EP2602238B1 - Nicht toxische perkussionszünder und verfahren zu ihrer herstellung - Google Patents

Nicht toxische perkussionszünder und verfahren zu ihrer herstellung Download PDF

Info

Publication number
EP2602238B1
EP2602238B1 EP13157579.7A EP13157579A EP2602238B1 EP 2602238 B1 EP2602238 B1 EP 2602238B1 EP 13157579 A EP13157579 A EP 13157579A EP 2602238 B1 EP2602238 B1 EP 2602238B1
Authority
EP
European Patent Office
Prior art keywords
explosive
nano
mixture
buffer
combining
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.)
Active
Application number
EP13157579.7A
Other languages
English (en)
French (fr)
Other versions
EP2602238A3 (de
EP2602238A2 (de
Inventor
Jack Erickson
Joel Sandstrom
Gene Johnston
Neal Norris
Patrick Braun
Reed Blau
Lisa Liu
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.)
Vista Outdoor Operations LLC
Original Assignee
Vista Outdoor Operations LLC
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 Vista Outdoor Operations LLC filed Critical Vista Outdoor Operations LLC
Priority to EP13157579.7A priority Critical patent/EP2602238B1/de
Publication of EP2602238A2 publication Critical patent/EP2602238A2/de
Publication of EP2602238A3 publication Critical patent/EP2602238A3/de
Application granted granted Critical
Publication of EP2602238B1 publication Critical patent/EP2602238B1/de
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • C—CHEMISTRY; METALLURGY
    • C06—EXPLOSIVES; MATCHES
    • C06C—DETONATING OR PRIMING DEVICES; FUSES; CHEMICAL LIGHTERS; PYROPHORIC COMPOSITIONS
    • C06C7/00—Non-electric detonators; Blasting caps; Primers
    • C—CHEMISTRY; METALLURGY
    • C06—EXPLOSIVES; MATCHES
    • C06B—EXPLOSIVES OR THERMIC COMPOSITIONS; MANUFACTURE THEREOF; USE OF SINGLE SUBSTANCES AS EXPLOSIVES
    • C06B23/00—Compositions characterised by non-explosive or non-thermic constituents
    • C06B23/006—Stabilisers (e.g. thermal stabilisers)
    • C—CHEMISTRY; METALLURGY
    • C06—EXPLOSIVES; MATCHES
    • C06B—EXPLOSIVES OR THERMIC COMPOSITIONS; MANUFACTURE THEREOF; USE OF SINGLE SUBSTANCES AS EXPLOSIVES
    • C06B33/00—Compositions containing particulate metal, alloy, boron, silicon, selenium or tellurium with at least one oxygen supplying material which is either a metal oxide or a salt, organic or inorganic, capable of yielding a metal oxide

