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EP0607449A1 - Composition explosive et sa production - Google Patents

Composition explosive et sa production Download PDF

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Publication number
EP0607449A1
EP0607449A1 EP93913524A EP93913524A EP0607449A1 EP 0607449 A1 EP0607449 A1 EP 0607449A1 EP 93913524 A EP93913524 A EP 93913524A EP 93913524 A EP93913524 A EP 93913524A EP 0607449 A1 EP0607449 A1 EP 0607449A1
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EP
European Patent Office
Prior art keywords
microspheres
explosive
explosive composition
organic
thermoplastic
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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.)
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EP93913524A
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German (de)
English (en)
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EP0607449A4 (fr
EP0607449B1 (fr
Inventor
Takenori 17 Sakuragaoka 1-Chome Arita
Shunichi 5981-1 Datecho 3-Chome Sato
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Asahi Kasei Corp
Asahi Chemical Industry Co Ltd
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Asahi Chemical Industry Co Ltd
Asahi Kasei Kogyo KK
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Priority claimed from JP4178940A external-priority patent/JPH05208885A/ja
Application filed by Asahi Chemical Industry Co Ltd, Asahi Kasei Kogyo KK filed Critical Asahi Chemical Industry Co Ltd
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    • C—CHEMISTRY; METALLURGY
    • C06—EXPLOSIVES; MATCHES
    • C06B—EXPLOSIVES OR THERMIC COMPOSITIONS; MANUFACTURE THEREOF; USE OF SINGLE SUBSTANCES AS EXPLOSIVES
    • C06B47/00—Compositions in which the components are separately stored until the moment of burning or explosion, e.g. "Sprengel"-type explosives; Suspensions of solid component in a normally non-explosive liquid phase, including a thickened aqueous phase
    • C06B47/14—Compositions in which the components are separately stored until the moment of burning or explosion, e.g. "Sprengel"-type explosives; Suspensions of solid component in a normally non-explosive liquid phase, including a thickened aqueous phase comprising a solid component and an aqueous phase
    • 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

