EP2231317A2 - Desensitisation by coating crystals of explosive energy substances, coated crystals of such substances, and energy materials - Google Patents
Desensitisation by coating crystals of explosive energy substances, coated crystals of such substances, and energy materialsInfo
- Publication number
- EP2231317A2 EP2231317A2 EP08865625A EP08865625A EP2231317A2 EP 2231317 A2 EP2231317 A2 EP 2231317A2 EP 08865625 A EP08865625 A EP 08865625A EP 08865625 A EP08865625 A EP 08865625A EP 2231317 A2 EP2231317 A2 EP 2231317A2
- Authority
- EP
- European Patent Office
- Prior art keywords
- crystals
- metal
- coated
- film
- polymer
- 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.)
- Withdrawn
Links
- 239000013078 crystal Substances 0.000 title claims description 113
- 238000000576 coating method Methods 0.000 title claims description 58
- 239000011248 coating agent Substances 0.000 title claims description 55
- 239000000463 material Substances 0.000 title claims description 41
- 239000002360 explosive Substances 0.000 title claims description 33
- 239000000126 substance Substances 0.000 title claims description 32
- 238000000586 desensitisation Methods 0.000 title claims description 5
- 238000000034 method Methods 0.000 claims description 77
- 229910052751 metal Inorganic materials 0.000 claims description 63
- 239000002184 metal Substances 0.000 claims description 63
- 239000010949 copper Substances 0.000 claims description 54
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 44
- 229910052802 copper Inorganic materials 0.000 claims description 44
- 229920000642 polymer Polymers 0.000 claims description 44
- 239000002243 precursor Substances 0.000 claims description 40
- 230000008569 process Effects 0.000 claims description 31
- 239000012530 fluid Substances 0.000 claims description 29
- 230000008021 deposition Effects 0.000 claims description 27
- 239000002904 solvent Substances 0.000 claims description 23
- 239000000203 mixture Substances 0.000 claims description 17
- 229920006254 polymer film Polymers 0.000 claims description 13
- 239000012296 anti-solvent Substances 0.000 claims description 12
- MTHSVFCYNBDYFN-UHFFFAOYSA-N diethylene glycol Chemical compound OCCOCCO MTHSVFCYNBDYFN-UHFFFAOYSA-N 0.000 claims description 12
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims description 10
- 239000005062 Polybutadiene Substances 0.000 claims description 9
- 229920002857 polybutadiene Polymers 0.000 claims description 9
- 238000001556 precipitation Methods 0.000 claims description 9
- 230000009467 reduction Effects 0.000 claims description 9
- -1 polyoxyethylene Polymers 0.000 claims description 8
- XTFIVUDBNACUBN-UHFFFAOYSA-N 1,3,5-trinitro-1,3,5-triazinane Chemical compound [O-][N+](=O)N1CN([N+]([O-])=O)CN([N+]([O-])=O)C1 XTFIVUDBNACUBN-UHFFFAOYSA-N 0.000 claims description 6
- 229920003171 Poly (ethylene oxide) Polymers 0.000 claims description 6
- 238000002360 preparation method Methods 0.000 claims description 6
- 239000000725 suspension Substances 0.000 claims description 6
- 150000002739 metals Chemical class 0.000 claims description 5
- 229910052759 nickel Inorganic materials 0.000 claims description 5
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims description 4
- QCWXUUIWCKQGHC-UHFFFAOYSA-N Zirconium Chemical compound [Zr] QCWXUUIWCKQGHC-UHFFFAOYSA-N 0.000 claims description 4
- 229910052782 aluminium Inorganic materials 0.000 claims description 4
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 4
- 239000004814 polyurethane Substances 0.000 claims description 4
- 239000010936 titanium Substances 0.000 claims description 4
- 229910052719 titanium Inorganic materials 0.000 claims description 4
- 229910052726 zirconium Inorganic materials 0.000 claims description 4
- 125000005595 acetylacetonate group Chemical group 0.000 claims description 3
- 229920001451 polypropylene glycol Polymers 0.000 claims description 3
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 2
- 150000001242 acetic acid derivatives Chemical class 0.000 claims description 2
- 229920001577 copolymer Polymers 0.000 claims description 2
- 125000003055 glycidyl group Chemical group C(C1CO1)* 0.000 claims description 2
- 239000001257 hydrogen Substances 0.000 claims description 2
- 229910052739 hydrogen Inorganic materials 0.000 claims description 2
- 229920002635 polyurethane Polymers 0.000 claims 2
- 238000000151 deposition Methods 0.000 description 29
- 239000000243 solution Substances 0.000 description 22
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 description 19
- 239000010410 layer Substances 0.000 description 19
- 238000012360 testing method Methods 0.000 description 18
- 230000035945 sensitivity Effects 0.000 description 12
- 239000002245 particle Substances 0.000 description 11
- 238000006243 chemical reaction Methods 0.000 description 10
- KDLHZDBZIXYQEI-UHFFFAOYSA-N palladium Substances [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 description 8
- 238000006722 reduction reaction Methods 0.000 description 8
- 238000004626 scanning electron microscopy Methods 0.000 description 7
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 6
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 6
- 239000000843 powder Substances 0.000 description 6
- 238000004833 X-ray photoelectron spectroscopy Methods 0.000 description 5
- 230000005611 electricity Effects 0.000 description 5
- 239000007788 liquid Substances 0.000 description 5
- 239000002105 nanoparticle Substances 0.000 description 5
- 230000003068 static effect Effects 0.000 description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- NDYLCHGXSQOGMS-UHFFFAOYSA-N CL-20 Chemical compound [O-][N+](=O)N1C2N([N+]([O-])=O)C3N([N+](=O)[O-])C2N([N+]([O-])=O)C2N([N+]([O-])=O)C3N([N+]([O-])=O)C21 NDYLCHGXSQOGMS-UHFFFAOYSA-N 0.000 description 4
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- 239000003054 catalyst Substances 0.000 description 4
- 238000012512 characterization method Methods 0.000 description 4
- 239000006184 cosolvent Substances 0.000 description 4
- 230000035939 shock Effects 0.000 description 4
- 239000011230 binding agent Substances 0.000 description 3
