JP2001048689A - Granular explosive powder - Google Patents
Granular explosive powderInfo
- Publication number
- JP2001048689A JP2001048689A JP11225699A JP22569999A JP2001048689A JP 2001048689 A JP2001048689 A JP 2001048689A JP 11225699 A JP11225699 A JP 11225699A JP 22569999 A JP22569999 A JP 22569999A JP 2001048689 A JP2001048689 A JP 2001048689A
- Authority
- JP
- Japan
- Prior art keywords
- ammonium nitrate
- explosive
- emulsified mixture
- weight
- emulsifier
- 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.)
- Pending
Links
- 239000002360 explosive Substances 0.000 title claims abstract description 90
- 239000000843 powder Substances 0.000 title abstract description 5
- 239000000203 mixture Substances 0.000 claims abstract description 51
- PAWQVTBBRAZDMG-UHFFFAOYSA-N 2-(3-bromo-2-fluorophenyl)acetic acid Chemical compound OC(=O)CC1=CC=CC(Br)=C1F PAWQVTBBRAZDMG-UHFFFAOYSA-N 0.000 claims abstract description 43
- 239000002245 particle Substances 0.000 claims abstract description 32
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 32
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 21
- 239000003995 emulsifying agent Substances 0.000 claims abstract description 21
- 239000007800 oxidant agent Substances 0.000 claims abstract description 17
- 239000000446 fuel Substances 0.000 claims abstract description 5
- 239000000839 emulsion Substances 0.000 abstract description 10
- 238000004519 manufacturing process Methods 0.000 abstract description 8
- 229910052751 metal Inorganic materials 0.000 abstract description 8
- 239000002184 metal Substances 0.000 abstract description 8
- 239000011248 coating agent Substances 0.000 abstract description 5
- 238000000576 coating method Methods 0.000 abstract description 5
- 239000004094 surface-active agent Substances 0.000 abstract description 5
- 239000004200 microcrystalline wax Substances 0.000 abstract description 2
- 235000019808 microcrystalline wax Nutrition 0.000 abstract description 2
- 230000001105 regulatory effect Effects 0.000 abstract 1
- 229910002651 NO3 Inorganic materials 0.000 description 22
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 21
- 229910001220 stainless steel Inorganic materials 0.000 description 16
- 239000010935 stainless steel Substances 0.000 description 16
- VWDWKYIASSYTQR-UHFFFAOYSA-N sodium nitrate Chemical compound [Na+].[O-][N+]([O-])=O VWDWKYIASSYTQR-UHFFFAOYSA-N 0.000 description 14
- 238000011156 evaluation Methods 0.000 description 12
- 238000005469 granulation Methods 0.000 description 10
- 230000003179 granulation Effects 0.000 description 10
- 230000002776 aggregation Effects 0.000 description 8
- 238000004945 emulsification Methods 0.000 description 7
- 235000010344 sodium nitrate Nutrition 0.000 description 7
- 239000004317 sodium nitrate Substances 0.000 description 7
- 238000012360 testing method Methods 0.000 description 7
- 230000000052 comparative effect Effects 0.000 description 6
- 239000000454 talc Substances 0.000 description 6
- 229910052623 talc Inorganic materials 0.000 description 6
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 5
- 238000004140 cleaning Methods 0.000 description 5
- 238000005054 agglomeration Methods 0.000 description 4
- 238000004220 aggregation Methods 0.000 description 4
- 229910052782 aluminium Inorganic materials 0.000 description 4
- 238000012790 confirmation Methods 0.000 description 4
- 238000005474 detonation Methods 0.000 description 4
- 239000003814 drug Substances 0.000 description 4
- 229940079593 drug Drugs 0.000 description 4
- 239000011521 glass Substances 0.000 description 4
- 239000007788 liquid Substances 0.000 description 4
- 238000002156 mixing Methods 0.000 description 4