Definitions

  • the present invention relates to an explosive for industrial use. More particularly, it relates to an explosive composition that can be used for various destructive works such as blasting, crushing, excavation, etc., in the field of civil engineering and construction, mining operations such as quarrying, coal and other ore mining, etc., and operations in agricultural and forestry industries including drainage, irrigation, grubbing and lumbering.
  • Slurry explosives and emulsion explosives are typical of the conventional hydrous explosives.
  • the active explosive components comprising an oxidizer solution, an inflammable material and a sensitizer and the bubbles are held stably in high concentrations in a mass in the presence of a sizing agent, and these explosives are usually detonated by means of a detonator.
  • the aerated bubbles or chemical bubbles are usually allowed to exist in the explosive composition to let them play a role like a sensitizer, and guar gum is used as sizing agent to compose an aqueous gel.
  • an oxidizer solution and an oil serving as an inflammable agent are combined to form a W/O type emulsion in the presence of a surfactant serving as a sizing agent.
  • the bubbles in these explosives comprise glass or resinous microballoons, besides the aerated bubbles.
  • the slurry explosives have their peculiar gel elasticity and lack plasticity, and when they are packed into a cartridge, such a cartridge itself proves to be soft and limp, so that it is hard to handle and also difficulties are encountered in inserting the cartridge into a blast hole, resulting in a reduced working efficiency for blasting operation. Also, because of poor moldability of this type of explosives, it was hard to use the explosives in the bare form without cartridge.
  • An object of the present invention is to provide an explosive composition which is basically composed of an oxidizer, water and organic hollow microspheres and which has a highly stabilized bursting performance and long-time keeping quality without a gel or emulsion structure such as seen in the conventional hydrous explosives.
  • Another object of the present invention is to provide an explosive composition which can be handled with safety, produces few unexplosed residue after blasting and is also capable of reducing the degree of harmfulness of the produced gases.
  • Still another object of the present invention is to provide a low-detonation-rate explosive having a stabilized blasting performance even in the low-density section, which has been difficult to obtain with the conventional explosives.
  • the present invention provides a novel explosive composition characterized in that a liquid phase mainly composed of an oxidizer and water and containing substantially no viscous component is adsorbed and held on the surfaces of and/or between the organic hollow microspheres which are an inflammable component.
  • Fig. 1 is a microphotograph showing a fragmental fine structure of the explosive composition according to the present invention.
  • Fig. 2(a) is a schematic illustration of the above structure
  • (b) and (c) are schematic illustrations of the conventional powder compositions.
  • the fine structure of the explosive composition according to the present invention can be confirmed from, for example, microphotographs.
  • Fig. 1 which is a typical microphotographical representation of the structure of the present explosive composition
  • the composition is an aggregation of small granular bodies each comprising an organic hollow microsphere 2 having a high-concentration oxidizer solution 1 adhering to its periphery.
  • Fig. 2(a) A conceptual illustration of this structure is given in Fig. 2(a), from which it is seen that in the explosive composition of this invention the organic hollow microspheres 2 constitute the structural core of the composition.
  • Fig. 2(a) A conceptual illustration of this structure is given in Fig. 2(a), from which it is seen that in the explosive composition of this invention the organic hollow microspheres 2 constitute the structural core of the composition.
  • This is a contrast to the compositional structure of the conventional slurry explosives in which, as shown in Fig.
  • the aerated bubbles 5 and hollow bodies 4 are dispersed in a gelled oxidizer/sensitizer phase 3.
  • the hollow bodies 4 such as glass microballoons are dispersed in an emulsified oxidizer solution phase 6. It is thus obvious that the explosive composition of the present invention is quite different from those of the conventional slurry and emulsion explosives in form of bubbles, form of the oxidizer solution and structure of the composition.
  • the composition of this invention requires no gelling agent needed in the conventional slurry explosives and has a structure in which, unlike the conventional slurry explosives, the bubbles are incorporated in a stable form in the organic hollow microspheres which are an inflammable component. Also, as compared with the emulsion explosives, the composition of this invention requires no oil phase as an inflammable component, no surfactant for forming an emulsion and no glass microballoons for holding the bubbles, which presents a striking contrast to the conventional emulsion explosives.