Definitions

  • the present invention relates to a method of making a percussion primer composition for explosive systems.
  • Ignition devices rely on the sensitivity of the primary explosive that significantly limits available primary explosives.
  • the most common lead styphnate alternative, diazodinitrophenol (DDNP or dinol) has been used for several decades relegated to training ammunition, DDNP-based primers suffer from poor reliability that may be attributed to low friction sensitivity, low flame temperature, and are hygroscopic.
  • Metastable interstitial composites also known as metastable nanoenergetic composites (MNC) or superthermites
  • MNC metastable nanoenergetic composites
  • These materials have shown excellent performance characteristics, such as impact sensitivity and high temperature output.
  • the main difficulty is handling of dry nano-size powder mixtures due to their sensitivity to friction and electrostatic discharge (ESD). See U.S. Patent No. 5717159 and U.S. Patent Publication No. 2006/0113014 .
  • Health concerns may be further compounded by the use of barium and lead containing oxidizers. See, for example, U.S. Patent Publication No. 20050183805 .
  • US2006113014A1 discloses a method for preparing metastable nanoenergetic composites (MNC) and for wet loading those MNCs into percussion primer cups.
  • US4133707A discloses an extrudable ammunition priming mix with viscosity characteristics which remain relatively stable over an extended time span.
  • EP0334725A1 discloses new percussive primer charges and a process for their manufacture.
  • DE19606237A1 discloses a non-toxic detonator composition for light weapon munitions free of lead and barium.
  • EP1195366A discloses a non-toxic primer mix including both bismuth sulfide and potassium nitrate as the pyrotechnic portion of the primer.
  • WO9944968A1 discloses a non-toxic primer composition for use in ammunition with a hygroscopic oxidizer which is protected from absorption of water.
  • US6544363B1 discloses a non-toxic heavy-metal-free priming mix and a method of forming the same.
  • EP0699646A1 discloses a priming mixture containing no toxic materials, in particular no Pb, Ba or Sb compounds, and presenting at least one primary explosive, an oxidizing agent, a reducing agent, and an inert friction agent; the oxidizing agent comprising stannic oxide SnO 2 .
  • WO2006009579A2 discloses a primer for small arms ammunition including a primary explosive and an oxidizer system containing bismuth oxide.
  • US2006219341A1 discloses a sensitized explosive that comprises an explosive precipitated onto a sensitizer.
  • WO2006083379A2 discloses nanoenergetic materials based on aluminum and bismuth oxide.
  • US3367805A discloses thickened inorganic nitrate aqueous slurry containing finely divided aluminum having a lyophobic surface of high surface area.
  • US3113059A discloses an inhibited aluminum-water composition and method.
  • WO9612770A discloses a system for inhibiting the corrosion of ferrous and other metals by passivating the metals.
  • WO0206421A discloses reaction mixtures that include exothermic generating particles having a water soluble coating encasing a portion of the particles and, optionally an aqueous solution, and a buffer.
  • DE2513735A1 discloses a corrosion inhibitor for metals in aqueous systems containing polycarboxylic acid, zinc, phosphate, phosphonate or polymer dispersant.
  • the present invention concerns a method of making a percussion primer according to claim 1.
  • Another aspect not forming part of the present invention relates to a method for preparing a percussion primer, the method including providing at least one water wet explosive, combining at least one sensitizer with the at least one water wet explosive, combining at least one nano-size non-coated fuel particle having natural surface oxides thereon with the at least one additional water wet explosive to form a wet mixture, dry blending at least one oxidizer and at least one binder to form a resultant dry blend and adding the dry blend to the water wet mixture and mixing until homogeneous to form a final mixture.
  • a percussion primer composition including at least one explosive, at least one nano-size non-coated fuel particle having natural surface oxides thereon and at least one oxidizer.
  • a percussion primer premixture including at least one explosive, at least one nano-size non-coated fuel particle having surface oxides thereon and water in an amount of about 10 wt-% to about 40 wt-% of the premixture.
  • a primer composition including at least one explosive, at least one non-coated nano-size fuel particle having natural surface oxides thereon, a buffer system including at least one salt of citric acid and at least one salt of phosphoric acid and an oxidizer.
  • a gun cartridge including a casing, a secondary explosive disposed within the casing and a primary explosive disposed within the casing, the primary explosive including at least one primary energetic, at least one nano-size non-coated fuel particle having natural surface oxides thereon and at least one oxidizer.
  • a primer-containing ordinance assembly including a housing, a secondary explosive disposed within the housing and a primary explosive disposed within the housing, the primary explosive including at least one primary energetic, at least one nano-size non-coated fuel particle having natural surface oxides thereon; and at least one oxidizer.
  • percussion primer compositions that include at least one energetic, at least one nano-size non-coated fuel particle having natural surface oxides thereon, and at least one oxidizer.
  • a buffer or mixture of buffers may be employed.
  • a sensitizer for increasing the sensitivity of the primary explosive is added to the primer compositions,
  • the primer mixture creates sufficient heat to allow for the use of moderately active metal oxides that are non-hygroscopic, non-toxic and non-corrosive.
  • the primary energetic is suitably selected from energetics that are relatively insensitive to shock, friction and heat according to industry standards, making processing of these energetics more safe.
  • Some of the relatively insensitive explosives that find utility herein for use as the primary explosive have been categorized generally as a secondary explosive due to their relative insensitivity.
  • Suitable classes of energetics include, but are not limited to, nitrate esters, nitramines, nitroaromatics and mixtures thereof.
  • the energetics suitable for use herein include both primary and secondary energetics in these classes.
  • nitramines examples include, but are not limited to, CL-20, RDX, HMX and nitroguanidine.
  • RDX (royal demolition explosive), hexahydro-1,3,5-trinitro-1,3,5 triazine or 1,3,5-trinitro-1,3,5-triazacyclohexane, may also be referred to as cyclonite, hexagen, or cyclotrimethylenetrinitramine.
  • HMX high melting explosive
  • octahydro-1,3,5,7-tetranitro-1,3,5,7-tetrazocine or 1,3,5,7-tetranitro-1,3,5,7 tetraazacyclooctane (HMX) may also be referred to as cyclotetramethylene-tetranitramine or octagen, among other names.
  • CL-20 is 2,4,6,8,10,12-hexanitrohexaazaisowurtzitane (HNIW) or 2,4,6,8,10,12-hexanitro-2,4,6,8,10,12-hexaazatetracyclo[S.5.0.0 5,9 0 3,11 ]-dodecane,
  • Suitable nitroaromatics include, but are not limited to, tetryl (2,4,6-trinitrophenyl-methylnitramine), TNT (2,4,6-trinitrotoluene), DDNP (diazodinitrophenol or 4',6-dinitrobenzene-2-diazo-1-oxide) and mixtures thereof.
  • nitrate esters examples include, but are not limited to, PETN (pentaerythritoltetranitrate) and nitrocellulose.
  • nitrocellulose is employed. Nitrocellulose, particularly nitrocellulose having a high percentage of nitrogen, for example, greater than about 10 wt-% nitrogen, and having a high surface area, has been found to increase sensitivity. In primers wherein the composition includes nitrocellulose, flame temperatures exceeding those of lead styphnate have been created. In some embodiments, the nitrocellulose has a nitrogen content of about 12.5-13.6% by weight and a particle size of 80-120 mesh.
  • the primary explosive can be of varied particulate size.
  • particle size may range from approximately 0.1 micron to about 100 microns. Blending of more than one size and type can be effectively used to adjust formulation sensitivity.