- 229910052799 carbon Inorganic materials 0.000 description 3
- 238000000354 decomposition reaction Methods 0.000 description 3
- 238000005474 detonation Methods 0.000 description 3
- 238000013507 mapping Methods 0.000 description 3
- 229910052757 nitrogen Inorganic materials 0.000 description 3
- 229910052573 porcelain Inorganic materials 0.000 description 3
- 239000000377 silicon dioxide Substances 0.000 description 3
- 238000011144 upstream manufacturing Methods 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- QPLDLSVMHZLSFG-UHFFFAOYSA-N Copper oxide Chemical compound [Cu]=O QPLDLSVMHZLSFG-UHFFFAOYSA-N 0.000 description 2
- 239000005751 Copper oxide Substances 0.000 description 2
- 239000000028 HMX Substances 0.000 description 2
- 241001494479 Pecora Species 0.000 description 2
- 238000002441 X-ray diffraction Methods 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 2
- 238000004458 analytical method Methods 0.000 description 2
- 239000011324 bead Substances 0.000 description 2
- 239000001569 carbon dioxide Substances 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 239000011247 coating layer Substances 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 229910000431 copper oxide Inorganic materials 0.000 description 2
- 239000002537 cosmetic Substances 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 239000006185 dispersion Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 229910010272 inorganic material Inorganic materials 0.000 description 2
- UZGLIIJVICEWHF-UHFFFAOYSA-N octogen Chemical compound [O-][N+](=O)N1CN([N+]([O-])=O)CN([N+]([O-])=O)CN([N+]([O-])=O)C1 UZGLIIJVICEWHF-UHFFFAOYSA-N 0.000 description 2
- 150000002894 organic compounds Chemical class 0.000 description 2
- 229910052763 palladium Inorganic materials 0.000 description 2
- 238000001878 scanning electron micrograph Methods 0.000 description 2
- 238000004611 spectroscopical analysis Methods 0.000 description 2
- 230000007704 transition Effects 0.000 description 2
- GDDNTTHUKVNJRA-UHFFFAOYSA-N 3-bromo-3,3-difluoroprop-1-ene Chemical compound FC(F)(Br)C=C GDDNTTHUKVNJRA-UHFFFAOYSA-N 0.000 description 1
- 239000012691 Cu precursor Substances 0.000 description 1
- JPVYNHNXODAKFH-UHFFFAOYSA-N Cu2+ Chemical compound [Cu+2] JPVYNHNXODAKFH-UHFFFAOYSA-N 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 238000003556 assay Methods 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000005234 chemical deposition Methods 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 230000006837 decompression Effects 0.000 description 1
- 230000007123 defense Effects 0.000 description 1
- 238000004200 deflagration Methods 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000010892 electric spark Methods 0.000 description 1
- 238000000921 elemental analysis Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000001198 high resolution scanning electron microscopy Methods 0.000 description 1
- 230000000977 initiatory effect Effects 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 150000002484 inorganic compounds Chemical class 0.000 description 1
- 239000011147 inorganic material Substances 0.000 description 1
- 239000010954 inorganic particle Substances 0.000 description 1
- 239000002923 metal particle Substances 0.000 description 1
- 238000006263 metalation reaction Methods 0.000 description 1
- 239000002120 nanofilm Substances 0.000 description 1
- 229910017604 nitric acid Inorganic materials 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- 230000003287 optical effect Effects 0.000 description 1
- 239000011368 organic material Substances 0.000 description 1
- 239000011146 organic particle Substances 0.000 description 1
- 229920000620 organic polymer Polymers 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 230000008520 organization Effects 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 239000002861 polymer material Substances 0.000 description 1
- 239000003380 propellant Substances 0.000 description 1
- 238000010926 purge Methods 0.000 description 1
- 239000012429 reaction media Substances 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 230000000284 resting effect Effects 0.000 description 1
- 238000012552 review Methods 0.000 description 1
- 238000001228 spectrum Methods 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000010408 sweeping Methods 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C06—EXPLOSIVES; MATCHES
- C06B—EXPLOSIVES OR THERMIC COMPOSITIONS; MANUFACTURE THEREOF; USE OF SINGLE SUBSTANCES AS EXPLOSIVES
- C06B45/00—Compositions or products which are defined by structure or arrangement of component of product
- C06B45/18—Compositions or products which are defined by structure or arrangement of component of product comprising a coated component
- C06B45/20—Compositions or products which are defined by structure or arrangement of component of product comprising a coated component the component base containing an organic explosive or an organic thermic component
-
- 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
- C06B21/0083—Treatment of solid structures, e.g. for coating or impregnating with a modifier
-
- 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
- C06B23/005—Desensitisers, phlegmatisers
-
- 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
- C06B23/009—Wetting agents, hydrophobing agents, dehydrating agents, antistatic additives, viscosity improvers, antiagglomerating agents, grinding agents and other additives for working up
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/54—Improvements relating to the production of bulk chemicals using solvents, e.g. supercritical solvents or ionic liquids
Definitions
- the subject of the present invention is: a process for desensitising by coating crystals with an explosive energy substance
- crystals of a coated explosive energy substance i.e., such desensitized crystals by coating; as well as
- the present invention more specifically relates to the coating of crystals of explosive energy materials by an inorganic layer
- the field of application of the invention covers all that of energetic materials, in particular for defense, space and automobile safety.