  • said hollow microspheres can concurrently serve as an inflammable component, it has become possible to provide an explosive with excellent performance without necessarily requiring use of an inflammable agent such as carbon or aluminum powder and a sensitizer mainly composed of an organic nitrate and/or an inorganic nitrate.
  • the composition of the present invention can be applied to a variety of explosives ranging from detonator explosives to booster explosives. Especially when the average thickness of the explosive compound layer around the organic hollow microsphere becomes about 20 ⁇ m or less as observed by a microscope, it is noted that the composition is even more stabilized.
  • the oxidizer used in the present invention can be selected from those known in the art.
  • examples of such oxidizers include ammonium salts, alkali metal salts and alkaline earth metal salts of inorganic acids such as nitric acid, chloric acid, perchloric acid and the like, and these oxidizers can be used either singly or in combination.
  • ammonium nitrate is especially recommendable as it has high solubility in water and is also easily available.
  • the content of the oxidizer in the composition of the present invention is decided according to the specifications of the explosive to be produced, but usually it is in the range of 50 to 90% by weight based on the whole composition.
  • the water content in the composition of this invention is usually in the range of 3 to 20% by weight based on the whole composition.
  • the solid content of the explosive composition increases to affect the stable blasting performance thereof, while a too high water content results in a reduced detonating performance.
  • the organic hollow microspheres used in the present invention are preferably those made by using an organic high-molecular weight compound as base material.
  • organic high-molecular weight compounds usable here include phenol resins, epoxy resins, urea resins, unsaturated polyester resins, polyimides, maleic acid resins, melamine resins, celluloses, vinyl chloride, vinylidene chloride, acrylonitrile, acrylic acids, acrylic acid salts, acrylic esters, methacrylic acids, methacrylic acid salts, methacrylic esters, single polymers or copolymers of styrene, ethylene, propylene, butadiene, vinyl acetate and the like, polycarbonates, polysulfone, polyacetal, polyamides, polyethylene oxide, polyphenylene oxide and the like.
  • organic high-molecular weight compounds those having thermoplasticity, such as vinylidene chloride-acrylonitrile copolymer, vinylidene chloride-acrylonitrile-methacrylic ester copolymer, acrylonitrile-acrylic ester copolymer and the like are especially preferred for use in carrying out the process of the present invention.
  • the unfoamed microparticles of a vinylidene chloride-acrylonitrile copolymer or methyl methacrylate-acrylonitrile copolymer incorporated with a low-boiling point hydrocarbon can be easily made into hollow microspheres by heating, so that they can be used in a heat-foamed form after mixed with the explosive composition.
  • the organic hollow microspheres used in the composition of the present invention are not specifically defined; they may be hollow spheres containing a gas or air in the inside hollow portion or hollow bodies having closed or open spaces therein, but hollow spherical bodies are preferred for efficiently forming the hot spots where the explosive charge is detonated.
  • the gas held in the organic hollow spheres may be air, a low-boiling point hydrocarbon, other inflammable gas, or a mixture thereof.
  • the recommendable particle size of the organic hollow microspheres is about 1,000 ⁇ m or less in diameter. When the particle size exceeds this limit, the hot spots for initiating explosion are reduced in number, making it difficult to produce good detonation property.
  • the organic hollow microspheres have a particle diameter of 20 to 200 ⁇ m as these spheres can provide a stabilized explosion without lowering the velocity of detonation.
  • the film thickness of the organic hollow microspheres is not critical; it may be properly selected as far as the film has enough strength to give a space for accommodating the explosive composition. Usually, the film thickness is 0.1 to 5 ⁇ m.
  • the organic high-molecular weight compound forming the organic hollow microspheres is the thermoplastic type, there are used those microspheres whose film thickness in the foamed state is about 0.1 to 2 ⁇ m since they are required to be capable of being foamed by heating in the explosive composition.
  • the organic hollow microspheres in the explosive composition of this invention are usually of a bulk density of about 0.01 to 0.3 as measured in a dry state.
  • the amount of the organic hollow microspheres in the composition is usually about 2 to 15% by weight based on the whole composition.
  • the density of the explosive composition can be controlled by the amount of the organic hollow microspheres.
