WO2003035581A2 - Herstellung wasserfreier nitrocellulose und explosivstoffe in sphäroider form - Google Patents
Herstellung wasserfreier nitrocellulose und explosivstoffe in sphäroider form Download PDFInfo
- Publication number
- WO2003035581A2 WO2003035581A2 PCT/EP2002/011850 EP0211850W WO03035581A2 WO 2003035581 A2 WO2003035581 A2 WO 2003035581A2 EP 0211850 W EP0211850 W EP 0211850W WO 03035581 A2 WO03035581 A2 WO 03035581A2
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- explosive
- nitrocellulose
- water
- particles
- solvent
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L1/00—Compositions of cellulose, modified cellulose or cellulose derivatives
- C08L1/08—Cellulose derivatives
- C08L1/16—Esters of inorganic acids
- C08L1/18—Cellulose nitrate, i.e. nitrocellulose
-
- 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
-
- 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
- C06B21/0066—Shaping the mixture by granulation, e.g. flaking
-
- C—CHEMISTRY; METALLURGY
- C06—EXPLOSIVES; MATCHES
- C06B—EXPLOSIVES OR THERMIC COMPOSITIONS; MANUFACTURE THEREOF; USE OF SINGLE SUBSTANCES AS EXPLOSIVES
- C06B25/00—Compositions containing a nitrated organic compound
- C06B25/18—Compositions containing a nitrated organic compound the compound being nitrocellulose present as 10% or more by weight of the total composition
Definitions
- the invention relates to a process for the production of shaped nitrocellulose and explosives and fuels according to the preamble of claim 1, a process for the production of an essentially water-free explosive lacquer or an explosive lacquer with a defined water content according to the preamble of claim 8 an explosive paint according to the preamble of claim 10, and a nitrocellulose paint according to the preamble of claim 11.
- explosive includes explosive and / or explosive, in particular solid, liquid and gelatinous substances and
- Explosives are used for numerous applications, particularly in the ammunition sector. As a rule, it is for both efficient and effective
- the explosives have a certain geometry, for example spherical.
- explosive substances for example as propellant charges
- a defined structure and a defined geometry thereof are required, the latter being achievable, for example, by the explosives being present in uniform sizes, preferably as spherical or spheroidal particles.
- Nitrocellulose can be both the explosive described above and a raw material for paint production. Spherical nitrocellulose as a raw material for paint production offers the advantages that it is in this form is also desensitized without moistening agent, is easy to handle and additives may already have been incorporated.
- a disadvantage of this process is that the spheroidal particles formed have a very wide size distribution. In some cases, the proportion of the size range that can be used for an application is only 1/3 of the total mass;
- Another method for producing spherical nitrocellulose particles uses an underwater granulator for the formation of the particles.
- the organic phase is pressed into the aqueous phase through a perforated disk, the strands emerging from the holes in the perforated disk being broken up into particles by a rotating knife on the outlet side. Classification of the spheres formed is also necessary in this method.
- Further disadvantages of this process are that the organic phase for use in the underwater pelletizer has to have such a high consistency that the cylindrical particles which are formed no longer round in the normal stirring process. They must therefore be conveyed through long pipelines with a small cross-section, the rounding taking place through intensive contact with the pipe wall.
- High throughput rates of the device require high rotational speeds of the knife. With the speed of the rotating knife, the hydraulic shear forces increase, which very quickly leads to a reduction in quality due to another cause uncontrolled comminution of the particles. The speed of the cutting knife, which is very limited as a result, considerably limits the performance of the device.
- the particles are hardened by removing the solvent.
- the particles produced by both processes still contain undefined quantities of dispersed water, which causes an undefined porosity in the finished grain.
- this is a decisive quality feature of the product, since the porosity has a decisive influence on the burn-up of the product.
- the object of the invention is accordingly to provide a method and a substance for the production of shaped explosives, by means of which the aforementioned disadvantages, in particular porosity, water and salt content, inconsistent grain size and the environmentally relevant aspects are avoided.
- This object is achieved in each case by a method according to patent claims 1 and 8, by using an explosive lacquer according to patent claim 10 and by a nitrocellulose / explosive lacquer according to patent claim 11.
- propellant charge powder such as spheroidal propellant charge powder, made from an explosive, in particular desensitized with water, has the following steps:
- An essential point of the invention is that by removing the desensitizing substance, in particular water, from the mixture, it is possible to form the explosive particles without having to fear inclusion of a desensitizing substance.
- the desensitizing substance in particular water
- azeotropic distillation This allows the water to be removed from the explosive both efficiently and effectively and safely, particularly with the aid of pervaporation / vapor permeation.
- the solvent is returned to the explosive during and / or after the distillation.
- Suitable auxiliaries are, for example, surface-active substances, wetting agents or release agents.