- the coating material is generally a polymer which can be either inert (US 4,043,850, DE 37 11 995) pyrotechnically or energetically (WO 2000/73245, GB 2 374 867).
- the coating material consists of a polymeric binder charged with a metal in powder form, said metal being used with reference to electrostatic charges (EP 1,500,639).
- the prior art does not propose a solution for controlling the deposition of a small predetermined amount of coating material on an explosive crystalline substance.
- the control of the quality and thickness of the coating layer is essential to optimize the compromise between the level of desensitization and the energy of the coated explosive substance.
- the skilled person is therefore always looking for a method to control at least the amount of coating, so as to obtain a continuous layer as thin as possible.
- the goal is indeed not to relativize the amount of active product at the expense of a material (coating) less or not energetically active.
- the method must of course also meet, on the one hand, the handling criteria of explosive materials (that is to say, can be implemented at temperatures low enough not to change the structure of the molecules or crystals) and environmental criteria for the use of volatile solvents (for example, VOC emission).
- the method of coating with a thin metallic layer of supercritical fluid consists in depositing a thin nanostructured metal layer (ranging from the organization of nanoparticles to the homogeneous nanostructured film) on organic or inorganic compounds.
- This deposit is made by dissolving a metal precursor in a solvent; said precursor, decomposed, causes precipitation of the metal on the compound to be coated.
- the method is described in application WO 2000/59622.
- the reference "Design at the nanometer scale of multifunctional mater / a / s using supercritical fluid chemical deposition, Samuel Marre et al, Nanotechnology Volume 17, Number 18, September 28, 2006, PP 4594-4599" describes the implementation of this method.
- for the deposition of a copper film (consisting of copper nanoparticles) on submicron silica beads The process is carried out at temperatures of 100 ° C. to 150 ° C. for pressures of 24 MPa. It consists:
- the method of coating with a continuous thin layer of polymer in a supercritical medium is also well known, particularly in the pharmaceutical and cosmetic fields.
- the deposit is made by dissolving the coating agent in a solvent and then by precipitation of said coating agent on the compound to be coated by an anti-solvent effect.
- WO 2004/91571 discloses a method for depositing a polymer coating on particles using a fluid supercritical, for example supercritical carbon dioxide, as antisolvent which is added a polymer solution and an organic solvent in which the particles are dispersed. The deposition is obtained when the supercritical fluid and the suspended particles are combined to cause the precipitation of the polymer on the particles to be coated.
- the present invention therefore relates to a desensitization process by coating crystals with an explosive energy substance.
- said coating process comprises: - the preparation of a solution, containing, dissolved:
- At least one precursor of a coating material said coating material being chosen from metals and their mixtures, and / or
- the deposition implemented in a fluid, outside the normal conditions of temperature and pressure, preferably under supercritical conditions, of a metallic and / or polymeric film, advantageously of a metallic film or of a polymeric film on the surface of said crystals (the film in question is generally a metal film or a polymer film but a mixed film (metal + polymer) is not excluded (see below)).
- the coating material or its precursor is previously dissolved in a solvent: this leaves the possibility of optimizing the choice of the couple: coating material or its precursor / solvent, of adjusting the concentrations of said material or precursor in said solvent ... and thus makes it possible to control subsequently the deposition of the coating material; said coating material is deposited at a temperature greater than ambient temperature (greater than 25 ° C., generally greater than 30 ° C.) and at a pressure greater than atmospheric pressure.
- it is implemented in the liquid field of the fluid in question (above the liquid / gas curve) outside said normal temperature and pressure conditions.
- it is implemented under supercritical conditions.
- the process in question implemented (for the deposition of the coating material) typically under pressure and temperature, is of the type described for application in other fields (see above); process based on the reduction of a metal precursor in a medium under pressure and temperature, preferably supercritical, for the deposition of a metal film; so-called anti-solvent process for the deposition of a polymer film.
- the fluid that operates under pressure and temperature during the implementation of the process of the invention is advantageously carbon dioxide (CO 2 ).
- CO 2 carbon dioxide
- a mass of metal film and / or (advantageously or) polymer, on each coated crystal which represents from 0.3 to 6% of the total mass of said coated crystal; to advantageously deposit: a mass of metal film and / or (advantageously or) polymer, on each coated crystal, which represents 2 to 4% of the total mass of said coated crystal.
- the process of the invention is particularly suitable for depositing a layer of metal particles (Cu) with a thickness of the order of 50 nm, which corresponds to a measured mass ratio of 2.6%.
- the metal layer in question is a blanket (continuous layer) made of nanoparticles.