- 239000004677 Nylon Substances 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- 238000002844 melting Methods 0.000 description 3
- 230000008018 melting Effects 0.000 description 3
- 229920001778 nylon Polymers 0.000 description 3
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 238000005422 blasting Methods 0.000 description 2
- ZCCIPPOKBCJFDN-UHFFFAOYSA-N calcium nitrate Chemical compound [Ca+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O ZCCIPPOKBCJFDN-UHFFFAOYSA-N 0.000 description 2
- 239000006229 carbon black Substances 0.000 description 2
- 238000004880 explosion Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 239000008187 granular material Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000000123 paper Substances 0.000 description 2
- FGIUAXJPYTZDNR-UHFFFAOYSA-N potassium nitrate Chemical compound [K+].[O-][N+]([O-])=O FGIUAXJPYTZDNR-UHFFFAOYSA-N 0.000 description 2
- 238000005096 rolling process Methods 0.000 description 2
- 230000035945 sensitivity Effects 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 1
- IOVCWXUNBOPUCH-UHFFFAOYSA-N Nitrous acid Chemical compound ON=O IOVCWXUNBOPUCH-UHFFFAOYSA-N 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 229910052783 alkali metal Inorganic materials 0.000 description 1
- 150000001340 alkali metals Chemical class 0.000 description 1
- 229910052784 alkaline earth metal Inorganic materials 0.000 description 1
- 150000001342 alkaline earth metals Chemical class 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 238000009412 basement excavation Methods 0.000 description 1
- 239000002981 blocking agent Substances 0.000 description 1
- 235000008429 bread Nutrition 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 239000007771 core particle Substances 0.000 description 1
- 239000003599 detergent Substances 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- -1 dynamite Substances 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 238000009472 formulation Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 229910017604 nitric acid Inorganic materials 0.000 description 1
- 150000002828 nitro derivatives Chemical class 0.000 description 1
- 239000008041 oiling agent Substances 0.000 description 1
- 239000012188 paraffin wax Substances 0.000 description 1
- 235000010333 potassium nitrate Nutrition 0.000 description 1
- 239000004323 potassium nitrate Substances 0.000 description 1
- OTYBMLCTZGSZBG-UHFFFAOYSA-L potassium sulfate Chemical compound [K+].[K+].[O-]S([O-])(=O)=O OTYBMLCTZGSZBG-UHFFFAOYSA-L 0.000 description 1
- 229910052939 potassium sulfate Inorganic materials 0.000 description 1
- 235000011151 potassium sulphates Nutrition 0.000 description 1
- 230000009257 reactivity Effects 0.000 description 1
- 239000011435 rock Substances 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 description 1
- 229920002554 vinyl polymer Polymers 0.000 description 1
- 239000011800 void material Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C06—EXPLOSIVES; MATCHES
- C06B—EXPLOSIVES OR THERMIC COMPOSITIONS; MANUFACTURE THEREOF; USE OF SINGLE SUBSTANCES AS EXPLOSIVES
- C06B31/00—Compositions containing an inorganic nitrogen-oxygen salt
- C06B31/28—Compositions containing an inorganic nitrogen-oxygen salt the salt being ammonium nitrate
Landscapes
- Chemical & Material Sciences (AREA)
- Inorganic Chemistry (AREA)
- Organic Chemistry (AREA)
- Lubricants (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、産業用爆薬におけ
る発破、破砕、掘削などに関するものである。本発明
は、更に詳しくは、産業用爆薬の改良に関するものであ
る。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to blasting, crushing, excavation and the like of industrial explosives. The invention relates more particularly to improvements in industrial explosives.