- the desensitizing substance is a solid, a salt or another substance which is difficult to distill, it is provided according to the invention that it is extracted with suitable solvents.
- Solid phase extraction or precipitation for example, is also possible according to the invention, provided that this is compatible with the type of explosive, in particular its density and solubility. Sublimation is also possible, provided that this can be done safely.
- the shaping of nitrocellulose and / or explosive particles is carried out or initiated by means of jet cutting, one jet, preferably a full jet, of an explosive-solvent mixture or one
- Explosive-solvent solution in particular an explosive lacquer, is divided by means of a separating device into jet sections with a defined and / or adjustable length, which fall into a, preferably moving, fluid in which the explosive-solvent mixture, in particular lacquer, is poor and / or essentially insoluble.
- This process is excellently suited for the production of spheroidal particles with approximately the same grain size for processing explosive-solvent mixtures.
- the organic phase of the fluid to be processed, from which the particles are to be produced is pressed out of a nozzle at high speed in the form of a full jet.
- a rotating cutting tool which consists of short, preferably held in a socket outwardly facing wires, which divides the fluid jet into cylindrical segments.
- spherical particles form from these segments due to the surface tension of the fluid, and these particles are collected in a solvent, in particular in water.
- the size of the particles produced is dependent on the nozzle diameter
- One of the main advantages of the invention is that it is ensured by means of jet cutting that only particles with a desired size that can be adjusted by means of the aforementioned parameters can be produced, and also that the explosive particles produced essentially only contain explosive and solvent, however contain no or a precisely defined amount of a desensitizing substance.
- the advantages of the jet cutting process are first discussed:
- the cutting device runs in the air. This means that very high cutting frequencies and high throughputs are possible.
- the cutting tool In contrast to the underwater pelletizer, the cutting tool has no contact with the outlet opening.
- explosive particles with a defined porosity can be produced, the degree of porosity being set, for example, by the introduction of suitable substances, in particular water, into the explosive lacquer.
- suitable substances in particular water
- substances are preferably used which diffuse out of the explosive particle or can be detached and thus leave a cavity in the explosive particle.
- salts or similarly inert substances which remain in solid form in the explosive particle.
- water-containing nitrocellulose is used as the desensitizing explosive and ethyl acetate is used as the solvent.
- This explosive-solvent system is ideal for the production of spherical, water and salt-free nitrocellulose particles, which are particularly suitable for the production of spheroidal propellant powder.
- the object of the invention is achieved by a method for producing an essentially water-free explosive lacquer or an explosive lacquer with a defined water content, in particular nitrocellulose lacquers, from an explosive which has been desensitized, in particular with water, the method following the following Steps comprises:
- the main advantage of this aspect of the invention is that an essentially water-free explosive varnish is suitable for the production of water-free and also salt-free explosive particles, since, according to the method, these consist of a matrix from which the particles are produced before the use of the explosive lacquer. have been removed.
- the solvent for setting a predefined viscosity is returned to the explosive before and / or after the distillation.
- auxiliaries such as, in particular, surface-active substances, wetting agents, release agents and agents for adjusting the viscosity can also be used to adjust the viscosity.
- wetting and / or release agents makes it possible, for example, to optimally match the explosive varnish to the materials with which it comes into contact during the manufacturing process, so that, for example, contamination caused by the explosive sticking to the apparatus and equipment used is minimized is or is completely omitted. Due to the inherent energy content of an explosive, such measures contribute to handling and operational safety in the manufacture of explosives.
- the object is achieved by using an essentially water-free explosive lacquer, in particular a nitrocellulose lacquer, for producing shaped, in particular spherical or spheroidal, explosive substances.
- the object of the invention is achieved by a nitrocellulose lacquer which consists of at least nitrocellulose and a solvent, the nitrocellulose lacquer being essentially water-free.
- the nitrocellulose lacquer has a viscosity which makes it possible, in particular by means of the jet cutting method, to have particles with a predefinable particle size in the range from 0.1 mm to 10 mm, preferably in the range from 0.2 mm to 2 mm and particularly preferably to form in the range of 0.5 mm to 1.0 mm.
- the nitrocellulose lacquer preferably has auxiliaries, in particular surface-active substances, wetting agents or release agents, and agents for adjusting the viscosity.
- the nitrocellulose lacquer is essentially salt-free.
- nitrocellulose ceilulose nitrate with an N content of approx. 12.5%
- 700 grams of nitrocellulose contains approx. 300 grams of water, is in one liter
- the mixture is distilled azeotropically, the distilled azeotrope being dewatered and the ethyl acetate being continuously returned to the distillation.