- the process of the invention is not limited to obtaining such thin coating layers, but the fact that it makes it possible to obtain such thin, but also continuous, uniform layers is particularly advantageous. interesting. It is now proposed to specify a variant of the method of the invention implemented for the deposition of a metal film. Incidentally, the deposition of such a film on the surface of crystals of explosive energy substances is totally novel.
- the process of the invention is advantageously used for the deposition of a metal film of at least one metal chosen from nickel, copper, aluminum, titanium, zirconium and / or at least one oxide of such a metal.
- the metal film in question contains the metal (the metals), the corresponding oxide (s)) or a mixture thereof.
- composition of the coating film is controlled by controlling the parameters of the process and more particularly the pressure and the temperature of implementation of said process as well as the composition of the reaction medium.
- the method of the invention, implemented for the deposition of a metal film is advantageously of the type described in WO 2000/59622. It is based on the reduction of a metal precursor. He understands :
- the heating of the medium causes the precursor to decompose on the surface of the crystals, resulting in the formation of a (metallic) film.
- the fluid used is therefore the solvent of the solution containing said at least one precursor.
- Said at least one precursor is advantageously chosen from metal acetates and acetylacetonates, advantageously from metal hexafluoroacetylacetonates. Such acetylacetonates have a high solubility in supercritical CO 2 .
- Said at least one precursor is very advantageously copper hexafluoroacetylacetonate.
- a known amount of precursor (Cu [hfac] 2) is solubilized in a cosolvent (alcohol).
- the charges (crystals) of CL20 are added and then dispersed by stirring.
- the co-solvent improves the solubility of the precursor (Cu complex) in the supercritical CO 2 (see below) and assists in the reduction reaction.
- the mixture is placed in a pressurized reactor with CO 2 and H 2 .
- the reactor (of constant volume) is heated to supercritical conditions. Once the required pressure and temperature levels have been reached, it is stabilized for a definite time to allow the decomposition of the precursor.
- Cu nanoparticles are deposited on the surface of the crystals.
- the thickness of the deposited layer is obviously a function, for defined conditions, of time and temperature. It also depends on the initial concentration of precursor.
- the coated crystals are then recovered either in dispersion in the co-solvent (after decompression and removal of CO 2 + H 2 ), or in dry form (after entrainment of the cosolvent by the gases).
- the thickness of the deposited metal film is controlled, inter alia, by the temperature, the contact time and the concentration.
- the temperatures for carrying out the reduction vary according to the exact nature of the precursors involved. They generally vary between 70 ° C. and 270 ° C., which makes it possible to be below the decomposition temperatures of explosive energetic substances. It is now proposed to specify a variant of the process of the invention implemented for the deposition of a polymer film.
- the deposition of such a film had been obtained, according to the prior art, wet.
- the films obtained by the method of the invention are of better quality than those obtained according to the prior art (they are deposited, over the entire surface of the crystals, in a continuous and uniform manner, advantageously in a very small thickness).
- the process of the invention is advantageously used for the deposition of a polybutadiene polymer film, in particular a hydroxytelechelic polybutadiene (PBHT), polyurethane (PU), in particular a diethylene glycol polyadipate (PADEG), a polyoxyethylene / polyoxypropylene copolymer (POE / POP), glycidyl polyazide (PAG) or a mixture of such polymers.
- PBHT hydroxytelechelic polybutadiene
- PU polyurethane
- PADEG diethylene glycol polyadipate
- POE / POP polyoxyethylene / polyoxypropylene copolymer
- PAG glycidyl polyazide
- the method of the invention implemented for the deposition of a polymer film, is advantageously of the type described in WO 2004/91571. It is as indicated above an antisolvent process. He understands ;
- PBHT is dissolved in a solvent (dichloromethane, for example).
- the fillers (crystals of CL20 for example) are added and the mixture is stirred mechanically.
- This solution is placed in a reactor.
- CO 2 anti-solvent and solvent of the first solvent
- the reactor is then filled with supercritical solvent, resulting in the precipitation of PBHT on the surface of the crystals.
- the purge valves are then ajar. Traces of solvent (dichloromethane) are entrained, for example by sending a flow of CO 2 .
- characterization techniques made it possible to observe the uniformity of the layer (context of CL20 coated with PBHT or PAG). To quantify the deposited layer, it is expressed in mass percentages, perfectly measurable, which speak to those skilled in the art (see above).
- Layers of PBHT deposited on silica beads according to the process of the invention have thicknesses of 7 ⁇ 2 nm, for a mass ratio of 3% (the density of the silica is obviously not that of CL20). .
- Joint deposition of at least one metal and at least one polymer is not totally excluded from the scope of the invention.
- the control of such a deposit, mixed, is obviously more delicate. It is necessary to involve upstream at least one metal precursor and at least one polymer in solution and determine the conditions of temperature and pressure, in particular, where the at least two reactions provided (reduction of said at least one precursor to at least one metal and precipitation of said at least one polymer) take place.
- it is advantageously used for coating, under pressure and he
- an explosive energy substance of the organic secondary explosive type in particular selected from: roctahydro-1,3,5,7-tetranitro-1,3,5,7-tetrazocine (HMX or octogen), hexahydro ⁇ 1, 3 , 5-trinitro-1,3,5-triazine (RDX, hexogen or cyclonite), 2,4,6,8,10,12-hexanitrohexaazaisowurtzitane (CL20 or HNIW), and 4,10-dinitro-2, 4,6,8,12-tetraoxa-4,10-diazaisowurtzitane (TEX).