  • the ratio of the organic hollow microspheres in the composition is too low, the detonating efficiency is lowered, and it also becomes difficult to maintain a stabilized blasting performance for a long time.
  • the ratio of said organic hollow microspheres is too high, the power of explosion is lowered to jeopardize the blasting reliability.
  • an explosive composition having a density ranging from 0.2 to 1.4 g/cm3 in a stabilized way be adjusting the extent of foaming of the organic hollow microspheres.
  • the explosive composition of this invention has a velocity of detonation of usually about 1,500 to 5,500 m/sec.
  • a mixture of an oxidizer and water is heated to a degree that will cause substantial dissolution of the mixture, and then the organic hollow microspheres are uniformly mixed therein.
  • the method for heat-foaming the organic microspheres is not specified in this invention, but the following methods may be cited as recommendable examples: 1 an oxidizer, water and the foamable organic microspheres are heated to a temperature that allows substantially uniform mixing of said materials to form a mixed solution, and then this solution is dropped or sprayed onto a heated plate or into an atmosphere adjusted to a temperature, or above that, at which said microspheres are caused to begin foaming, thereby foaming the organic microspheres contained in said mixed solution; 2 an oxidizer, water and the foamable organic microspheres are heated to a temperature allowing substantially uniform mixing of said materials to form a mixed solution, and the solution is supplied into a metal tube heated to a temperature, or above that, which causes start of foaming of said microspheres, thereby foaming the organic microspheres contained in said mixed solution; 3 a mixed solution of an oxidizer, water and the foamable organic microspheres is put into a container and this container is heated in an external bath of a temperature at which foaming of
  • the amount of water that may be evaporated is estimated and water is added in an excess amount so that the desired explosive composition will be provided.
  • the unfoamed organic microspheres are increased in internal pressure by heating and begin to foam as they are heated close to a temperature at which the organic polymer film begins to soften, and they are expanded about 20- to 100-fold in volume ratio.
  • the organic hollow microspheres are heated more than necessary and bursted, they can no longer serve as an effective component of an explosive, so that it is recommended to stop heating before reaching a temperature at which overfoaming may be caused.
  • the explosive composition according to the present invention can be presented in various forms such as solid, powder, flakes, paste, etc., and it can be packed with a known packaging material such as paper, laminated paper, plastic film, laminated plastic film, paper tube, plastic tube, etc., selected according to the form of the composition, its properties, object of use and other factors, and thus can be commercially offered in the form of packs.
  • a known packaging material such as paper, laminated paper, plastic film, laminated plastic film, paper tube, plastic tube, etc.
  • the explosive composition of this invention is capable of well satisfying the quality requirements for an explosive, but for additional improvement of blasting performance, an organic nitrate such as a lower saturated aliphatic amine or an inorganic nitrate such as hydrazine nitrate may be added as a sensitizer to accommodate use in the cold districts. Also, in consideration of gas release after blasting in a tunnel or underground mine, a solid inflammable material such as coal powder or aluminum powder may be additionally supplied. Other pertinent substances, for example, an activator such as phosphoric ester, a decomposition inhibitor such as urea, etc., may be safely added as desired.
  • the explosive composition and its producing method according to the present invention there can be obtained a variety of explosives ranging from the booster-blasted type to the percussion-initiated type, and the explosives with a wide variety of dead pressing density.
  • the present invention can be applied to formulation of almost all sorts of conventional explosives.
  • the explosive composition of this invention is improved in dead pressing phenomenon attendant on the emulsion explosives, that is, improved in anti-dead pressing property, and the safety in the work field can be further improved due to the reduction of the unexploded compound residue.
  • the production method according to this invention needs no high-degree production techniques such as required in the production of the conventional slurry and emulsion explosives, and is capable of producing a desired type of explosive with ease and safety.
  • the explosive composition of this invention can be usually detonated by using various known systems such as electric detonator, industrial detonator, detonator with blasting tube, detonator with gas-blasting tube, electromagnetic detonator, laser detonator, wireless detonator, blasting fuse, detonating fuse, etc.