- the water After the water has been completely removed from the nitrocellulose-ethyl acetate solution, it is subjected to a jet cutting process using cutting wires with a thickness of 0.05 mm
- nitrocellulose cellulose nitrate with an N content of approx. 13.2%
- nitrocellulose cellulose nitrate with an N content of approx. 13.2%
- the mixture is distilled azeotropically, the distilled azeotrope being dewatered and the ethyl acetate being continuously returned to the distillation.
- 100 g of metriol trinitrate dissolved in 200 g of ethyl acetate are added to the mixture.
- the resulting explosive varnish is then fed to the jet cutting process as described above and processed further.
- nitrocellulose cellulose nitrate with an N content of approx. 12.2%
- 700 grams of nitrocellulose contains approx. 300 grams of water in one liter
- the mixture is distilled azeotropically, the distilled azeotrope being dewatered and the ethyl acetate being continuously returned to the distillation.
- 20 g of dibutyl phthalate dissolved in 200 g of ethyl acetate are added to the mixture.
- the resulting nitrocellulose varnish is then fed to the jet cutting process and further processed as previously described.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Processes Of Treating Macromolecular Substances (AREA)
- Paints Or Removers (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
- Cosmetics (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Abstract
Description
Claims
Priority Applications (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR10-2004-7005814A KR20040060942A (ko) | 2001-10-24 | 2002-10-23 | 회전 타원체 형태의 수분이 없는니트로셀룰로스(Nitrocellulose)와폭발물의 제작 |
EP02782986A EP1438274A2 (de) | 2001-10-24 | 2002-10-23 | Herstellung wasserfreier nitrocellulose und explosivstoffe in sphäroider form |
AU2002346869A AU2002346869A1 (en) | 2001-10-24 | 2002-10-23 | Production of water-free nitrocellulose and explosive substances that have a spheroidal shape |
US10/493,367 US20050000610A1 (en) | 2001-10-24 | 2002-10-23 | Production of water-free nitrocellulose and explosive substances that have a spheroidal shape |
ZA2004/02643A ZA200402643B (en) | 2001-10-24 | 2004-04-05 | Production of water-free nitrocellulose and explosive substances that have a spheroidal shape |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE10152396.3 | 2001-10-24 | ||
DE10152396A DE10152396A1 (de) | 2001-10-24 | 2001-10-24 | Herstellung wasserfreier Nitrocellulose und Eyplosivstoffe in sphäroider Form |
Publications (2)
Publication Number | Publication Date |
---|---|
WO2003035581A2 true WO2003035581A2 (de) | 2003-05-01 |
WO2003035581A3 WO2003035581A3 (de) | 2003-12-24 |
Family
ID=7703523
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/EP2002/011850 WO2003035581A2 (de) | 2001-10-24 | 2002-10-23 | Herstellung wasserfreier nitrocellulose und explosivstoffe in sphäroider form |
Country Status (8)
Country | Link |
---|---|
US (1) | US20050000610A1 (de) |
EP (1) | EP1438274A2 (de) |
KR (1) | KR20040060942A (de) |
CN (1) | CN1703385A (de) |
AU (1) | AU2002346869A1 (de) |
DE (1) | DE10152396A1 (de) |
WO (1) | WO2003035581A2 (de) |
ZA (1) | ZA200402643B (de) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE502005001724D1 (de) * | 2005-01-19 | 2007-11-29 | Fuchs Kg Otto | Abschreckunempfindliche Aluminiumlegierung sowie Verfahren zum Herstellen eines Halbzeuges aus dieser Legierung |
CN103553853B (zh) * | 2013-11-01 | 2016-04-20 | 南京理工大学 | 水溶性氧化剂在含能复合材料中的原位超细化分散方法 |
Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE701493C (de) * | 1936-01-07 | 1941-01-18 | Western Cartridge Company | Rauchloses Pulver und Verfahren zu dessen Herstellung |
GB746705A (en) * | 1952-01-24 | 1956-03-21 | Olin Mathieson | Improvements in or relating to the production of spherical grained propellent powders |
GB792848A (en) * | 1954-10-04 | 1958-04-02 | Olin Mathieson | Improvements in or relating to process and apparatus for the manufacture of propellent powder |
US2982643A (en) * | 1958-07-23 | 1961-05-02 | Olin Mathieson | Nitrocellulose |
US3723207A (en) * | 1970-10-23 | 1973-03-27 | Us Navy | Process for preparing stable essentially water-free slurries of nitrocellulose and products thereof |