- HMX roctahydro-1,3,5,7-tetranitro-1,3,5,7-tetrazocine
- RDX hexahydro ⁇ 1, 3
- RDX hexogen or cyclonite
- 2,4,6,8,10,12-hexanitrohexaazaisowurtzitane CL20 or HNIW
- the present invention relates to coated crystals of an explosive energy substance, obtainable by the method described above: coating process with a metal film and / or (advantageously or) polymer, put typically, outside normal temperature and pressure conditions.
- Said coated crystals are novel by the nature of the film in question and / or by the characteristics thereof (quality (uniform and continuous character, on any surface of the crystals) and / or deposited quantity).
- the crystals coated with a metallic film are new per se.
- the crystals coated with a polymer film are new because of the characteristics of the coating. Said characteristics - original and particularly interesting - result from the original implementation of the coating, under pressure and temperature with a suspension, containing in solution the coating material or at least one precursor thereof (said material or said at least one precursor thereof having been dissolved upstream in a solvent (the nature of said solvent and the concentration of said material or said at least one precursor within said solvent having been optimized) (see above).
- the coated crystals of the invention advantageously have:
- the coated crystals of the invention are advantageously coated with a metal film of at least one metal chosen from nickel, copper, aluminum, titanium, zirconium and / or at least one oxide of such a metal; or coated with a polybutadiene polymer film, in particular a hydroxytelechelic polybutadiene (PHBT), polyurethane (PU), in particular a polyadipate diethylene glycol (PADEG), a polyoxyethylene / polyoxypropylene (POE / POP) copolymer, polyazide glycidile
- crystals are advantageously crystals of an organic secondary explosive chosen especially from those identified upstream in the present text.
- the present invention finally relates to energetic materials incorporating in their composition the crystals of the invention, coated crystals per se and / or desensitized crystals obtained by the process of the invention.
- the energetic materials contain an effective amount of said coated or desensitized crystals. In fact, generally, they consist of said crystals or contain, in an effective amount, in a binder.
- FIG. 2 shows an X-ray photoelectron spectroscopy spectrum (XPS) of a copper coated CL20 crystal according to the method of the invention of example 1.5 (the intensity is plotted on the ordinate in an arbitrary unit (ua); )) -
- XPS X-ray photoelectron spectroscopy spectrum
- FIG. 3 shows a high resolution scanning electron microscopy image made on Cu coated CL20 crystals according to the method of Example 1.4.
- FIGS. 4-1 to 4-3 show scanning electron micrographs taken on CL20 crystals without coating
- Example 1 relates to the application of the method of the invention to the coating with a copper film of the explosive substance 2,4,6,8,10,12-hexanitrohexaazaisowurtzitane (HNIW or CL20).
- HNIW 2,4,6,8,10,12-hexanitrohexaazaisowurtzitane
- the test was carried out by preparing a solution comprising
- Copper-coated CL20 has a gray / black color
- the copper deposition on the CL20 crystals was characterized by
- EDX X-ray dispersed energy
- XPS X-ray photoelectron spectroscopy
- the morphology of copper-coated CL20 crystals was characterized by scanning electron microscopy (SEM).
- SEM scanning electron microscopy
- EDX MEB-associated X-ray analysis technique
- Peaks corresponding to the binding energies of the carbon, oxygen, nitrogen, copper and palladium atoms can be clearly distinguished.
- the (low) presence of palladium comes from the precursor of palladium (Pd (hfac) 2 ) catalyst of the reduction of the copper precursor.
- the enlargement of the copper peak makes it possible to see the proportions of metallic copper (right peak) and copper in oxidized form (precursor, copper oxide - left peak).
- Metallic copper is predominantly present on the surface of CL20.
- the copper present on the surface was determined by atomic absorption. To do this, the samples were washed twice with isopropanol and then filtered in order to remove unencumbered copper particles on the surface of CL20. A gray / black powder is recovered which is dispersed in a nitric acid solution (30% v / v). The CL20 is not modified during this manipulation, while the copper is dissolved to form a measurable Cu 2+ solution. The copper (II) solution can then be determined. The mass percentage of copper present on the surface is 2.76% under the conditions of Example 1.5. However, this value can be varied by varying the parameters of the reaction (initial precursor concentration, catalyst concentration, injection sequences in the precursor and catalyst reactor, reaction time) between 0.3 and 30%. as shown in Table 1. Those skilled in the art will be able to adjust these parameters according to their needs.
- Table 1 Percentage of Cu deposited on the CL20 crystals as a function of the reaction parameters.
- Example 1.5 The sensitivity of the copper-coated CL20 crystals of Example 1.5 was evaluated by following standardized ISI * impact sensitivity, ISF ** friction, ES *** electrical ignition, and critical height tests. without TDD confinement ****. Table 2 below presents the results obtained by comparison with the initial ⁇ -CL20.
- Table 2 Comparison of sensitivity tests for the reference ⁇ -CL20 crystals and the product obtained in Example 1.5.
- the energy can be varied from 1 to 50 J. ** ISF: The test performed corresponds to that described in standard NF T 70-503, itself similar to UN test 3b) ii).
- the force resulting in 50% positive results of an explosive substance subjected to friction is determined using the Bruceton method.
- the material to be tested is placed on a porcelain wafer of defined roughness, moved in a single back and forth motion, of 10 mm amplitude at a speed of 7 cm / s when empty, compared to a pencil. porcelain resting on the material.