【0002】[0002]
【従来の技術】産業用爆薬として一般的に使用されてい
る爆薬は、ダイナマイト、エマルション爆薬やスラリー
爆薬などの含水爆薬、硝安油剤爆薬(ANFO)であ
る。ダイナマイトは、製造の段階でシリンダー状に成形
され、一本づつ紙で巻かれたカートリッジタイプのもの
があり、その状態で消費される。含水爆薬にも、紙巻き
のものとビニールチューブのカートリッジタイプのもの
がある。含水爆薬は、配合によっては通常の爆薬使用温
度領域で流動性があり、バルクタイプといって、流動性
を保持したまま重袋や金属容器に入れて出荷され、モー
ノポンプなどを使用して発破孔に装填され消費されるも
のがある。硝安油剤爆薬は、粒状の爆薬であり、圧縮空
気を利用したANFOローダー等で装薬されるバルクタ
イプの爆薬である。カートリッジタイプの爆薬は、一本
づつ発破孔に装填されるため、作業に時間がかかった
り、作業者が不安定な岩盤が存在する切羽に接近しなく
てはならないため、安全性に問題がある。一方、バルク
タイプの爆薬は機械で装薬されるため、比較的迅速で安
全な作業が可能である。2. Description of the Related Art Explosives generally used as industrial explosives are hydrous explosives such as dynamite, emulsion explosives and slurry explosives, and nitrous acid explosives (ANFO). Dynamite is formed into a cylinder at the stage of manufacturing, and there is a cartridge type wound with paper one by one, and is consumed in that state. Wet explosives are also available in paper roll and vinyl tube cartridge types. Depending on the formulation, hydrous explosives have fluidity in the normal explosive operating temperature range.They are called bulk type and are shipped in heavy bags or metal containers while maintaining fluidity, and are blasted using a mono pump or the like. Some are loaded and consumed. An ammonium nitrate explosive is a granular explosive, and is a bulk explosive charged by an ANFO loader or the like using compressed air. Cartridge-type explosives are loaded one by one into the blast holes, which takes a long time to work and poses a safety problem because workers have to approach the face where there is unstable rock. . On the other hand, bulk-type explosives are charged mechanically, so that relatively quick and safe operation is possible.
【0003】[0003]
【発明が解決しようとする課題】バルクタイプの含水爆
薬は、粘着性が非常に高いものが多く、付着残留薬とい
って運搬・貯蔵用の重袋や装填機の金属容器などに爆薬
が付着して残りやすい問題がある。付着残留薬を回収す
るためにへら等で除去しようとしても完全に取り去るこ
とはしばしば困難であり、特に、装填用ホース内、金属
容器のわん曲部や直角部は完全に取り去ることは非常に
困難である。結局、適当な界面活性剤を用いて、時間を
かけて水で洗い流すしか方法がない。更に、作業者の体
表面や作業着に付着して不快を感じさせたりすることが
ある。また、手に付着した場合は、滑りやすくなるた
め、安全上また作業の能率上も支障を与えることが多
い。硝安油剤爆薬は、バルクタイプの爆薬ではあるが、
粒状の爆薬であるため、付着残留薬の心配はないが、耐
水性が乏しいことや含水爆薬よりも威力が小さいこと、
また後ガスが悪いことなどの問題がありトンネル工事の
発破等には必ずしも適していない。そうした問題から、
近年エマルション爆薬を硝安油剤爆薬粒子表面に被覆し
た粒状爆薬(中国特許1137507)が研究されてい
る。その爆薬は、耐水性のない硝安油剤爆薬を耐水性の
あるエマルション爆薬で覆うことにより耐水性を付加し
たものであり、また粒状爆薬として作業性が比較的改善
されたものであるが、そのような爆薬を製造するには、
まず硝安油剤爆薬とエマルション爆薬の二つの爆薬をそ
れぞれ製造しなければならない。また、それら二つの爆
薬を混合する時は、乳化温度付近まで加熱されなければ
ならず、更に軽油が蒸発するなどの危険が伴うことが多
い。更に、生成した爆薬は、凝集を防ぐために8時間程
度の慎重な撹拌が必要であり、製造工程が危険を伴って
大変複雑である。Many types of bulk type water-containing explosives have extremely high adhesiveness, and are referred to as "adhesive residues". The explosives adhere to heavy bags for transportation and storage, metal containers of loading machines, and the like. There is a problem that tends to remain. It is often difficult to completely remove the residual drug by using a spatula in order to recover it, especially in the loading hose and in the bent or right-angled metal containers. It is. After all, there is no other way but to wash away with water with a suitable surfactant over time. Furthermore, it may adhere to the body surface or the work clothes of the worker and make the worker feel uncomfortable. In addition, if it adheres to the hand, it becomes slippery, which often impairs safety and work efficiency. The nitrate explosive is a bulk type explosive,
Because it is a granular explosive, there is no need to worry about residual drugs, but it has poor water resistance and is less powerful than hydrous explosives.
