WO1986005175A1 - Process for the manufacture of combustible moulded ammunition components - Google Patents
Process for the manufacture of combustible moulded ammunition components Download PDFInfo
- Publication number
- WO1986005175A1 WO1986005175A1 PCT/EP1986/000110 EP8600110W WO8605175A1 WO 1986005175 A1 WO1986005175 A1 WO 1986005175A1 EP 8600110 W EP8600110 W EP 8600110W WO 8605175 A1 WO8605175 A1 WO 8605175A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- nitrocellulose
- combustible
- hot
- raw
- felts
- Prior art date
Links
Classifications
-
- 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
- C06B21/0041—Shaping the mixture by compression
-
- 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
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F42—AMMUNITION; BLASTING
- F42B—EXPLOSIVE CHARGES, e.g. FOR BLASTING, FIREWORKS, AMMUNITION
- F42B5/00—Cartridge ammunition, e.g. separately-loaded propellant charges
- F42B5/02—Cartridges, i.e. cases with charge and missile
- F42B5/18—Caseless ammunition; Cartridges having combustible cases
- F42B5/188—Manufacturing processes therefor
Definitions
- Combustible molded ammunition parts are increasingly used as propellant charge containers or cartridge cases in tank cannons and field howitzers.
- Such molded parts consist of cellulose and one or more energy sources such as nitrocellulose, hexogen or octogen.
- Flammable molded parts made of cellulose and nitrocellulose have e.g. proven to be useful.
- the ratio of the proportion of cellulose to the proportion of nitrocellulose depends on the demands placed on the molded parts in terms of strength and combustion behavior.
- the ammunition moldings contain a binding resin to achieve sufficient strength.
- the molded parts can be produced in a known manner of operation in such a way that suction molds are immersed in aqueous pulps of a suitable concentration or rotating suction molds are supplied with pulps to form raw felts which are compressed and dried in hot presses. Depending on the selected production method, raw felts can be produced in a uniform or zone-wise different composition.
- the binder resins can be introduced into the raw felts via the aqueous pulps or by immersing the pressed molded parts in a manner known per se.
- binder resin has been introduced into the molded parts in order to achieve a usable strength of the molded parts.
- the binder resins significantly reduce the heat of explosion of the combustible material, the combustibility of the molded parts is impaired by the binder resin content. 10% resin content lower e.g. the heat of explosion of the combustible material around 150 - 220 cal / g.
- PVN polyvinyl nitrate
- the heat of explosion from PVN is 1180 cal / g
- the conditions when hot pressing the raw felts can be selected so that that a binding resin effect is achieved by PVN.
- the press temperatures are advantageously kept between 100-120 ° C.
- the optimum pressing times are to be determined in tests depending on the raw felt thickness and the PVN content; they are usually between 5 and 8 minutes.
- Flammable molded parts are obtained through PVN installation, the strength values of which are considerably higher than those with 12% binding resins.
- the PVN can be introduced into the raw felt as fine-grained material or fiber via the aqueous pulps.
- ⁇ PVN can contain the nitrocellulose in the flammable
- compositions contain e.g. a share in
- a raw felt of the following composition, calculated on dry substance, is produced in a known manner via an appropriately composed aqueous pulp.
- a raw felt of the following composition, calculated on dry substance, is produced in a known manner via an appropriately composed aqueous pulp.
- bleached cellulose 40% polyvinyl nitrate, fibers 30%
- a raw felt with three zones of different composition is produced in a known manner via three correspondingly composed pulps.