- the force applied to the porcelain pencil which is pressed on the material may vary from 7.8 to 353 N.
- the test performed is a test developed by the Applicant with no equivalent NF or UN.
- the material to be tested placed in a cup of diameter 10 mm and height 1.5 mm, is placed between two electrodes and is subjected to an electric spark of variable energy from 5 to 726 ml. pyrotechnic or not and we determine the threshold of energy no longer ensuring the initiation of the material. This value is confirmed by 20 successive tests.
- the test consists of measuring the ability of a mass of divided material (grain bed) to pass from combustion to detonation following ignition, performed on the surface of the bed, specifically for CL20, otherwise at the base of the powder bed.
- the N ° 55 SNPE test consists of filling a 40 mm diameter metal tube of variable height. The tube is open at one end. The critical height leading to a violent reaction is determined from the effects noted on the tube.
- Table 3 compares the values of density p, pulse Is and pulse volume Isxp calculated for three types of propellants comprising in their composition either ⁇ -CL20 or copper-coated CL20 according to Example 1.5.
- Table 3 Comparison of the p, Is and Isxp values obtained by calculation with two different Azalanes® compositions (Al: 18% w / w, ammonium perchlorate: 12% w / w + binder + explosive substance).
- the density of the coated substance increases slightly with respect to the initial substance due to the presence of (approximately) 3% copper.
- the specific impulse of the copper-coated CL20 according to Example 1.5 is, on the other hand, reduced.
- the value of the Isxp, which takes into account the specific pulse and the density of the product is almost equal to that of a composition using ⁇ -CL20.
- EXAMPLE 2 Coating TEX crystals with a copper film
- Example 2 relates to the application of the process to the coating with a copper film of the explosive substance 4,10-dinitro-2,4,6,8,12-tetraoxa-4,10-diazaisowurtzitane so-called TEX.
- Table 4 gives the two reaction parameters and
- Table 4 Percentage of Cu deposited on the TEX crystals as a function of the reaction parameters.
- Example 3 relates to the application of the method to the coating with a PBHT polymer film of the explosive substance 2,4,6,8,10,12-hexanitrohexaazaisowurtzitane (HNIW or CL20).
- the principle of polymer deposition on the surface of CL20 crystals is based on an antisolvent process under supercritical conditions.
- the polymer is dissolved in a dichloromethane solution
- DCM supercritical antisolvent
- ScCO 2 supercritical antisolvent
- PBHT precipitation of PBHT on the surface of the crystals of the explosive substance.
- the removal of the DCM is done by slow depressurization and sweeping of an antisolvent flow for a determined duration (drying time).
- the crystals coated with the polymer are recovered in the bottom of the reactor in the form of a dry powder.
- the polymer deposition on the CL20 crystals was characterized by SEM and UV-Visible spectroscopy.
- UV-Visible spectroscopy makes it possible to determine the amount of polymer deposited on the surface of the crystals.
- the principle of the assay is to redissolve the deposited polymer by placing a certain amount of crystals embedded in DCM. The solution is then filtered and the polymer collected is assayed.
- Example 3 The reaction conditions of Example 3 and the percentage of PBHT are given in Table 5 below.
- Table 5 Percentage of PBHT deposited on CL20 crystals as a function of reaction parameters.
- the PBHT coated CL20 crystals are white in color and have an expanded texture compared to the initial powder ( Figure 4).
- Example 3 The sensitivity of the PBHT-coated CL20 crystals of Example 3 was evaluated by following the standardized tests described in Example 1. Table 6 below shows the results obtained by comparison with the initial ⁇ -CL20.
- Table 6 Comparison of sensitivity tests for the initial substance ⁇ -CL20 and the coated product of Example 3.1.
- the PBHT coating reduces sensitivity to ISF friction and static electricity, and to a lesser extent to ISI impact. It significantly decreases the sensitivity to the TDD test.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Crystallography & Structural Chemistry (AREA)
- Other Surface Treatments For Metallic Materials (AREA)
- Crystals, And After-Treatments Of Crystals (AREA)
- Application Of Or Painting With Fluid Materials (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Chemically Coating (AREA)
Abstract
Description
Claims
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR0760036A FR2925488B1 (en) | 2007-12-19 | 2007-12-19 | CRYSTAL COATING DENSIBILIZATION OF EXPLOSIVE ENERGY SUBSTANCES; CRYSTALS SUCH AS COATED SUBSTANCES, ENERGY MATERIALS. |
PCT/FR2008/052353 WO2009081048A2 (en) | 2007-12-19 | 2008-12-18 | Desensitisation by coating crystals of explosive energy substances, coated crystals of such substances, and energy materials |
Publications (1)
Publication Number | Publication Date |
---|---|
EP2231317A2 true EP2231317A2 (en) | 2010-09-29 |
Family
ID=39768940