In addition, it is not always suitable for blasting tunnel construction due to problems such as bad post gas. From such a problem,
Recently, a granular explosive (Chinese Patent 1137507) in which an emulsion explosive is coated on the surface of an ammonium nitrate explosive particle has been studied. The explosives were made by adding water resistance by covering a non-water resistant nitric acid oil explosive with a water resistant emulsion explosive, and the workability was relatively improved as a granular explosive. In order to produce a powerful explosive,
First of all, two explosives must be manufactured: a nitrate oil explosive and an emulsion explosive. In addition, when mixing these two explosives, they must be heated to near the emulsification temperature, and there is often a danger that gas oil evaporates. Furthermore, the produced explosive requires careful stirring for about 8 hours to prevent agglomeration, and the manufacturing process is very complicated with danger.
【0004】[0004]
【課題を解決するための手段】本発明は、硝安を主成分
とする多孔質粒子の表面が油剤、酸化剤、水及び乳化剤
からなる乳化混合物によって被覆されており、乳化混合
物の組成は、酸化剤と油剤の重量比が9.0以下対1.
0以上であることを特徴とする粒状爆薬である。本発明
の望ましい態様としては、硝安を主成分とする多孔質粒
子の少なくとも一個の粒子を含んで造粒された爆薬であ
る。According to the present invention, the surface of porous particles mainly composed of ammonium nitrate is coated with an emulsified mixture comprising an oil agent, an oxidizing agent, water and an emulsifier. Weight ratio of the agent to the oil agent is 9.0 or less to 1.
It is a granular explosive characterized by being 0 or more. A preferred embodiment of the present invention is an explosive granulated including at least one porous particle mainly composed of ammonium nitrate.
【0005】ここで、油剤及び酸化剤とは「エネルギー
物質ハンドブック、P.95−P.98、共立出版(1
999年)」に記載されている油剤と酸化剤のことであ
る。すなわち、エマルション爆薬に用いられる、例えば
マイクロクリスタリンワックスやパラフィンワックスな
どの油剤と、硝酸アンモニウムやアルカリ金属の硝酸
塩、アルカリ土類金属の硝酸塩などの酸化剤のことであ
る。また、硝安を主成分とする多孔質粒子とは、たとえ
ば同「エネルギー物質ハンドブック」P.93−P.9
4等に記載されるプリル硝安等をいう。また、乳化剤と
は、界面活性剤等としてエマルション爆薬に用いられる
通常のものをいう。[0005] Here, the oil agent and the oxidizing agent are described in "Energy Material Handbook, P.95-P.98, Kyoritsu Shuppan (1.
999) ". That is, it refers to oil agents such as microcrystalline wax and paraffin wax used for emulsion explosives, and oxidizing agents such as ammonium nitrate, nitrate of alkali metal, and nitrate of alkaline earth metal. Further, the porous particles mainly composed of ammonium nitrate are described in, for example, "Energy Material Handbook", p. 93-P. 9
4 means prill nitrate and the like. Further, the emulsifier refers to a usual one used for an emulsion explosive as a surfactant or the like.
【0006】本発明の望ましい実施の態様の一つにおい
ては、乳化混合物の組成は、酸化剤と油剤の重量比が
9.0以下対1.0以上とされ、更に望ましくは、9.