  • the explosive composition may be detonated by using a booster.
  • the present invention will hereinafter be described in more detail with reference to the examples thereof, which examples, however, are merely intended to be illustrative and not to be construed as limiting the scope of the invention.
  • the cap sensitivity, booster performance, velocity of detonation, cartridge propagation in steel tube and anti-dead pressing property in sand were determined by the following methods.
  • An explosive charge was densely packed in a polyethylene laminated paper tube or a nylon 66 film tube (pack diameter: 20 mm or 30 mm; pack length: about 200 mm) and kept in a refrigerator of about -30°C for about 15 hours. Thereafter, the charge, with its temperature adjusted, was detonated by a #6 detonator, and the temperature at which the charge was perfectly exploded was measured. For evaluating the keeping quality, the same detonation test was conducted on the same explosive charge which has been kept in storage for one year after production thereof.
  • a test explosive filled in a steel cylinder (JIS G 3452 32A; inner diameter: 36 mm; length: 350 mm) closed on one side in the longitudinal direction was detonated by a booster (50 g of #2 Enoki dynamite attached with a #6 detonator), and from visual observation of the state of wrecking of the steel cylinder, it was determined whether perfect explosion occurred or not.
  • a booster 50 g of #2 Enoki dynamite attached with a #6 detonator
  • An explosive charge was packed in a polyethylene laminated paper tube or a nylon 66 film tube (pack diameter: about 20 mm ⁇ ; pack length: 150 mm), and about 20 packs were set in juxtaposition to each other in a steel tube (JIS G 3452 40A; inner diameter: about 41.6 mm; length: 3,000 mm) so that no deformation would take place in the longitudinal direction. Then the pack at an end was detonated by #6 detonator and the length of the wrecked portion of the steel tube was measured to determine propagation performance in steel tube. For evaluating the keeping quality, the same test was conducted on the same packs which have been kept in storage for one year after production thereof.
  • An explosive charge was packed in a polyethylene laminated paper tube or a nylon 66 film tube (pack diameter: 30 mm; pack length: about 150 mm).
  • This test was conducted 5 times repeatedly, and it was checked whether the explosive pack attached with the 10 ms short-delay electric detonator was perfectly detonated or not to determine anti-dead pressing property in sand. For evaluating the keeping quality, the same test was conducted on the same packs which have been kept in storage for one year after production thereof.
  • This explosive composition was packed in a steel tube (JIS G 3452 32A; inner diameter: about 36 mm; length: 350 mm) which had been closed on one side in the longitudinal direction, and detonated by a booster (50 g of #2 Enoki dynamite attached with a #6 detonator). There took place perfect detonation.
  • a booster 50 g of #2 Enoki dynamite attached with a #6 detonator
  • 1608 g of ammonium nitrate, 310 g of water and 82 g of non-foamed organic microspheres (MATSUMOTO MICROSPHERE F-30 which is a vinylidene chloride-acrylonitrile-methacrylic ester copolymer produced by Matsumoto Yushi-Seiyaku Co., Ltd.) were supplied into a metallic container and mixed with stirring in an external bath of about 80°C to obtain a mixture of about 70°C. There was also prepared a metal plate heated to about 100-150°C. The above mixture was dropped peacemeal onto the surface of said metal plate, whereby a granular explosive composition could be obtained in a very short time.
  • MATEROTO MICROSPHERE F-30 which is a vinylidene chloride-acrylonitrile-methacrylic ester copolymer produced by Matsumoto Yushi-Seiyaku Co., Ltd.
  • This explosive composition was dispensed and packed in the polyethylene laminated paper tubes of 20 mm and 30 mm in diameter to obtain the explosive packs each containing 30-40 g of said composition, and their blasting performance was examined.
  • the density of the 30 mm-diameter pack was 0.35 g/cm3, and this pack could be detonated by a #6 detonator at -10°C.
  • the rate of detonation at the temperature of 5°C was 1,900 m/s.
  • the 2 mm-diameter pack was loaded in a steel tube having an inner diameter of 41.6 mm and a length of 3 m and detonated from one end thereof by a #6 detonator.
  • Example 3 Example 4
  • Example 5 Ammonium nitrate 1530 g 1550 g 1530 g Water 270 g 270 g 270 g Non-foamed organic microspheres 1 200 g - - Non-foamed organic microspheres 2 - 180 g - Non-foamed organic microspheres 3 - - 200 g
  • the non-foamed organic microspheres 1 were the same as used in Example 2.
  • the non-foamed organic microspheres 2 were made of an acrylonitrile-methyl methacrylate copolymer (053WU produced by Expancel AB), and the non-foamed organic microspheres 3 were composed of an acrylonitrile-acrylic ester copolymer (MATSUMOTO MICROSPHERE F-30, Matsumoto Yusi-Seiyaku Co., Ltd.).