US4031172A (en) * | 1975-01-27 | 1977-06-21 | The United States Of America As Represented By The Secretary Of The Army | Process for preparing nitrocellulose for use in small arms |
WO2000048722A1 (de) * | 1999-02-17 | 2000-08-24 | Vorlop Klaus Dieter | Verfahren und vorrichtung zur herstellung von festen teilchen aus einem flüssigen medium |
EP1031547A1 (de) * | 1999-02-23 | 2000-08-30 | Primex Technologies, Inc. | Perforierter Treibstoff und Verfahren zu seiner Herstellung |
Family Cites Families (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
BE652163A (de) * | 1963-08-27 | 1900-01-01 | ||
DE1203652B (de) * | 1964-02-18 | 1965-10-21 | Wolff & Co Ag | Verfahren zur Herstellung gelatinierter Nitrocellulose |
US3702353A (en) * | 1970-09-24 | 1972-11-07 | Us Navy | Continuous process for manufacturing small particle nitrocellulose |
GB2067568B (en) * | 1979-12-28 | 1984-05-31 | Asahi Chemical Ind | Nitrocellulose composition and process for production thereof |
JPS5790001A (en) * | 1980-11-22 | 1982-06-04 | Daicel Chem Ind Ltd | Production of anhydrous nitrocellulose dope |
DE3139840A1 (de) * | 1981-10-07 | 1983-04-21 | Wolff Walsrode Ag, 3030 Walsrode | Zaehfluessiges cellulosehaltiges gemisch (paste) und verfahren zur herstellung von waessriger ueberzugsemulsion aus diesem |
DE3639431A1 (de) * | 1986-11-18 | 1988-05-26 | Basf Lacke & Farben | Waessriges ueberzugsmittel auf der basis von nitrocellulose, verfahren zu seiner herstellung sowie seine verwendung, insbesondere zur beschichtung von holz, folien und papier |
DE19936634A1 (de) * | 1999-08-04 | 2001-02-15 | Wolff Walsrode Ag | Cellulose-Substanz-enthaltendes Überzugsmittel sowie dessen Verwendung in Lacken |
US6136112A (en) * | 1999-10-26 | 2000-10-24 | Trw Inc. | Smokeless gas generating composition for an inflatable vehicle occupant protection device |
-
2001
- 2001-10-24 DE DE10152396A patent/DE10152396A1/de not_active Withdrawn
-
2002
- 2002-10-23 AU AU2002346869A patent/AU2002346869A1/en not_active Abandoned
- 2002-10-23 KR KR10-2004-7005814A patent/KR20040060942A/ko not_active Application Discontinuation
- 2002-10-23 EP EP02782986A patent/EP1438274A2/de not_active Withdrawn
- 2002-10-23 WO PCT/EP2002/011850 patent/WO2003035581A2/de not_active Application Discontinuation
- 2002-10-23 US US10/493,367 patent/US20050000610A1/en not_active Abandoned
- 2002-10-23 CN CNA028208064A patent/CN1703385A/zh active Pending
-
2004
- 2004-04-05 ZA ZA2004/02643A patent/ZA200402643B/en unknown
Patent Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE701493C (de) * | 1936-01-07 | 1941-01-18 | Western Cartridge Company | Rauchloses Pulver und Verfahren zu dessen Herstellung |
GB746705A (en) * | 1952-01-24 | 1956-03-21 | Olin Mathieson | Improvements in or relating to the production of spherical grained propellent powders |
GB792848A (en) * | 1954-10-04 | 1958-04-02 | Olin Mathieson | Improvements in or relating to process and apparatus for the manufacture of propellent powder |
US2982643A (en) * | 1958-07-23 | 1961-05-02 | Olin Mathieson | Nitrocellulose |
US3723207A (en) * | 1970-10-23 | 1973-03-27 | Us Navy | Process for preparing stable essentially water-free slurries of nitrocellulose and products thereof |
US4031172A (en) * | 1975-01-27 | 1977-06-21 | The United States Of America As Represented By The Secretary Of The Army | Process for preparing nitrocellulose for use in small arms |
WO2000048722A1 (de) * | 1999-02-17 | 2000-08-24 | Vorlop Klaus Dieter | Verfahren und vorrichtung zur herstellung von festen teilchen aus einem flüssigen medium |
EP1031547A1 (de) * | 1999-02-23 | 2000-08-30 | Primex Technologies, Inc. | Perforierter Treibstoff und Verfahren zu seiner Herstellung |
Non-Patent Citations (1)
Title |
---|
DATABASE WPI Section Ch, Week 198228 Derwent Publications Ltd., London, GB; Class A11, AN 1982-58152E XP002237897 & JP 57 090001 A (DAICEL CHEM INDS LTD), 4. Juni 1982 (1982-06-04) * |
Also Published As
Publication number | Publication date |
---|---|
CN1703385A (zh) | 2005-11-30 |
DE10152396A1 (de) | 2003-05-15 |
US20050000610A1 (en) | 2005-01-06 |
ZA200402643B (en) | 2005-01-26 |
EP1438274A2 (de) | 2004-07-21 |
KR20040060942A (ko) | 2004-07-06 |
AU2002346869A1 (en) | 2003-05-06 |
WO2003035581A3 (de) | 2003-12-24 |
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