0以下1.0以上対1.0以上9.0以下、更に望まし
くは8.0以下2.0以上対2.0以上8.0以下とさ
れる。更に、乳化機による乳化を促進、安定させるため
乳化剤も加えられる。水の添加量は安全性や製造方法な
どによって決定される。例えば、乳化時の酸化剤の溶解
温度を下げるために、水は少なくとも酸化剤に対して外
割で3重量%以上を必要とする。また、乳化混合物と硝
安を主成分とする多孔質粒子を混合する際、例えば乳化
混合物をスプレーしてプリル硝安に添加していく場合、
粘度が大きいとスプレーしても噴霧状態にならないた
め、水の量は酸化剤、油剤及び乳化剤の合計重量に対し
て19倍までの量が必要である。これらの組成であると
き乳化混合物自体は起爆性が低いかあるいは全く起爆性
を示さない。In one preferred embodiment of the present invention, the composition of the emulsified mixture is such that the weight ratio of the oxidizing agent to the oiling agent is 9.0 or less to 1.0 or more, and more preferably 9.
The ratio is from 1.0 to 9.0, more preferably from 2.0 to 8.0, and more preferably from 2.0 to 8.0. Further, an emulsifier is added to promote and stabilize emulsification by an emulsifier. The amount of water to be added is determined by safety, production method, and the like. For example, in order to lower the dissolution temperature of the oxidizing agent at the time of emulsification, water needs to be at least 3% by weight based on the oxidizing agent. Also, when mixing the emulsified mixture and porous particles containing ammonium nitrate as a main component, for example, when adding the emulsion mixture to prill ammonium nitrate by spraying,
If the viscosity is large, the spray does not result in a sprayed state. Therefore, the amount of water must be up to 19 times the total weight of the oxidizing agent, oil agent and emulsifier. With these compositions, the emulsified mixture itself has low or no explosive properties.
【0007】本発明において、乳化混合物は酸素バラン
スがマイナスで硝安粒子に対して燃料の役割を持つが、
酸化剤である硝安粒子に被覆されて耐水性を付与する働
きを有する。また、乳化化合物は起爆性が低いかあるい
は全く起爆性を示さないので、製造上も安全である。乳
化混合物の成分である油剤は、常温では固体で、酸化剤
と反応を開始する温度よりも低い融点を持つものがよ
く、好ましくは融点が50℃から140℃の範囲にある
もの、更に好ましくは融点が60℃から120℃の範囲
にあるものである。そのとき、乳化混合物は、いったん
爆薬として硝安を主成分とする粒子に被覆され造粒され
た後は、爆薬粒子の凝集が防がれ、運搬袋、装填機の金
属容器などへの付着が防がれる。In the present invention, the emulsified mixture has a negative oxygen balance and plays a role of fuel for ammonium nitrate particles.
It has a function of imparting water resistance by being coated with ammonium nitrate particles as an oxidizing agent. In addition, the emulsified compound has low or no explosive property and is safe in production. The oil agent which is a component of the emulsified mixture is solid at ordinary temperature and preferably has a melting point lower than the temperature at which the reaction with the oxidizing agent starts, and preferably has a melting point in the range of 50 ° C to 140 ° C, more preferably It has a melting point in the range of 60 ° C to 120 ° C. At that time, once the emulsified mixture is coated and granulated with particles mainly composed of ammonium nitrate as an explosive, the agglomeration of the explosive particles is prevented, and the adhesion to the transport bag, the metal container of the loading machine, etc. is prevented. Can come off.