  • the primary explosive is suitably employed in amounts of about 5% to about 40% by weight. This range may be varied depending on the primary explosive employed.
  • suitable nano-size non-coated fuel particles include, but are not limited to, aluminum, boron, molybdenum, silicon, titanium, tungsten, magnesium, melamine, zirconium, calcium silicide, and mixtures thereof.
  • the size of the fuel particle may vary from about 0.05 microns (50 nm) to about 0.120 microns (about 120 nm), and suitably about 70 nm to about 120 nm.
  • the fuel particle has an average size of greater than 0.05 microns (50 nm), more suitably greater than about 0.070 microns (70 nm) and even more suitably has an average particle size of about 0.1 micron or about 100 nanometers. Keeping the average size fuel particle above about 0.05 microns or 50 nanometers, can significantly improve the safety of processing due to the naturally occurring surface oxides and thicker oxide layer that exist on larger fuel particles. Smaller fuel particles may exhibit higher impact (friction) and shock sensitivities.
  • Very small fuel particles such as those between about 20 nm and 50 nm, can be unsafe to handle. In the presence of oxygen they are prone to autoignition and are thus typically kept solvent wet or coated such as with polytetrafluoroethylene or an organic acid such as oleic acid.
  • the fuel particles have a natural oxide coating.
  • Surface oxides reduce the sensitivity of the fuel particle, and reduce the need to provide any additional protective coating such as a fluoropolymer coating, e.g. polytetrafluoroethylene (PTFE), an organic acid coating or a phosphate based coating to reduce sensitivity and facilitate safe processing of the composition.
  • PTFE polytetrafluoroethylene
  • the natural oxide coating on nano-size particles having a larger average particle size i.e. those having a particle size of about 50 nm to about 120 nm, suitably those having a particle size of about 70 nm to about 120 nm, improves the stability of the particles, which consequently increases the margin of safety for processing and handling, Furthermore, a lower surface area may also decrease hazards while handling the nano-size fuel particles as risk of an electrostatic discharge initiation of the nano-size fuel particles decreases as the surface area decreases.
  • coatings for the protection of the fuel particle may be eliminated due to the increased surface oxides on the larger fuel particles.
  • Alex® nano-aluminum powder having an average particle size of about 100 nanometers (0.1 microns) available from Argonide Nanomaterials in Pittsburgh, PA.
  • the nano-size fuel particles are employed in amounts of about 5% to about 20% by weight of the primer composition.
  • Buffers can be optionally added to the primer compositions to decrease the likelihood of hydrolysis of the fuel particles, which is dependent on both temperature and pH. While single acid buffers may be employed, it has been found that a dual acid buffer system significantly increases the temperature stability of the percussion primer composition. Of course, more than two buffers may be employed as well. For example, it has been found that while a single acid buffer system can increase the temperature at which hydrolysis of the fuel particle occurs to about 120-140° F (about 49°C - 60°C), these temperatures are not sufficient for standard processing of percussion primers that includes oven drying. Therefore, higher hydrolysis onset temperatures are desirable for safe oven drying of the percussion primer compositions.
  • any buffer may be suitably employed herein, it has been found that some buffers are more effective than others for reducing the temperature of onset of hydrolysis.
  • an organic acid and a phosphate salt are employed. More specifically, in some embodiments, a combination of citrate and phosphate are employed. In weakly basic conditions, the dibasic phosphate ion (HPO 4 2- ) and the tribasic citrate ion (C 6 H 5 O 7 3- ) are prevalent. In weakly acid conditions, the monobasic phosphate ion (H 2 PO 4 - ) and the dibasic citrate ion (C 6 H 6 O 7 2- ) are most prevalent.
  • the stability of explosives to both moisture and temperature is desirable for safe handling of firearms.
  • small cartridges are subject to ambient conditions including temperature fluctuations and moisture, and propellants contain small amounts of moisture and volatiles. It is desirable that these loaded rounds are stable for decades, be stable for decades over a wide range of environmental conditions of fluctuating moisture and temperatures.
  • primer compositions according to one or more embodiments not forming part of the invention can be safely stored water wet (25%) for long periods without any measurable affect on the primer sensitivity or ignition capability. In some embodiments, the primer compositions may be safely stored for at least about 5 weeks without any measurable affect on primer sensitivity or ignition capability.
  • the aluminum contained in the percussion primer compositions according to one or more embodiments not forming part of the invention exhibit no exotherms during simulated bulk autoignition tests (SBAT) at temperatures greater than about 200° F (about 93° C), and even greater than about 225° F (about 107° C) when tested as a slurry in water.
  • SBAT simulated bulk autoignition tests
  • additional fuels may be added.
  • a sensitizer may be added to the percussion primer compositions according to one or more embodiments not forming part of the invention. As the particle size of the nano-size fuel particles increases, sensitivity decreases. Thus, a sensitizer may be beneficial. Sensitizers may be employed in amounts of 0% to about 20%, suitably 0% to about 15% by weight and more suitably 0% to about 10% by weight of the composition.
  • a suitable sensitizer includes, but is not limited to, tetracene,
  • the sensitizer may be employed in combination with a friction generator.
  • Friction generators are useful in amounts of about 0% to about 25% by weight of the primer composition.
  • a suitable friction generator includes, but is not limited to, glass powder.
  • Tetracene is suitably employed as a sensitizing explosive while glass powder is employed as a friction generator.
  • Oxidizers may be employed in amounts of about 20% to about 70% by weight of the primer composition.
  • the oxidizers employed herein are moderately active metal oxides, and are non-hygroscopic and are not considered toxic. Examples of oxidizers include, but are not limited to, bismuth oxide, bismuth subnitrate, bismuth tetroxide, bismuth sulfide, zinc peroxide, tin oxide, manganese dioxide, molybdenum trioxide, and combinations thereof.
  • binders may be employed in the primer compositions herein as is known in the art. Both natural and synthetic binders find utility herein. Examples of suitable binders include, but are not limited to, natural and synthetic gums including xanthan, Arabic, tragacanth, guar, karaya, and synthetic polymeric binders such as hydroxypropylcellulose and polypropylene oxide, as well as mixtures thereof. See also U.S. Patent Publication No. 2006/0219341 A1 . Binders may be added in amounts of about 0.1 wt% to about 5 wt-% of the composition, and more suitably about 0.1 wt% to about 1 wt% of the composition.
  • compositions according to one or more embodiments not forming part of the invention may also be employed in the compositions according to one or more embodiments not forming part of the invention.
  • inert fillers, diluents, other binders, low out put explosives, etc. may be optionally added.
  • the primer compositions according to one or more embodiments not forming part of the invention may be processed using simple water processing techniques. Larger fuel particles are safer for handling while maintaining the sensitivity of the assembled primer. It is surmised that this may be attributed to the use of larger fuel particles and/or the dual buffer system. The steps of milling and sieving employed for MIC-MNC formulations may also be eliminated. For at least these reasons, processing of the primer compositions not forming part of the invention is safer.
  • the method of making the primer compositions according to one or more embodiments of the invention includes mixing the primary explosive water wet with at least one nano-size non-coated fuel particle having natural surface oxides thereon to form a first mixture, and adding an oxidizer to the first mixture.