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP08865625A Withdrawn EP2231317A2 (en) | 2007-12-19 | 2008-12-18 | Desensitisation by coating crystals of explosive energy substances, coated crystals of such substances, and energy materials |
Country Status (8)
Country | Link |
---|---|
US (1) | US20100307648A1 (en) |
EP (1) | EP2231317A2 (en) |
JP (1) | JP2011506262A (en) |
KR (1) | KR20100106493A (en) |
FR (1) | FR2925488B1 (en) |
IL (1) | IL206041A0 (en) |
RU (1) | RU2484887C2 (en) |
WO (1) | WO2009081048A2 (en) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
RU2590562C1 (en) * | 2014-12-26 | 2016-07-10 | Российская Федерация, от имени которой выступает Государственная корпорация по атомной энергии "Росатом" - Госкорпорация "Росатом" | Method for treatment of explosive substance |
US10184327B2 (en) | 2015-12-15 | 2019-01-22 | Schlumberger Technology Corporation | Downhole tool explosive with thermally conductive material |
DE102019205276A1 (en) | 2019-04-11 | 2020-10-15 | Christof-Herbert Diener | Coating process of an energetic material and coating system for coating the energetic material by such a coating process |
KR102575548B1 (en) * | 2020-09-08 | 2023-09-05 | 한화에어로스페이스 주식회사 | Boron bead complex for solid propellant, method for manufacturing the same, and solid propellant comprising the same |
Family Cites Families (24)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2031677A5 (en) * | 1969-02-04 | 1970-11-20 | France Etat | Explosive mixtures contg metals prepn |
US4043850A (en) * | 1976-08-06 | 1977-08-23 | The United States Of America As Represented By The Secretary Of The Navy | Polymeric-coated HMX crystals for use with propellant materials |
DE3711995A1 (en) * | 1987-04-09 | 1988-10-20 | Messerschmitt Boelkow Blohm | Desensitising explosives or propellants - comprises mixing them with desensitiser e.g. graphite dissolved in a liq. solvent, evaporating solvent etc. |
DE4111752C1 (en) * | 1991-04-11 | 1992-09-17 | Fraunhofer-Gesellschaft Zur Foerderung Der Angewandten Forschung Ev, 8000 Muenchen, De | |
EP0706821A1 (en) * | 1994-10-06 | 1996-04-17 | Centre De Microencapsulation | Method of coating particles |
US5587553A (en) * | 1994-11-07 | 1996-12-24 | Thiokol Corporation | High performance pressable explosive compositions |
US5808234A (en) * | 1996-05-06 | 1998-09-15 | Eastman Chemical Company | Explosive formulations |
FR2753639B1 (en) * | 1996-09-25 | 1998-12-11 | PROCESS FOR THE PREPARATION OF MICROCAPSULES OF ACTIVE MATERIALS COATED WITH A POLYMER AND NOVEL MICROCAPSULES OBTAINED IN PARTICULAR BY THE PROCESS | |
DE19711393C1 (en) * | 1997-03-19 | 1998-08-13 | Fraunhofer Ges Forschung | Process for microencapsulating particles |
US5879079A (en) * | 1997-08-20 | 1999-03-09 | The United States Of America As Represented By The Administrator, Of The National Aeronautics And Space Administration | Automated propellant blending |
DE19742034A1 (en) * | 1997-09-24 | 1999-03-25 | Diehl Stiftung & Co | Electric fuze |
EP1028820B1 (en) * | 1997-10-15 | 2009-12-30 | University Of South Florida | Supercritical fluid aided coating of particulate material |
US5886293A (en) * | 1998-02-25 | 1999-03-23 | The United States Of America As Represented By The Secretary Of The Navy | Preparation of magnesium-fluoropolymer pyrotechnic material |
US6083565A (en) * | 1998-11-06 | 2000-07-04 | North Carolina State University | Method for meniscus coating with liquid carbon dioxide |
FR2791580B1 (en) * | 1999-04-02 | 2001-05-04 | Centre Nat Rech Scient | PROCESS FOR COATING PARTICLES |
US6194571B1 (en) * | 1999-05-26 | 2001-02-27 | Schlumberger Technology Corporation | HMX compositions and processes for their preparation |
GB9913262D0 (en) * | 1999-06-09 | 2002-08-21 | Royal Ordnance Plc | Desensitation of energetic materials |
US6605167B1 (en) * | 2000-09-01 | 2003-08-12 | Trw Inc. | Autoignition material for a vehicle occupant protection apparatus |
US7537803B2 (en) * | 2003-04-08 | 2009-05-26 | New Jersey Institute Of Technology | Polymer coating/encapsulation of nanoparticles using a supercritical antisolvent process |
FR2857963B1 (en) * | 2003-07-25 | 2006-09-08 | Giat Ind Sa | PULVERULENT SUBSTANCE AND PROCESS FOR PRODUCING SUCH A SUBSTANCE. |
US6958308B2 (en) * | 2004-03-16 | 2005-10-25 | Columbian Chemicals Company | Deposition of dispersed metal particles onto substrates using supercritical fluids |
US8163114B2 (en) * | 2004-04-07 | 2012-04-24 | New Jersey Institute Of Technology | Netshape manufacturing processes and compositions |
RU2267010C1 (en) * | 2004-09-02 | 2005-12-27 | Открытое акционерное общество "Боровичский комбинат огнеупоров" | Proppant and a method for manufacturing thereof |
JP2007085632A (en) * | 2005-09-21 | 2007-04-05 | Asahi Kasei Chemicals Corp | Table propellant |
-
2007
- 2007-12-19 FR FR0760036A patent/FR2925488B1/en not_active Expired - Fee Related
-
2008
- 2008-12-18 US US12/809,315 patent/US20100307648A1/en not_active Abandoned
- 2008-12-18 RU RU2010128085/05A patent/RU2484887C2/en not_active IP Right Cessation
- 2008-12-18 EP EP08865625A patent/EP2231317A2/en not_active Withdrawn
- 2008-12-18 WO PCT/FR2008/052353 patent/WO2009081048A2/en active Application Filing