  • the 20 mm-diameter and 30 mm-diameter pack densities of the above three explosive compositions were 0.23, 0.30 and 0.40, respectively.
  • the 30 mm-diameter packs at a temperature of -10°C could be detonated by a #6 detonator.
  • the velocity of detonation of said three explosive compositions at a temperature of 5°C was 1,900 m/s, 2,000 m/s and 2,200 m/s, respectively.
  • 1608 g of ammonium nitrate, 310 g of water and 82 g of non-foamed organic microspheres (MATSUMOTO MICROSPHERE F-30 which is a vinylidene chloride-acrylonitrile-methacrylic ester copolymer, produced by Matsumoto Yusi-Seiyaku Co., Ltd.) were charged into a metallic container and mixed with stirring in a water bath of about 70°C to obtain a mixture of about 70°C.
  • This mixture was injected into a 20 mm-diameter metallic tube (Teflon coated on the inner wall), which had been heated to about 100-150°C, from one end thereof, and an open-cell foamed string-shaped explosive composition was obtained from the other end.
  • the thus obtained explosive composition was dispended to form the explosive packs in the manner described above, and their blasting performance was examined.
  • the density of the 20 mm ⁇ packs was 0.45 g/cm3, and these packs could be detonated by a #6 detonator at a temperature of -5°C.
  • the velocity of detonation at the temperature of 5°C was 1,900 m/s.
  • This mixture was injected into a 20 mm ⁇ metal tube (Teflon coated on inner wall), which had been heated to about 90-110°C, from the opening at one end thereof, and a creamy explosive composition having a density of 1.35 g/cm3 was obtained from the opening at the other end.
  • Example 8 Example 9
  • Example 10 Ammonium nitrate 1560 g 1524 g 1530 g Water 320 g 286 g 270 g Non-foamed organic microspheres 1 120 g - - Non-foamed organic microspheres 2 - 190 g - Non-foamed organic microspheres 3 - - 200 g
  • the non-foamed organic microspheres 1 were the same as used in Example 1, and the non-foamed organic microspheres 2 were made of an acrylonitrile-methyl methacrylate copolymer (053WU, Expancel AB).
  • the non-foamed organic microspheres 3 were composed of an acrylonitrile-acrylic ester copolymer (MATSUMOTO MICROSPHERE F-50, Matsumoto Yusi-Seiyaku Co., Ltd.).
  • the densities of the above three explosive compositions were 1.38 g/cm3 and 1.35 g/cm3, respectively.
  • Each of the above explosive compositions was packed in a steel tube (JIS G 3452 32A; inner diameter: about 36 mm; length: 350 mm), which had been closed on one side in the longitudinal direction, and detonated by a booster (50 g of #2 Enoki dynamite attached with a #6 detonator).
  • a booster 50 g of #2 Enoki dynamite attached with a #6 detonator.
  • each of said explosive compositions was detonated perfectly, and the velocity of detonation was 5,500 m/s, 4,600 m/s and 5,100 m/s, respectively.
  • the similar result was obtained.
  • 1608 g of ammonium nitrate, 310 g of water and 82 g of non-foamed organic microspheres (MATSUMOTO MICROSPHERE F-30, a vinylidene-acrylonitrile-methacrylic ester copolymer, produced by Matsumoto Yusi-Seiyaku Co., Ltd.) were placed in a stainless steel container and heated with slow stirring in an oil bath of about 100-130°C to obtain a creamy explosive composition.
  • This explosive composition was dispensed and packed in the 20 mm ⁇ and 30 mm ⁇ polyethylene laminated paper tubes to form the explosive packs each containing about 50 g of said composition, and their blasting performance was examined.
  • the density of the 30 mm ⁇ explosive pack was 0.70 g/cm3, and this pack could be detonated by a #6 detonator at -5°C.
  • the velocity of detonation at of 5°C was 2,500 m/s.
  • the 20 mm ⁇ pack was loaded in a steel tube of 41.6 mm in inner diameter and 3 m in length and detonated from one end by a #6 detonator. All of the explosive charge was perfectly detonated, and the length of the wrecked portion of the steel tube was 3 m.
  • two 30 mm ⁇ explosive packs were subjected to an in-sand dead pressing test in which said two packs were buried 80 cm deep in sand parallel to each other with a spacing of 15 cm therebetween, with a #6 electric detonator attached to one pack and a 10 ms short-delay detonator attached to the other pack, and detonated by electrifying said detonators.
  • This test was conducted 5 times. Both packs were perfectly detonated in each run of test. When the same test was conducted on the same explosive composition kept in storage for one year after production thereof, the similar result was obtained.
  • 1,250 g of ammonium nitrate, 170 g of water and 160 g of sodium nitrate, 300 g of monomethylamine nitrate and 120 g of non-foamed organic microspheres (MATSUMOTO MICROSPHERE F-30, a vinylidene chloride-acrylonitrile-methacrylic acid copolymer) were mixed while heating to about 70°C to form a homogeneous mixed solution.
  • An amount of this solution determined by taking into consideration possible volume expansion on heating, was filled in a 20 mm ⁇ nylon 66 film tube.
  • said tube was placed in a hot bath of 100-150°C to heat the mixed solution therein, causing foaming of the organic microspheres contained in said mixture, and the blasting performance as an explosive composition packed in said nylon 66 film tube was examined.