- the three zones when converted to dry matter, have the following compositions:
- Zone 1 Zone 2 Zone 3 unbleached pulp 50% 60% 65% polyvinyl nitrate, fibers 25% 30% 34.5% nitrocellulose, 13.25% N t, 24.5% 9.5% -
- the zone-wise different composition was chosen for this molded part, a cartridge case with a firmly attached projectile, on the one hand to ensure the required mechanical strength on the projectile side in zone 3 and on the other hand to ensure sufficient combustion behavior on the weapon breech side in zone 1.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Manufacturing & Machinery (AREA)
- General Engineering & Computer Science (AREA)
- Crystallography & Structural Chemistry (AREA)
- Paper (AREA)
Abstract
In a process for the manufacture of combustible moulded ammunition components of felted and hot-pressed fibre material, manufactured of cellulose, polyvinylchloride and, as the case may be, of nitrocellulose, the raw felts are pressed for densification and drying at temperatures at which polyvinylnitrate softens.
Description
B e s c h r e i b u n gDescription
Verfahren zum Herstellen von brennbaren Munitionsform¬ teilen.Process for producing combustible ammunition parts.
Brennbare Munitionsformteile werden als Treibladungs¬ behälter oder Kartuschhülsen in steigendem Maße in Panzerkanonen und Feldhaubitzen eingesetzt. Derartige Formteile bestehen aus Zellstoff und einem oder mehre- ren Energieträgern wie Nitrozellulosen, Hexogen oder Oktogen. Brennbare Formteile aus Zellstoff und Nitro¬ zellulosen haben sich z.B. als gut brauchbar erwiesen.Combustible molded ammunition parts are increasingly used as propellant charge containers or cartridge cases in tank cannons and field howitzers. Such molded parts consist of cellulose and one or more energy sources such as nitrocellulose, hexogen or octogen. Flammable molded parts made of cellulose and nitrocellulose have e.g. proven to be useful.
Das Verhältnis des Zellstoffanteils zum Nitrozellulo- seanteil ist abhängig von den Forderungen, die an die Formteile in bezug auf Festigkeit und Abbrandverhal- ten gestellt werden.The ratio of the proportion of cellulose to the proportion of nitrocellulose depends on the demands placed on the molded parts in terms of strength and combustion behavior.
Neben Zellstoff und Nitrozellulosen enthalten die Muni- tionsformteile zur Erreichung einer ausreichenden Fe¬ stigkeit ein Bindeharz. Die Herstellung der Formteile kann in bekannter Arbeitsweise so geschehen, daß Saug¬ formen in wässrige Pulpen geeigneter Konzentration tauchen oder rotierenden Saugformen Pulpen zugeführt werden zur Ausbildung von Rohfilzen, die in Heißpressen verdichtet und getrocknet werden. In Abhängigkeit von der gewählten Herstellungsweise können Rohfilze einheit¬ licher oder zonenweise unterschiedlicher Zusammenset¬ zung hergestellt werden.
Die Bindeharze können über die wässrigen Pulpen in die Rohfilze oder durch Tauchtränkung der gepreßten Formteile in an sich bekannter Arbeitsweise eingebracht werden.In addition to cellulose and nitrocellulose, the ammunition moldings contain a binding resin to achieve sufficient strength. The molded parts can be produced in a known manner of operation in such a way that suction molds are immersed in aqueous pulps of a suitable concentration or rotating suction molds are supplied with pulps to form raw felts which are compressed and dried in hot presses. Depending on the selected production method, raw felts can be produced in a uniform or zone-wise different composition. The binder resins can be introduced into the raw felts via the aqueous pulps or by immersing the pressed molded parts in a manner known per se.
Es hat sich als allgemein notwendig erwiesen, daß ca. 15 % Bindeharz in die Formteile eingebracht werden müssen, um eine brauchbare Festigkeit der Formteile zu erzielen.It has proven to be generally necessary that approx. 15% binder resin has to be introduced into the molded parts in order to achieve a usable strength of the molded parts.