  • the oxidizer may be optionally dry blended with at least one binder to form a second dry mixture, and the second mixture then added to the first mixture and mixing until homogeneous to form a final mixture.
  • water-wet shall refer to a water content of between about 10 wt-% and about 40 wt-%, more suitably about 18% to about 30% and most suitably about 25% by weight.
  • the sensitizer may be added either to the water wet primary explosive, or to the primary explosive/nano-size non-coated fuel particle water wet blend.
  • the sensitizer may optionally further include a friction generator such as glass powder.
  • At least one buffer is added to the process to keep the system acidic and to prevent significant hydrogen evolution and further oxides from forming.
  • a mildly acidic buffer having a pH in the range of about 4-8, suitably 4-7, can help to prevent such hydrolysis. While at a pH of 8, hydrolysis is delayed, by lowering the pH, hydrolysis can be effectively stopped, thus, a pH range of 4-7 is preferable.
  • the buffer solution is added as increased moisture to the primary explosive prior to addition of the non-coated nano-size fuel particle. Furthermore, the nano-size fuel particle may be preimmersed in the buffer solution to further increase handling safety.
  • Simple water mixing methods are used to assemble the percussion primer using standard industry practices and such assembly can be accomplished safely without stability issues.
  • the use of such water processing techniques is beneficial as previous primer compositions such as MIC/MNC primer compositions have limited stability in water.
  • the nano-size fuel particles and the explosive are water-mixed according to one or more embodiments of the invention, maintaining conventional mix methods and associated safety practices.
  • primary oxidizer-fuel formulations when blended with fuels, sensitizers and binders, can be substituted in applications where traditional lead styphnate and diazodinitrophenol (DDNP) primers and igniter formulations are employed.
  • DDNP diazodinitrophenol
  • the heat output of the system is sufficient to utilize non-toxic metal oxidizers of higher activation energy typically employed but under utilized in lower flame temperature DDNP based formulations.
  • Additional benefits of the present invention include improved stability, increased ignition capability, improved ignition reliability, lower final mix cost, and increased safety due to the elimination of lead styphnate production and handling.
  • the present invention finds utility in any igniter or percussion primer application where lead styphnate is currently employed.
  • the percussion primer not forming part of the present invention may be employed for small caliber and medium caliber cartridges, as well as industrial powerloads.
  • compositions and concentration ranges for a variety of different cartridges. Such compositions and concentration ranges are for illustrative purposes only.
  • the nitrocellulose is 30-100 mesh and 12,5-13.6 wt-% nitrogen.
  • the nano-aluminum is sold under the tradename of Alex® and has an average particles size of 0.1 microns.
  • the additional aluminum fuel is 80-120 mesh.
  • Table 1 Illustrative percussion primer compositions for pistol/small rifle. Pistol/Small Rifle Range wt-% Preferred wt-% Nitrocellulose 10-30 20 Nano-Aluminum 8-12 10 Bismuth trioxide 50-70 64.5 Tetracene 0-6 5 Binder 0.3-0.8 0.4 Buffer/stabilizer 0.1-0.5 0.1
  • Table 2 Illustrative percussion primer compositions for large rifle.
  • the percussion primer is used in a centerfire gun cartridge or in a rimfire gun cartridge.
  • a firing pin strikes a rim of a casing of the gun cartridge.
  • the firing pin of small arms using the centerfire gun cartridge strikes a metal cup in the center of the cartridge casing containing the percussion primer.
  • Gun cartridges and cartridge casings are known in the art and, therefore, are not discussed in detail herein.
  • the force or impact of the firing pin may produce a percussive event that is sufficient to detonate the percussion primer in the rimfire gun cartridge or in the centerfire gun cartridge, causing the secondary explosive composition to ignite.
  • FIG. 1A is a longitudinal cross-section of a rimfire gun cartridge shown generally at 6.
  • Cartridge 6 includes a housing 4.
  • Percussion primer 2 may be substantially evenly distributed around an interior volume defined by a rim portion 3 of casing 4 of the cartridge 6 as shown in FIG. 1B which is an enlarged view of an anterior portion of the rimfire gun cartridge 6 shown in FIG. 1A .
  • FIG. 2A is a longitudinal cross-sectional view of a centerfire gun cartridge shown generally at 8.
  • the percussion primer 2 may be positioned in an aperture 10 in the casing 4.
  • FIG. 2B is an enlarged view of aperture 10 in FIG. 2A more clearly showing primer 2 in aperture 10.
  • the propellant composition 12 may be positioned substantially adjacent to the percussion primer 2 in the rimfire gun cartridge 6 or in the centerfire gun cartridge 8.
  • the percussion primer 2 When ignited or combusted, the percussion primer 2 may produce sufficient heat and condensing of hot particles to ignite the propellant composition 12 to propel projectile 16 from the barrel of the firearm or larger caliber ordnance (such as, without limitation, handgun, rifle, automatic rifle, machine gun, any small and medium caliber cartridge, automatic cannon, etc.) in which the cartridge 6 or 8 is disposed.
  • the combustion products of the percussion primer 2 may be environmentally friendly, noncorrosive, and nonabrasive
  • the percussion primer 2 may also be used in larger ordnance, such as (without limitation) grenades, mortars, or detcord initiators, or to initiate mortar rounds, rocket motors, or other systems including a secondary explosive, alone or in combination with a propellant, all of the foregoing assemblies being encompassed by the term "primer-containing ordnance assembly," for the sake of convenience,
  • the percussion primer 2 may be positioned substantially adjacent to a secondary explosive composition 12 in a housing 18, as shown in FIG. 3 .
  • nitrocellulose in an amount of 30 grams was placed water-wet in a mixing apparatus.
  • Water-wet tetracene 5g was added to the mixture and further mixed until the tetracene was not visible.
  • Nano-aluminum powder, 10g was added to the water-wet nitrocellulose/tetracene blend and mixed until homogeneous.
  • Bismuth trioxide 54 g was dry blended with 1 g of gum tragacanth and the resultant dry blend was added to the wet explosive mixture, and the resultant blend was then mixed until homogeneous. The final mixture was removed and stored cool in conductive containers.
  • FIG. 4 is an SBAT graph illustrating the temperature at which hydrolysis begins when Alex® aluminum particles are mixed in water with no buffer.
  • the hydrolysis onset temperature is 118° F (47.8° C). See no. 1 in table 7.
  • FIG. 5 is an SBAT graph illustrating the temperature at which hydrolysis begins using only a single buffer which is citrate.
  • the hydrolysis onset temperature is 140° F (60° C). See no. 11 in table 7.
  • FIG. 6 is an SBAT graph illustrating the temperature at which hydrolysis begins using only a single buffer which is a phosphate buffer.
  • the hydrolysis onset temperature is 129° F (53.9° C).
  • FIG. 7 is an SBAT graph illustrating the temperature at which hydrolysis begins using a dual citrate/phosphate buffer system. Hydrolysis has been effectively stopped at a pH of 5.0 even at temperatures of well over 200° F (about 93° C).
  • the present invention finds utility in any application where lead styphnate based igniters or percussion primers are employed.
  • Such applications typically include an igniter or percussion primer, a secondary explosive, and for some applications, a propellant.
  • other applications include, but are not limited to, igniters for grenades, mortars, detcord initiators, mortar rounds, detonators such as for rocket motors and mortar rounds, or other systems that include a primer or igniter, a secondary explosive system, alone or in combination with a propellant, or gas generating system such as air bag deployment and jet seat ejectors.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Paints Or Removers (AREA)