【0008】硝安を主成分とする多孔質粒子は、硝酸ア
ンモニウムのみからなるものでもよく、または硝酸アン
モニウムを主成分として硝酸ナトリウム、硝酸カリウ
ム、硝酸カルシウム、硫酸カリウム等の無機塩を含有す
るものであってもよい。また、硝安を主成分とする多孔
質粒子には反応性を向上させる目的で、軽油やニトロ化
合物などの液体燃料を添加することができる。しかし、
乳化混合物が燃料としてプリル硝安表面に被覆されるた
め、酸素バランスや製造上の安全性を考慮して、例えば
硝安油剤爆薬において通常加えられる軽油量6%よりも
低い値にする必要がある。例えば、「Blaster
s’Handbook,17th edition,
p.89,International Societ
y of Explosives Engineer
s,Inc.,Cleveland,1998」には軽
油6重量%をプリル硝安に添加した場合に最大理論エネ
ルギー、最大理論爆轟速度を持つという記載があり、実
際の爆轟速度も6重量%から8重量%に最大値を持つ。
また起爆性に関係する感度についても、2重量%から6
重量%の範囲で感度が高いという記載がある。従って、
本発明において硝安を主成分とする多孔質粒子に軽油を
加える場合は2重量%以下にすることが望ましく、更に
1%以下にすることが望ましい。The porous particles mainly composed of ammonium nitrate may be composed of only ammonium nitrate, or may be composed of ammonium nitrate as a main component and containing inorganic salts such as sodium nitrate, potassium nitrate, calcium nitrate and potassium sulfate. Good. A liquid fuel such as light oil or a nitro compound can be added to the porous particles containing ammonium nitrate as a main component for the purpose of improving the reactivity. But,
Since the emulsified mixture is coated on the surface of prilled nitrate as a fuel, the value must be lower than 6% of the amount of light oil normally added in, for example, an ammonium nitrate explosive in consideration of oxygen balance and production safety. For example, "Blaster
s'Handbook, 17th edition,
p. 89, International Society
y of Explosives Engineer
s, Inc. , Cleveland, 1998 "describes that when 6% by weight of light oil is added to prilled nitrate, it has a maximum theoretical energy and a maximum theoretical detonation speed, and the actual detonation speed also increases from 6% by weight to 8% by weight. Has a value.
In addition, the sensitivity related to the detonation property is from 2% by weight to
There is a description that the sensitivity is high in the range of weight%. Therefore,
In the present invention, when light oil is added to porous particles containing ammonium nitrate as a main component, the content is preferably 2% by weight or less, and more preferably 1% or less.
【0009】本発明の爆薬は、たとえばプリル硝安中の
空隙により、起爆性及び安定爆轟性が与えられる。従っ
て、その場合に乳化混合物とプリル硝安の混合、造粒時
に乳化混合物がプリル硝安内部に浸入してプリル硝安の
空隙を減少させないようにすることが望ましい。例え
ば、水の添加量が多く乳化混合物が容易に硝安を主成分
とする多孔質粒子内部に浸入していく場合は、熱風など
で水を蒸発させながら乳化混合物を徐々に硝安を主成分
とする多孔質粒子に添加し、混合、造粒を行うことが望
ましい。乳化混合物の粘度が高く、乳化混合物が硝安を
主成分とする粒子内部に浸入していかない場合は、例え
ば乳化後直ちに常温か乳化混合物が冷えて混合し難い温
度以上に加温したプリル硝安等と混合、造粒すればよ
い。造粒は、例えば転動造粒装置、流動層造粒装置や複
合型造粒装置を用いて行うことができる。転動造粒装置
では、例えば回転するパンの中に核粒子としてのプリル
硝安を投入し回転運動を起こさせる。そこに乳化混合物
を徐々に添加していく。この乳化混合物が転動するプリ
ル硝安表面に付着し、プリル硝安と一緒に回転する事に
より造粒される。または、あらかじめ乳化混合物とプリ
ル硝安を混合しておき、その混合物を適当なサイズに調
整した後、回転するパンの中に投入し転動させながら造
粒することができる。本発明の爆薬は製造条件を変化さ
せることにより、一粒子のプリル硝安が乳化混合物で被
覆され一爆薬粒子が得られたり、また、数粒子から数十
粒子のプリル硝安が乳化混合物に被覆され集合して一爆
薬粒子とされることができる。例えば、回転パンの中で
回転中のプリル硝安に乳化混合物を徐々に添加していく
場合、乳化混合物の単位時間あたり添加量を少なくし、
プリル硝安の運動を激しくすると、数の少ないプリル硝
安粒子からなる一爆薬粒子が得られる。その他、例えば
混合時の温度や乳化混合物の粘度などによって爆薬粒子
サイズを調整しても良い。The explosive of the present invention is provided with a detonating property and a stable detonation property, for example, by a void in prilled nitrate. Therefore, in that case, it is desirable to prevent the emulsified mixture from entering the inside of the prilled ammonium nitrate and reducing the voids of the prilled ammonium nitrate during mixing and granulation of the emulsified mixture and prilled ammonium nitrate. For example, when a large amount of water is added and the emulsified mixture easily penetrates into the interior of the porous particles mainly composed of ammonium nitrate, the emulsified mixture is gradually composed mainly of ammonium nitrate while evaporating water