНИИХП") Method of producing ball powder
RU2653029C1 (en) * 2017-02-17 2018-05-04 Федеральное казенное предприятие "Государственный научно-исследовательский институт химических продуктов" (ФКП "ГосНИИХП") Method for obtaining large-dispersed spherical powder
RU2800299C1 (en) * 2022-08-05 2023-07-19 Федеральное казенное предприятие "Государственный научно-исследовательский институт химических продуктов" Method for producing spherical powder

Similar Documents

Publication Publication Date Title
US2715574A (en) Process of making spherical powder grains
US4102953A (en) Method for making extruded, solventless, composite-modified double base propellant
US2375175A (en) Smokeless powder process
DE2634195C3 (en) Thermostable composite explosive and its manufacturing process
US3702272A (en) Spherical rocket propellant casting granules and method of preparation
US3266957A (en) Booster explosive of ultrafine desensitized cyclotrimethylene-trinitramine and method of preparing same
US2160626A (en) Explosive
US2988438A (en) Combustible compositions
US4008110A (en) Water gel explosives
US2213255A (en) Explosive
US2292469A (en) Smokeless powder
EP0509200A1 (en) Process for the fabrication of phlegmatized explosives
US3329743A (en) Lacquer process for preparing small diameter nitrocellulose particles
US2885736A (en) Nitrocellulose particles
US3422170A (en) Slurry casting manufacture of nitrocellulose propellant grains
US2771035A (en) Propellant
US2973257A (en) Propellent powder
US4705582A (en) Desensitized explosive composition
US2916996A (en) Propellent powder
US3163567A (en) Production of disc-shaped nitrocellulose
US3037891A (en) Smokeless powder
US3422169A (en) Nitrocellulose product and method of manufacture of propellant grains employing same
US2407805A (en) Explosive composition
US3702271A (en) Azeotropic removal of water from ordnance
US2982643A (en) Nitrocellulose