Claims (26)

  1. Verfahren zur Herstellung eines Zündelements, das Verfahren umfassend:
    a) Bereitstellen mindestens eines Wasser-Nasssprengstoffs, wobei der mindestens eine Wasser-Nasssprengstoff einen Wassergehalt zwischen etwa 10 Gew.-% und 40 Gew.-% aufweist;
    b) Kombinieren mindestens eines Puffers mit dem mindestens einen Wasser-Nasssprengstoff;
    c) Kombinieren mindestens eines nicht beschichteten Nanogrößen-Brennstoffpartikels mit einer durchschnittlichen Partikelgröße von etwa 50 Nanometer bis etwa 120 Nanometer, wobei der Brennstoffpartikel natürliche Oberflächenoxide darauf aufweist, mit dem mindestens einen Wasser-Nasssprengstoff und dem mindestens einen Puffer, um eine erste Mischung zu bilden; und
    d) Kombinieren mindestens eines Oxidationsmittels mit i) der ersten Mischung, ii) dem mindestens einen Wasser-Nasssprengstoff vor Schritt b) oder iii) dem mindestens einen Wasser-Nasssprengstoff und dem mindestens einen Puffer vor Schritt c).
  2. Verfahren nach Anspruch 1, wobei der mindestens eine nicht beschichtete Nanogrößen-Brennstoffpartikel eine durchschnittliche Partikelgröße von etwa 70 Nanometer bis etwa 120 Nanometer aufweist.
  3. Verfahren nach Anspruch 1, ferner umfassend Kombinieren mindestens eines Bindemittels mit dem mindestens einen Oxidationsmittel, um eine zweite Mischung zu bilden, und Kombinieren der zweiten Mischung mit der ersten Mischung.
  4. Verfahren nach Anspruch 1, ferner umfassend Kombinieren mindestens eines Sensibilisators mit dem mindestens einen Wasser-Nasssprengstoff.
  5. Verfahren nach Anspruch 1, ferner umfassend Kombinieren mindestens eines Sensibilisators mit der ersten Mischung.
  6. Verfahren nach Anspruch 4, wobei der Sensibilisator Tetracen ist.
  7. Verfahren nach Anspruch 6, ferner umfassend Kombinieren mindestens eines Reibungserzeugers mit dem mindestens einen Wasser-Nasssprengstoff.
  8. Verfahren nach Anspruch 7, wobei der mindestens eine Reibungserzeuger Glaspulver ist.
  9. Verfahren nach Anspruch 1, wobei der mindestens eine Puffer eine organische Säure und ein Phosphatsalz umfasst.
  10. Verfahren nach Anspruch 1, wobei der mindestens eine Puffer vor Schritt b) zu dem mindestens einen Wasser-Nasssprengstoff hinzugefügt wird.
  11. Verfahren nach Anspruch 1, wobei der mindestens eine Puffer ein Doppelpuffersystem umfasst, das mindestens ein Salz von Zitronensäure und mindestens ein Salz von Phosphorsäure umfasst.
  12. Verfahren nach Anspruch 4, ferner umfassend Kombinieren des mindestens einen Puffers mit dem mindestens einen Sensibilisator und mindestens einem Wasser-Nasssprengstoff vor Schritt c).
  13. Verfahren nach Anspruch 1, wobei der mindestens eine nicht beschichtete Nanogrößen-Brennstoffpartikel ausgewählt ist aus der Gruppe bestehend aus Aluminium, Silizium, Titan, Zirkonium, Molybdän, Wolfram, Melamin, Magnesium und Mischungen davon.
  14. Verfahren nach Anspruch 1, wobei der Nanogrößen-Brennstoffpartikel Aluminium ist.
  15. Verfahren nach Anspruch 1, wobei der Nanogrößen-Brennstoffpartikel eine durchschnittliche Partikelgröße von etwa 100 Nanometer aufweist.
  16. Verfahren nach Anspruch 1, wobei der nicht beschichtete Nanogrößen-Brennstoffpartikel etwa 10 Gew.-% bis etwa 20 Gew.-% natürliche Oberflächenoxide darauf aufweist.
  17. Verfahren nach Anspruch 1, wobei der mindestens eine Sprengstoff ausgewählt ist aus der Gruppe bestehend aus Nitraminen, Nitroaromaten, Nitratestern und Mischungen davon.
  18. Verfahren nach Anspruch 17, wobei der mindestens eine Sprengstoff ein Nitratester ist und der Nitratester Nitrocellulose umfasst.
  19. Verfahren nach Anspruch 1, wobei das mindestens eine Oxidationsmittel nicht hygroskopisch ist.
  20. Verfahren nach Anspruch 1, wobei das mindestens eine Oxidationsmittel ein Metalloxid ist.
  21. Verfahren nach Anspruch 20, wobei das mindestens eine Oxidationsmittel ausgewählt ist aus der Gruppe bestehend aus Bismutoxid, Bismuttrioxid, Bismuttetroxid, Bismutsubnitrat, Bismutsulfid, Zinkperoxid, Zinnoxid, Mangandioxid, Kaliumnitrat, Molybdäntrioxid, Strontiumnitrat, Strontiumperoxid, Eisenoxid und Kombinationen davon.
  22. Verfahren nach Anspruch 1, wobei der Sprengstoff im Wesentlichen aus einem oder mehreren mäßig unempfindlichen Sprengstoffen besteht und etwa 10 Gew.-% bis etwa 40 Gew.-% des mindestens einen Sprengstoffs umfasst.
  23. Verfahren nach Anspruch 1, umfassend etwa 5 Gew.-% bis etwa 20 Gew.-% des mindestens einen nicht beschichteten Nanogrößen-Brennstoffpartikels mit natürlichen Oberflächenoxiden darauf.
  24. Verfahren nach Anspruch 4, umfassend etwa 5 Gew.-% bis etwa 15 Gew.-% des mindestens einen Sensibilisators.
  25. Verfahren nach Anspruch 1, umfassend etwa 20 Gew.-% bis etwa 70 Gew.-% des mindestens einen Oxidationsmittels.
  26. Verfahren nach Anspruch 3, wobei die zweite Mischung eine Trockenvermischung ist, die gebildet wird durch
    Trockenvermischen des mindestens einen Oxidationsmittels und mindestens eines Bindemittels; und danach Hinzufügen der Trockenvermischung zu der ersten Mischung und Mischen bis zur Homogenität, um eine Endmischung zu bilden.
EP13157579.7A 2007-02-09 2007-02-09 Nicht toxische perkussionszünder und verfahren zu ihrer herstellung Active EP2602238B1 (de)