  • the density of the explosive charge in said 20 mm ⁇ nylon 66 film tube was 0.35 g/cm3, and this explosive pack could be detonated by a #6 detonator at -10°C.
  • the velocity of detonation at 5°C was 2,200 m/s.
  • the above explosive pack was loaded in a steel tube of 41.6 mm in diameter and 3 m long and detonated from one end thereof by a #6 detonator.
  • This explosive composition was dispensed and packed in the 20 mm ⁇ and 30 mm ⁇ polyethylene laminated paper tubes to form the explosive packs each containing about 30-40 g of said composition, and their blasting performance was examined.
  • the density of the 30 mm ⁇ explosive pack was 0.35 g/cm3, and this pack could be detonated by a #6 detonator at of -20°C.
  • the velocity of detonation at 5°C was 2,300 m/s.
  • the 20 mm ⁇ explosive pack was loaded in a steel tube of 41.6 mm in diameter and 3 m in length and detonated from one end thereof by a #6 detonator.
  • Example 14 Ammonium nitrate 1,520 g 1,330 g Water 80 g 170 g Monomethylamine nitrate 350 g 300 g Sodium nitrate - 160 g Organic hollow microspheres 50 g 40 g
  • the 30 mm ⁇ pack densities of the above two explosive compositions were 1.02 and 0.95, respectively, and the packed compositions could be detonated by a #6 detonator at 0°C.
  • the velocity of detonation at 5°C was 3,700 m/s and 3,200 m/s, respectively.
  • 1,296 g of ammonium nitrate, 164 g of water, 358 g of monomethylamine nitrate and 78 g of non-foamed organic microspheres (MATSUMOTO MICROSPHERE F-30 which is a vinylidene chloride-acrylonitrile-methacrylic ester copolymer produced by Matsumoto Yusi-Seiyaku Co., Ltd.) were placed in a metallic container and mixed by stirring the container in a water bath of about 70°C to obtain a mixture of about 70°C. Meanwhile, there was prepared a metal plate (Teflon coated on inner side) heated to about 100-150°C. The above mixture was dropped peacemeal onto the surface of said hot metal plate, thereby obtaining a granular explosive composition in a very short time.
  • MATEROTO MICROSPHERE F-30 which is a vinylidene chloride-acrylonitrile-methacrylic ester copolymer produced by Matsumoto Yusi-
  • This explosive composition was dispended and packed in the 20 mm ⁇ and 30 mm ⁇ polyethylene laminated paper tubes to form the explosive packs each containing about 30-40 g of said composition, and their blasting performance was examined.
  • the density of the 30 mm ⁇ explosive pack was 0.80 g/cm3, and this pack could be detonated by a #6 detonator at -15°C.
  • the velocity of detonation at 5°C was 3,700 m/s.
  • the 20 mm ⁇ explosive pack was loaded in a steel tube of 41.6 mm in inner diameter and 3 m in length and detonated from one end thereof by a #6 detonator.
  • Example 17 Example 18
  • Example 19 Ammonium nitrate 1338 g 1490 g 1470 g Water 210 g 170 g 170 g Monomethylamine nitrate 300 g 240 g 240 g Sodium nitrate - 140 g - Non-foamed organic microspheres 1 152 g - - Non-foamed organic microspheres 2 - 100 g - Non-foamed organic microspheres 3 - - 120 g
  • the non-foamed organic microspheres 1 are the same as used in Example 16, and the non-foamed organic microspheres 2 are made of an acrylonitrile-methyl methacrylate copolymer (053WU, Expancel AB).
  • the non-foamed organic microspheres 3 are composed of an acrylonitrile-acrylic ester copolymer (MATSUMOTO MICROSPHERE F-50, Matsumoto Yusi-Seiyaku Co., Ltd.).
  • the 20 mm ⁇ and 30 mm ⁇ pack densities of the above three explosive compositions were 0.20, 0.30 and 0.45, respectively.
  • the 30 mm ⁇ pack at -25°C could be detonated by a #6 detonator.
  • the velocity of detonation at 5°C was 1,900 m/s, 2,300 m/s and 2,500 m/s, respectively.
  • the 20 mm ⁇ pack was loaded in a steel tube of 41.6 mm in diameter and 3 m in length and detonated from one side by a #6 detonator.
  • the whole pack charged was detonated perfectly, and the length of the wrecked portion of the steel tube was 3 m.
  • 1,346 g of ammonium nitrate, 240 g of water, 80 g of sodium nitrate, 174 g of monomethylamine nitrate and 160 g of non-foamed organic microspheres were supplied into a stainless steel container and heated with slow stirring in an oil bath of about 80-90°C to obtain an explosive composition with an explosive density of 1.38 g/cm3.
  • the explosive composition according to the present invention in virtue of its peculiar structure in which the active component comprising an oxidizer and water or a sensitizer, an oxidizer and water is held continuously on the surfaces of and/or in the spaces between the adjoining microspheres, substantially unnecessitates use of a thickener which has been indispensable for maintenance of quality of the conventional hydrous explosive compositions, and it can not only keep its quality for a long time but also realized practical use of the low-specific-gravity products which has been considered unfeasible with the conventional hydrous explosives. Owing to reduction of specific gravity, the noise and vibration generated at the time of blasting can be remarkably lessened.