- 2008-12-18 JP JP2010538868A patent/JP2011506262A/en active Pending
- 2008-12-18 KR KR1020107015893A patent/KR20100106493A/en not_active Application Discontinuation
-
2010
- 2010-05-27 IL IL206041A patent/IL206041A0/en unknown
Non-Patent Citations (1)
Title |
---|
See references of WO2009081048A2 * |
Also Published As
Publication number | Publication date |
---|---|
WO2009081048A3 (en) | 2010-04-08 |
FR2925488B1 (en) | 2011-12-23 |
WO2009081048A2 (en) | 2009-07-02 |
RU2010128085A (en) | 2012-01-27 |
FR2925488A1 (en) | 2009-06-26 |
IL206041A0 (en) | 2010-11-30 |
US20100307648A1 (en) | 2010-12-09 |
RU2484887C2 (en) | 2013-06-20 |
KR20100106493A (en) | 2010-10-01 |
JP2011506262A (en) | 2011-03-03 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
Kosareva et al. | HMX surface modification with polymers via sc-CO2 antisolvent process: A way to safe and easy-to-handle energetic materials | |
Huang et al. | Incorporation of high explosives into nano-aluminum based microspheres to improve reactivity | |
EP2231317A2 (en) | Desensitisation by coating crystals of explosive energy substances, coated crystals of such substances, and energy materials | |
EP2448885B1 (en) | Method for producing solid composite aluminized propellants, and solid composite aluminized propellants | |
EP2694187A1 (en) | Particle of a phase change material with coating layer | |
WO2010061127A2 (en) | Composite composition for solid propellants including a ferrocene derivative and a submicronic aluminum charge, solid propellant, and load | |
WO2011039459A2 (en) | Suspensions of hexanitrohexaazaisowurtzitane crystals, production of said suspensions and production of pyrotechnic objects | |
Popenko et al. | Effect of the addition of ultrafine aluminum powders on the rheological properties and burning rate of energetic condensed systems | |
Li et al. | Oxidation mechanism of perfluorooctanoic acid-functionalized aluminum metastable intermolecular composites regulated by Preignition reactions interface fuel-oxidizer ratio | |
CA2689318A1 (en) | Method for determining the sensitive or insensitive nature of a hexogen | |
Li et al. | Polyphenols-inspired interface modification and reduced agglomeration of solid propellants via a functionalized fluorine-containing organic substance coating layer | |
Fu et al. | Preparation of high-energy Al-Li alloy powders with enhanced compatibility and combustion performance by dense fluorosilane polymer composite coating | |
Eslami et al. | Stabilization of ammonium azide particles through its microencapsulation with some organic coating agents | |
Li et al. | Ultrastable aluminum nanoparticles with enhanced combustion performance enabled by a polydopamine/polyethyleneimine nanocoating | |
Manhas et al. | Thermoplastic polyurethane-based nanoencapsulation strategy for efficient storage and stability of RDX | |
Hosseini et al. | Orthogonal array design method for optimization experiments of sodium azide microencapsulation with stearic acid | |
EP2694516B1 (en) | Method for obtaining a batch of hexanitrohexaazaisowurtzitane crystals having a round morphology; batch and energetic material thereof | |
Gromov et al. | Characterization of Aluminum Powders: III. Non‐Isothermal Oxidation and Combustion of Modern Aluminized Solid Propellants with Nanometals and Nanooxides | |
EP1500639B1 (en) | Pyrotechnic material and method for manufacturing | |
EP3953317B1 (en) | New energy-releasing composite material and method for manufacturing same | |
Zhang et al. | Enhanced combustion characteristics of fuel‐rich propellant based on Al− Mg via GAP‐IPDI energetic thermoplastic polymer | |
Yao et al. | Combustion characteristics of composite solid propellants containing different coated aluminum nanopowders | |
Yang et al. | Preparation and characterization of core/shell structure of HMX/NTO composite particles | |
FR2936795A1 (en) | DENSITIZED EXPLOSIVE COMPOSITIONS, DENSATED EXPLOSIVE LOADS AND AMMUNITION COMPRISING THE SAME | |
Terry | Altered combustion characteristics of metallized energetics due to stable secondary material inclusion |
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 |
|
17P | Request for examination filed |
Effective date: 20100610 |
|
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 HR HU IE IS IT LI LT LU LV MC MT NL NO PL PT RO SE SI SK TR |
|
AX | Request for extension of the european patent |
Extension state: AL BA MK RS |
|
DAX | Request for extension of the european patent (deleted) | ||
RAP1 | Party data changed (applicant data changed or rights of an application transferred) |
Owner name: EURENCO |
|
RAP1 | Party data changed (applicant data changed or rights of an application transferred) |
Owner name: EURENCO Owner name: SNPE MATERIAUX ENERGETIQUES |
|
RAP1 | Party data changed (applicant data changed or rights of an application transferred) |
Owner name: EURENCO Owner name: SME |
|
RAP1 | Party data changed (applicant data changed or rights of an application transferred) |
Owner name: EURENCO Owner name: HERAKLES |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: THE APPLICATION IS DEEMED TO BE WITHDRAWN |
|
18D | Application deemed to be withdrawn |
Effective date: 20150701 |