Priority Applications (1)

Application Number Priority Date Filing Date Title
EP13157579.7A EP2602238B1 (de) 2007-02-09 2007-02-09 Nicht toxische perkussionszünder und verfahren zu ihrer herstellung

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
EP13157579.7A EP2602238B1 (de) 2007-02-09 2007-02-09 Nicht toxische perkussionszünder und verfahren zu ihrer herstellung
PCT/US2007/003806 WO2008100252A2 (en) 2007-02-09 2007-02-09 Non-toxic percussion primers and methods of preparing the same
EP07870653.8A EP2125673B1 (de) 2007-02-09 2007-02-09 Nichttoxische aufschlagzünder

Related Parent Applications (3)

Application Number Title Priority Date Filing Date
EP07870653.8 Division 2007-02-09
EP07870653.8A Division EP2125673B1 (de) 2007-02-09 2007-02-09 Nichttoxische aufschlagzünder
EP07870653.8A Division-Into EP2125673B1 (de) 2007-02-09 2007-02-09 Nichttoxische aufschlagzünder

Publications (3)

Publication Number Publication Date
EP2602238A2 EP2602238A2 (de) 2013-06-12
EP2602238A3 EP2602238A3 (de) 2014-11-26
EP2602238B1 true EP2602238B1 (de) 2021-07-28

Family

ID=39690638

Family Applications (2)