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Manufacturing Of Micro-Capsules (AREA)
  • Drilling And Exploitation, And Mining Machines And Methods (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Disintegrating Or Milling (AREA)
  • Agricultural Chemicals And Associated Chemicals (AREA)

Abstract

Composition explosive comprenant un composant explosif adsorbé à la surface de petites particules organiques creuses et entre lesdites particules creuses.
EP93913524A 1992-06-15 1993-06-15 Composition explosive et sa production Expired - Lifetime EP0607449B1 (fr)

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
JP17894092 1992-06-15
JP178940/92 1992-06-15
JP4178940A JPH05208885A (ja) 1991-06-26 1992-06-15 含水爆薬組成物
PCT/JP1993/000802 WO1993025500A1 (fr) 1992-06-15 1993-06-15 Composition explosive et sa production

Publications (3)

Publication Number Publication Date
EP0607449A1 true EP0607449A1 (fr) 1994-07-27
EP0607449A4 EP0607449A4 (fr) 1994-12-14
EP0607449B1 EP0607449B1 (fr) 2000-08-23

Family

ID=16057308

Family Applications (1)

Application Number Title Priority Date Filing Date
EP93913524A Expired - Lifetime EP0607449B1 (fr) 1992-06-15 1993-06-15 Composition explosive et sa production

Country Status (9)

Country Link
EP (1) EP0607449B1 (fr)
KR (1) KR970004708B1 (fr)
AU (1) AU657629B2 (fr)
CA (1) CA2115660C (fr)
DE (1) DE69329271T2 (fr)
ES (1) ES2148232T3 (fr)
TW (1) TW238296B (fr)
WO (1) WO1993025500A1 (fr)
ZA (1) ZA934244B (fr)

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR1544937A (fr) * 1967-11-13 1968-11-08 Du Pont Explosifs de sautage
GB1314285A (en) * 1970-12-16 1973-04-18 Ici Australia Ltd Explosive compositions
GB1344148A (en) * 1970-10-15 1974-01-16 Dow Chemical Co Explosive compositon
US3996078A (en) * 1971-05-29 1976-12-07 Dynamit Nobel Aktiengesellschaft Explosive composition and eutectic mixture therefor
GB2010239A (en) * 1977-12-15 1979-06-27 Nitro Nobel Ab Watergel explosive
EP0142271A1 (fr) * 1983-10-21 1985-05-22 Nippon Oil And Fats Company, Limited Composition explosive du type émulsion eau-dans-l'huile
US4547234A (en) * 1983-07-15 1985-10-15 Nippon Oil And Fats Company Limited Explosive composition
JPH04198081A (ja) * 1990-11-28 1992-07-17 Asahi Chem Ind Co Ltd 非ゲル含水爆薬組成物

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4343663A (en) * 1980-06-30 1982-08-10 E. I. Du Pont De Nemours And Company Resin-bonded water-bearing explosive
JPS6136189A (ja) * 1984-07-30 1986-02-20 旭化成株式会社 含水爆薬組成物

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR1544937A (fr) * 1967-11-13 1968-11-08 Du Pont Explosifs de sautage
GB1344148A (en) * 1970-10-15 1974-01-16 Dow Chemical Co Explosive compositon
GB1314285A (en) * 1970-12-16 1973-04-18 Ici Australia Ltd Explosive compositions
US3996078A (en) * 1971-05-29 1976-12-07 Dynamit Nobel Aktiengesellschaft Explosive composition and eutectic mixture therefor
GB2010239A (en) * 1977-12-15 1979-06-27 Nitro Nobel Ab Watergel explosive
US4547234A (en) * 1983-07-15 1985-10-15 Nippon Oil And Fats Company Limited Explosive composition
EP0142271A1 (fr) * 1983-10-21 1985-05-22 Nippon Oil And Fats Company, Limited Composition explosive du type émulsion eau-dans-l'huile
JPH04198081A (ja) * 1990-11-28 1992-07-17 Asahi Chem Ind Co Ltd 非ゲル含水爆薬組成物

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
DATABASE WPI Section Ch, Week 9235, Derwent Publications Ltd., London, GB; Class K04, AN 92-288838 & JP-A-4 198 081 (ASAHI CHEM IND CO LTD) 17 July 1992 *
See also references of WO9325500A1 *

Also Published As

Publication number Publication date
TW238296B (fr) 1995-01-11
DE69329271T2 (de) 2001-03-15
EP0607449A4 (fr) 1994-12-14
CA2115660A1 (fr) 1993-12-23
CA2115660C (fr) 1998-06-23
ES2148232T3 (es) 2000-10-16
AU657629B2 (en) 1995-03-16
AU4356293A (en) 1994-01-04
ZA934244B (en) 1994-01-12
KR970004708B1 (ko) 1997-04-02
WO1993025500A1 (fr) 1993-12-23
DE69329271D1 (de) 2000-09-28
EP0607449B1 (fr) 2000-08-23

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