Da die Bindeharze die Explosionswärme des brennbaren Materials nennenswert erniedrigen, wird die Brennbar¬ keit der Formteile durch den Bindeharzgehalt verschlech¬ tert. 10 % Harzanteil erniedrigen z.B. die Explosions- wärme des brennbaren Materials um 150 - 220 cal/g.Since the binder resins significantly reduce the heat of explosion of the combustible material, the combustibility of the molded parts is impaired by the binder resin content. 10% resin content lower e.g. the heat of explosion of the combustible material around 150 - 220 cal / g.
Um die Brennbarkeit der Formteile nicht zu stark durch den Bindeharzgehalt zu mindern, muß oft ein Kompromiß zwischen erwünschter Festigkeit und notwendiger Brenn- barkeitsreserve in Kauf genommen werden.In order not to reduce the flammability of the molded parts too much by the binder resin content, a compromise between the desired strength and the necessary flammability reserve must often be accepted.
Es wurde nun überraschenderweise ein Weg gefunden der diese Schwierigkeit in technisch einfacher Weise da¬ durch löst, daß ein Energieträger über die Pulpe in den Rohfilz eingebracht wird, der als Bindeharz wirkt. Diese zwei Funktionen, einerseits Einergieträger und andererseits Bindeharz zu sein, können durch Polyvinyl- nitrat (PVN) erfüllt werden.Surprisingly, a way has now been found that solves this difficulty in a technically simple manner by introducing an energy source via the pulp into the raw felt, which acts as a binder resin. These two functions, on the one hand to be an energy carrier and on the other hand to be binding resin, can be fulfilled by polyvinyl nitrate (PVN).
Die Explosionswärme von PVN beträgt 1180 cal/gThe heat of explosion from PVN is 1180 cal / g
(= 4941 KJ/Kg); sie ist der von hochnitrierter Nitro¬ zellulose vergleichbar.(= 4941 KJ / Kg); it is comparable to that of highly nitrated nitrocellulose.
Da PVN bei 40 - 50 °C plastisch wird, können die Bedin- gungen beim Heißpressen der Rohfilze so gewählt werden,
daß eine Bindeharzwirkung durch PVN erreicht wird. Die Pressentemperaturen werden vorteilhaft zwischen 100 - 120 °C gehalten. Die optimalen Preßzeiten sind in Abhängigkeit von der Rohfilzdicke und dem PVN-Gehalt in Versuchen zu ermitteln; sie betragen üblicherweise zwischen 5 bis 8 Minuten.Since PVN becomes plastic at 40 - 50 ° C, the conditions when hot pressing the raw felts can be selected so that that a binding resin effect is achieved by PVN. The press temperatures are advantageously kept between 100-120 ° C. The optimum pressing times are to be determined in tests depending on the raw felt thickness and the PVN content; they are usually between 5 and 8 minutes.
Durch PVN Einbau werden brennbare Formteile erhalten, deren Festigkeitswerte erheblich über denen mit 12 % Bin- deharzen liegen.Flammable molded parts are obtained through PVN installation, the strength values of which are considerably higher than those with 12% binding resins.
Das PVN kann als feinkörniges Material oder Faser über die wässrigen Pulpen in den Rohfilz eingebracht werden. α PVN kann den Nitrozelluloseanteil in den brennbarenThe PVN can be introduced into the raw felt as fine-grained material or fiber via the aqueous pulps. α PVN can contain the nitrocellulose in the flammable
Formteilen vollständig ersetzen, so daß die Formteile aus Zellstoff und PVN bestehen.Replace molded parts completely so that the molded parts consist of cellulose and PVN.
Um neben hoher Festigkeit optimale Brennbarkeit der Formteile sicherzustellen, ist es oft zweckmäßig gewis¬ se Anteile von Nitrozellulosen in den Formteilen zu belassen. Hierbei ist zu beachten, daß steigender Ge¬ halt an PVN die Materialfestigkeit und steigender Ge¬ halt an Nitrozellulosen die Brennbarkeit erhöht.In order to ensure optimum flammability of the molded parts in addition to high strength, it is often expedient to leave certain proportions of nitrocellulose in the molded parts. It should be noted here that increasing PVN content increases the material strength and increasing nitrocellulose content increases the flammability.