Application Number Title Priority Date Filing Date
EP13157579.7A Active EP2602238B1 (de) 2007-02-09 2007-02-09 Nicht toxische perkussionszünder und verfahren zu ihrer herstellung
EP07870653.8A Active EP2125673B1 (de) 2007-02-09 2007-02-09 Nichttoxische aufschlagzünder

Family Applications After (1)

Application Number Title Priority Date Filing Date
EP07870653.8A Active EP2125673B1 (de) 2007-02-09 2007-02-09 Nichttoxische aufschlagzünder

Country Status (2)

Country Link
EP (2) EP2602238B1 (de)
WO (1) WO2008100252A2 (de)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8641842B2 (en) 2011-08-31 2014-02-04 Alliant Techsystems Inc. Propellant compositions including stabilized red phosphorus, a method of forming same, and an ordnance element including the same
US8192568B2 (en) 2007-02-09 2012-06-05 Alliant Techsystems Inc. Non-toxic percussion primers and methods of preparing the same
US8206522B2 (en) 2010-03-31 2012-06-26 Alliant Techsystems Inc. Non-toxic, heavy-metal free sensitized explosive percussion primers and methods of preparing the same

Family Cites Families (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3113059A (en) * 1962-07-31 1963-12-03 Intermountain Res And Engineer Inhibited aluminum-water composition and method
US3367805A (en) * 1965-06-02 1968-02-06 Intermountain Res And Engineer Thickened inorganic nitrate aqueous slurry containing finely divided aluminum having a lyophobic surface of high surface area
DE2513735A1 (de) * 1974-04-01 1975-10-02 Calgon Corp Korrosionsschutzmittel
US4133707A (en) * 1977-11-14 1979-01-09 Olin Corporation Priming mix with minimum viscosity change
FR2628735B1 (fr) * 1988-03-15 1990-08-24 Ncs Pyrotechnie Technologies Charges d'amorcage a percussion et leur procede de fabrication
IT1266171B1 (it) * 1994-07-15 1996-12-23 Europa Metalli Sezione Difesa Miscela innescante esente da materiali tossici ed innesco a percussione per cartucce utilizzante tale miscela.
AU709965B2 (en) * 1994-10-21 1999-09-09 Elisha Holding Llc Corrosion preventing buffersystem for metal products
BR9500890A (pt) * 1995-02-24 1997-04-29 Companhia Brasileira De Cartuc Misturas iniciadoras não tóxicas isentas de chumbo e bário e tendo como oxidante principal óxido de estanho
US5717159A (en) 1997-02-19 1998-02-10 The United States Of America As Represented By The Secretary Of The Navy Lead-free precussion primer mixes based on metastable interstitial composite (MIC) technology
PT1062188E (pt) * 1998-03-06 2008-10-22 Gen Dynamics Ordnance & Tactic Escorvas não tóxicas para munições de pequeno calibre
MXPA03000357A (es) * 2000-07-13 2004-09-13 Procter & Gamble Metodos y mezclas de reaccion para controlar reacciones exotermicas.
US6478903B1 (en) * 2000-10-06 2002-11-12 Ra Brands, Llc Non-toxic primer mix
US6544363B1 (en) * 2000-10-30 2003-04-08 Federal Cartridge Company Non-toxic, heavy-metal-free shotshell primer mix
US8784583B2 (en) * 2004-01-23 2014-07-22 Ra Brands, L.L.C. Priming mixtures for small arms
US7670446B2 (en) * 2004-11-30 2010-03-02 The United States Of America As Represented By The Secretary Of The Navy Wet processing and loading of percussion primers based on metastable nanoenergetic composites
US20060219341A1 (en) * 2005-03-30 2006-10-05 Johnston Harold E Heavy metal free, environmentally green percussion primer and ordnance and systems incorporating same

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
None *

Also Published As

Publication number Publication date
EP2602238A3 (de) 2014-11-26
WO2008100252A3 (en) 2009-02-26
EP2125673A2 (de) 2009-12-02
EP2125673B1 (de) 2020-08-26
WO2008100252A2 (en) 2008-08-21
EP2602238A2 (de) 2013-06-12

Similar Documents

Publication Publication Date Title
US8202377B2 (en) Non-toxic percussion primers and methods of preparing the same
EP2167447B1 (de) Nicht toxische perkussionszünder
US8470107B2 (en) Non-toxic, heavy-metal free explosive percussion primers and methods of preparing the same
US8784583B2 (en) Priming mixtures for small arms
US8282751B2 (en) Methods of forming a sensitized explosive and a percussion primer
EP1195366B1 (de) Nicht-toxische Zündmittelmischung
EP1829849B1 (de) Nichttoxische, korrosionsfeste Primerzusammensetzung auf Phosphorbasis, Zündkapselprimer damit und diese enthaltendes Geschütz
EP2602238B1 (de) Nicht toxische perkussionszünder und verfahren zu ihrer herstellung
US9409830B1 (en) Non-toxic primer mix
CA2668123C (en) Non-toxic percussion primers and methods of preparing the same

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

AC Divisional application: reference to earlier application

Ref document number: 2125673

Country of ref document: EP

Kind code of ref document: P

AK Designated contracting states

Kind code of ref document: A2

Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HU IE IS IT LI LT LU LV MC NL PL PT RO SE SI SK TR

RIN1 Information on inventor provided before grant (corrected)

Inventor name: SANDSTROM, JOEL LEE

Inventor name: NORRIS, NEAL

Inventor name: BLAU, REED

Inventor name: ERICKSON, JACK

Inventor name: BRAUN, PATRICK

Inventor name: JOHNSTON, GENE

Inventor name: LIU, LISA

RIN1 Information on inventor provided before grant (corrected)