Vorteilhafte Zusammensetzungen enthalten z.B. einen Anteil anAdvantageous compositions contain e.g. a share in
Zellstoff von 40 Gew. % PVN 30 bis 50 Gew. %Pulp from 40% by weight PVN 30 to 50% by weight
Nitrozellulose 30 bis 10 Gew. %Nitrocellulose 30 to 10% by weight
Die folgenden Beispiele erläutern die erfindungsgemäße Arbeitsweise in ihren Möglichkeiten, bedeuten jedoch keine Begrenzung auf Zusammensetzung oder Durchführungs¬ weise.
Beispiele:The following examples explain the method of operation according to the invention in its possibilities, but do not mean any limitation to the composition or method of implementation. Examples:
Beispiel 1example 1
Über eine entsprechend zusammengesetzte wässrige Pulpe wird in bekannter Weise ein Rohfilz folgender, auf Trockensubstanz berechneter Zusammensetzung herge- stellt.A raw felt of the following composition, calculated on dry substance, is produced in a known manner via an appropriately composed aqueous pulp.
ungebleichter Zellstoff: 40 %unbleached pulp: 40%
Polyvinylnitrat, gemahlen: 40 %Polyvinyl nitrate, ground: 40%
Nitrozellulose, 12,6 % N„: 19 % Stabilisator, Centralit: 1 %Nitrocellulose, 12.6% N ": 19% stabilizer, Centralit: 1%
Nach Verdichtung des Rohfilzes über 4 Minuten in einer 130 °C heißen Presse wurde eine Hülse folgender Mate¬ rialeigenschaften erhalten:After the raw felt was compacted for 4 minutes in a hot press at 130 ° C., a sleeve with the following material properties was obtained:
Wandstärke: 1,7 mmWall thickness: 1.7 mm
3 Dichte: 1,56 g/cm 3 Density: 1.56 g / cm
Zugfestigkeit: 420 barTensile strength: 420 bar
Explosionswärme: 2190 Joule/g Abbrandverhalten: 20 m/secExplosive heat: 2190 Joule / g combustion behavior: 20 m / sec
Beispiel 2:Example 2:
Über eine entsprechend zusammengesetzte wässrige Pulpe wird in bekannter Weise ein Rohfilz folgender, auf Trockensubstanz berechneter, Zusammensetzung herge¬ stellt.
gebleichter Zellstoff 40 % Polyvinylnitrat, Fasern 30 %A raw felt of the following composition, calculated on dry substance, is produced in a known manner via an appropriately composed aqueous pulp. bleached cellulose 40% polyvinyl nitrate, fibers 30%
Nitrozellulose, 13,25 % N _, 29 %Nitrocellulose, 13.25% N _, 29%
Stabilisator, Akardit 1 %Stabilizer, acardite 1%
Nach Verdichtung des Rohfilzes über 4 Minuten in einer 1 13300 °CC hheeiißßeenn PPrreessssee wwuurrddee eine Hülse folgender Mate- rialeigenschaften erhaltenAfter compacting the raw felt for 4 minutes in a 1 13300 ° CC high-heat PPrreessssee wwuurrddee, obtain a sleeve with the following material properties
Wandstärke 1,8 mm Dichte 1,62 g/cmWall thickness 1.8 mm, density 1.62 g / cm
Zugfestigkeit 492 bar Explosionswärme 2161 Joule/g Abbrandverhalten 12 m/secTensile strength 492 bar explosion heat 2161 Joule / g combustion behavior 12 m / sec
Über drei entsprechend zusammengesetzte Pulpen wird in bekannter Weise ein Rohfilz mit drei Zonen unter¬ schiedlicher Zusammensetzung hergestellt. Die drei Zonen haben, auf Trockensubstanz umgerechnet, folgende Zusammensetzungen:A raw felt with three zones of different composition is produced in a known manner via three correspondingly composed pulps. The three zones, when converted to dry matter, have the following compositions:
Zone 1 Zone 2 Zone 3 ungebleichter Zellstoff 50 % 60 % 65 % Polyvinylnitrat, Fasern 25 % 30 % 34,5 % Nitrozellulose, 13,25 % N t, 24,5 % 9,5 % -Zone 1 Zone 2 Zone 3 unbleached pulp 50% 60% 65% polyvinyl nitrate, fibers 25% 30% 34.5% nitrocellulose, 13.25% N t, 24.5% 9.5% -
Stabilisator, Akardit 0,5 % 0,5 % 0,5 %Stabilizer, acardite 0.5% 0.5% 0.5%
Nach Verdichtung des Rohfilzes über 4 Minuten in einer 130 °C heißen Presse wurde ein Formteil folgender Mate¬ rialeigenschaften erhalten:
Zone 1 Zone 2 ZoneAfter compacting the raw felt in a hot press at 130 ° C. for 4 minutes, a molded part with the following material properties was obtained: Zone 1 Zone 2 Zone
Wandstärke mm 1,52 1 ,52 1 ,53Wall thickness mm 1.52 1, 52 1, 53
Dichte g/cm3 1 ,62 1 ,58 1 ,53Density g / cm3 1, 62 1, 58 1, 53
Zugfestigkeit bar 566 579 603Tensile strength bar 566 579 603
Explosionswärme Joule/g 1800 1441 1243Heat of explosion Joule / g 1800 1441 1243
Abbrandverhalten m/sec 14 26 34,8Burning behavior m / sec 14 26 34.8
Die zonenweise unterschiedliche Zusammensetzung wurde für dieses Formteil eine Kartuschhülse mit festverbunde¬ nem Projektil gewählt, um einerseits zur Projektilseite in Zone 3 die geforderte mechanische Festigkeit und andererseits zur Waffenverschlußseite in der abbrandkri- tischen Zone 1 ein ausreichendes Abbrandverhalten zu sichern.
The zone-wise different composition was chosen for this molded part, a cartridge case with a firmly attached projectile, on the one hand to ensure the required mechanical strength on the projectile side in zone 3 and on the other hand to ensure sufficient combustion behavior on the weapon breech side in zone 1.
Claims
1.1.
Verfahren zur Herstellung brennbarer Munitionsformteile aus verfilzten, und heißgepreßtem Fasermaterial alsProcess for the production of combustible ammunition parts from felted, and hot-pressed fiber material as
Stoffbasis, dadurch gekennzeichnet, daß die Rohfilze aus Zellstoff und Polyvinylnitrat gegenbenenfalls unter Zusatz von Nitrozellulosen hergestellt werden und die Rohfilze zur Verdichtung und Trocknung bei Temperaturen verpreßt werden, bei denen das Polyvinylnitrat erweicht.Fabric base, characterized in that the raw felts are made from cellulose and polyvinyl nitrate, optionally with the addition of nitrocellulose, and the raw felts are compressed for compression and drying at temperatures at which the polyvinyl nitrate softens.
2.Second
Verfahren nach Anspruch 1, dadurch gekennzeichnet, daß der Nitrozelluloseanteil bis 90 % des Energieträ- gers:A method according to claim 1, characterized in that the nitrocellulose content up to 90% of the energy source:
Polyvinylnitrat + Nitrozellulose beträgt.Is polyvinyl nitrate + nitrocellulose.
3.3rd
Verfahren nach Anspruch 2, dadurch gekennzeichnet, daß der Nitrozelluloseanteil 30 - 50 % des Energieträ¬ gers: Polyvinylnitrat + Nitrozellulose beträgt.A method according to claim 2, characterized in that the nitrocellulose content is 30-50% of the energy carrier: polyvinyl nitrate + nitrocellulose.
4. Verfahren nach einem der Ansprüche 1 - 3, dadurch ge¬ kennzeichnet, daß das Verpressen der wasserfeuchten Rohfilze in über 100 °C heißen Pressen geschieht. 4. The method according to any one of claims 1-3, characterized ge indicates that the pressing of the water-moist raw felts takes place in presses hot above 100 ° C.
5.5th
Verfahren nach Anspruch 4, dadurch gekennzeichnet, daß das Verpressen der wasserfeuchten Rohfilze in 110Method according to claim 4, characterized in that the pressing of the water-moist raw felts in 110
- 130 C heißen Pressen geschieht.- 130 C hot presses happens.
6.6th
Verfahren nach einem der Ansprüche 1 bis 5, dadurch gekennzeichnet, daß die Preßlinge zu Munitionsformtei¬ len wie Kartuschhülsen, Treibladungsbehälter, Anzünd¬ rohre o.dgl. verarbeitet bzw. zusammengesetzt werden. Method according to one of claims 1 to 5, characterized in that the compacts to form ammunition such as cartridge cases, propellant charge containers, ignition tubes or the like. processed or assembled.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE3507797 | 1985-03-05 | ||
DEP3507797.2 | 1985-03-05 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO1986005175A1 true WO1986005175A1 (en) | 1986-09-12 |
Family
ID=6264275
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/EP1986/000110 WO1986005175A1 (en) | 1985-03-05 | 1986-03-04 | Process for the manufacture of combustible moulded ammunition components |
Country Status (2)
Country | Link |
---|---|
EP (1) | EP0218614A1 (en) |
WO (1) | WO1986005175A1 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2672381A1 (en) * | 1985-10-01 | 1992-08-07 | Dynamit Nobel Ag | AMMUNITION WITHOUT SOCKET. |
EP1319919A1 (en) * | 2001-12-15 | 2003-06-18 | Nitrochemie Aschau GmbH | Process for manufacturing a combustible cartridge case for ammunition |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1036137B (en) * | 1944-09-09 | 1958-08-07 | Wasagchemie Ag | Process for the production of shaped explosive bodies of high strength |
FR2210589A1 (en) * | 1972-12-14 | 1974-07-12 | Poudres & Explosifs Ste Nale | |
DE2436743B2 (en) * | 1973-08-09 | 1977-01-27 | Societe Nationale Des Poudres Et Explosifs, Paris | THERMOPLASTIC COMPOSITION ON A POLYVINYL NITRATE BASE |
-
1986
- 1986-03-04 WO PCT/EP1986/000110 patent/WO1986005175A1/en unknown
- 1986-03-04 EP EP19860901843 patent/EP0218614A1/en not_active Withdrawn
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1036137B (en) * | 1944-09-09 | 1958-08-07 | Wasagchemie Ag | Process for the production of shaped explosive bodies of high strength |
FR2210589A1 (en) * | 1972-12-14 | 1974-07-12 | Poudres & Explosifs Ste Nale | |
DE2436743B2 (en) * | 1973-08-09 | 1977-01-27 | Societe Nationale Des Poudres Et Explosifs, Paris | THERMOPLASTIC COMPOSITION ON A POLYVINYL NITRATE BASE |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2672381A1 (en) * | 1985-10-01 | 1992-08-07 | Dynamit Nobel Ag | AMMUNITION WITHOUT SOCKET. |
EP1319919A1 (en) * | 2001-12-15 | 2003-06-18 | Nitrochemie Aschau GmbH | Process for manufacturing a combustible cartridge case for ammunition |
US6910422B2 (en) | 2001-12-15 | 2005-06-28 | Nitrochemie Aschau Gmbh | Method for producing a combustible cartridge case for cartridge ammunition |
Also Published As
Publication number | Publication date |
---|---|
EP0218614A1 (en) | 1987-04-22 |
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