Inventor name: ERICKSON, JACK

Inventor name: SANDSTROM, JOEL

Inventor name: LIU, LISA

Inventor name: BRAUN, PATRICK

Inventor name: BLAU, REED

Inventor name: JOHNSTON, GENE

Inventor name: NORRIS, NEAL

PUAL Search report despatched

Free format text: ORIGINAL CODE: 0009013

AK Designated contracting states

Kind code of ref document: A3

Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HU IE IS IT LI LT LU LV MC NL PL PT RO SE SI SK TR

RIC1 Information provided on ipc code assigned before grant

Ipc: C06B 33/00 20060101ALI20141021BHEP

Ipc: C06C 7/00 20060101AFI20141021BHEP

Ipc: C06B 23/00 20060101ALI20141021BHEP

17P Request for examination filed

Effective date: 20150526

RBV Designated contracting states (corrected)

Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HU IE IS IT LI LT LU LV MC NL PL PT RO SE SI SK TR

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: EXAMINATION IS IN PROGRESS

17Q First examination report despatched

Effective date: 20171012

RAP1 Party data changed (applicant data changed or rights of an application transferred)

Owner name: VISTA OUTDOOR OPERATIONS LLC

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: EXAMINATION IS IN PROGRESS

GRAP Despatch of communication of intention to grant a patent

Free format text: ORIGINAL CODE: EPIDOSNIGR1

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: GRANT OF PATENT IS INTENDED

INTG Intention to grant announced

Effective date: 20210210

GRAS Grant fee paid

Free format text: ORIGINAL CODE: EPIDOSNIGR3

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: THE PATENT HAS BEEN GRANTED

AC Divisional application: reference to earlier application

Ref document number: 2125673

Country of ref document: EP

Kind code of ref document: P

AK Designated contracting states

Kind code of ref document: B1

Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HU IE IS IT LI LT LU LV MC NL PL PT RO SE SI SK TR

REG Reference to a national code

Ref country code: GB

Ref legal event code: FG4D

REG Reference to a national code

Ref country code: CH

Ref legal event code: EP

REG Reference to a national code

Ref country code: DE

Ref legal event code: R096

Ref document number: 602007061237

Country of ref document: DE

REG Reference to a national code

Ref country code: AT

Ref legal event code: REF

Ref document number: 1414625

Country of ref document: AT

Kind code of ref document: T

Effective date: 20210815

REG Reference to a national code

Ref country code: IE

Ref legal event code: FG4D

REG Reference to a national code

Ref country code: DE

Ref legal event code: R081

Ref document number: 602007061237

Country of ref document: DE

Owner name: FEDERAL CARTRIDGE CO., ANOKA, US

Free format text: FORMER OWNER: VISTA OUTDOOR OPERATIONS LLC, FARMINGTON, UT, US

Ref country code: DE

Ref legal event code: R081

Ref document number: 602007061237

Country of ref document: DE

Owner name: VISTA OUTDOOR OPERATIONS LLC, ANOKA, US

Free format text: FORMER OWNER: VISTA OUTDOOR OPERATIONS LLC, FARMINGTON, UT, US

REG Reference to a national code

Ref country code: LT

Ref legal event code: MG9D

RAP4 Party data changed (patent owner data changed or rights of a patent transferred)

Owner name: VISTA OUTDOOR OPERATIONS LLC

REG Reference to a national code

Ref country code: NL

Ref legal event code: MP

Effective date: 20210728

REG Reference to a national code

Ref country code: AT

Ref legal event code: MK05

Ref document number: 1414625

Country of ref document: AT

Kind code of ref document: T

Effective date: 20210728

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: SE

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20210728

Ref country code: NL

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20210728

Ref country code: PT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20211129

Ref country code: ES

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20210728

Ref country code: FI

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20210728

Ref country code: LT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20210728

Ref country code: AT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20210728

Ref country code: BG

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20211028

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: PL

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20210728

Ref country code: LV

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20210728

Ref country code: GR

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20211029

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: DK

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20210728

REG Reference to a national code

Ref country code: DE

Ref legal event code: R097

Ref document number: 602007061237

Country of ref document: DE

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: SK

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20210728

Ref country code: RO

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20210728

Ref country code: EE

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20210728

Ref country code: CZ

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20210728

PLBE No opposition filed within time limit

Free format text: ORIGINAL CODE: 0009261

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT

26N No opposition filed

Effective date: 20220429

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: MC

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20210728

REG Reference to a national code

Ref country code: CH

Ref legal event code: PL

REG Reference to a national code

Ref country code: BE

Ref legal event code: MM

Effective date: 20220228

GBPC Gb: european patent ceased through non-payment of renewal fee

Effective date: 20220209

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: LU

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20220209

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: LI

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20220228

Ref country code: IE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20220209

Ref country code: GB

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20220209

Ref country code: CH

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20220228

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: BE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20220228

REG Reference to a national code

Ref country code: DE

Ref legal event code: R081

Ref document number: 602007061237

Country of ref document: DE

Owner name: FEDERAL CARTRIDGE CO., ANOKA, US

Free format text: FORMER OWNER: VISTA OUTDOOR OPERATIONS LLC, ANOKA, MN, US

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: HU

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT; INVALID AB INITIO

Effective date: 20070209

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: CY

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20210728

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: DE

Payment date: 20240228

Year of fee payment: 18

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: IT

Payment date: 20240222

Year of fee payment: 18

Ref country code: FR

Payment date: 20240226

Year of fee payment: 18