with hot air or the like. It is desirable to add, mix and granulate the porous particles. When the viscosity of the emulsified mixture is high and the emulsified mixture does not penetrate into the particles mainly composed of ammonium nitrate, for example, immediately after emulsification, the mixture is cooled to room temperature or the temperature at which the emulsified mixture is cooled and hardly mixed. What is necessary is just to mix and granulate. Granulation can be performed using, for example, a rolling granulator, a fluidized bed granulator, or a composite granulator. In a tumbling granulator, for example, prill nitrate as core particles is put into a rotating pan to cause a rotating motion. The emulsified mixture is gradually added thereto. This emulsified mixture adheres to the surface of the rolling prill nitrate, and is granulated by rotating together with the prill nitrate. Alternatively, the emulsified mixture and prill nitrate are mixed in advance, the mixture is adjusted to an appropriate size, and then the mixture is poured into a rotating pan and granulated while being rolled. By changing the manufacturing conditions, the explosive of the present invention obtains one explosive particle by coating one particle of prill nitrate with the emulsified mixture, or collects several particles to several tens of particles of prill ammonium nitrate by coating the emulsified mixture. Can be used as a single explosive particle. For example, when gradually adding the emulsified mixture to the rotating prill nitrate in a rotating pan, reduce the amount of the emulsified mixture added per unit time,
When the exercise of prill nitrate is increased, one explosive particle consisting of a small number of prill nitrate particles is obtained. In addition, the explosive particle size may be adjusted by, for example, the temperature at the time of mixing or the viscosity of the emulsified mixture.
【0010】本発明の爆薬には、乳化混合物に比重調整
剤として、ガラスマイクロバルーンや有機中空粒子など
を加えることができる。また、本発明の爆薬には造粒
時、または製造後、凝集や付着をしない様に、カーボン
ブラック、シリカやタルクなどの耐ブロッキング剤を添
加することができる。また、帯電防止性を向上、付加す
る目的でカーボンブラックや界面活性剤などの帯電防止
物質を添加することができる。また、エネルギー向上剤
として、アルミニウム粉やマグネシウム粉などの金属粉
などを添加することができる。In the explosive of the present invention, glass microballoons, organic hollow particles and the like can be added to the emulsified mixture as a specific gravity adjusting agent. The explosive of the present invention may contain an anti-blocking agent such as carbon black, silica or talc so as not to cause aggregation or adhesion during granulation or after production. Further, an antistatic substance such as carbon black or a surfactant can be added for the purpose of improving and adding the antistatic property. Further, metal powder such as aluminum powder and magnesium powder can be added as an energy improver.
【0011】[0011]
【発明の実施の形態】実施例及び比較例によって本発明
をさらに詳細に説明する。実施例及び比較例にて行う評
価方法を以下に示す。The present invention will be described in more detail with reference to Examples and Comparative Examples. The evaluation methods performed in Examples and Comparative Examples are shown below.
【0012】[0012]
【評価法1】 重袋付着確認試験 粒状爆薬の重袋への付着状況を評価するために、爆薬5
kgを15リットルのナイロン袋に詰め込み封をし、段
ボールに梱包後1週間保管した。その後、爆薬をナイロ
ン袋より取り出し、内径19mmφの導電性ホースを底
部に取り付けた30cm×30cm×30cmのステン
レス容器に移した。この後、ナイロン袋への爆薬の付着
状況を確認した。[Evaluation method 1] Heavy bag adhesion confirmation test In order to evaluate the state of adhesion of granular explosives to heavy bags, explosives 5
kg was packed in a 15 liter nylon bag, sealed, packed in cardboard, and stored for one week. Thereafter, the explosive was taken out of the nylon bag and transferred to a 30 cm × 30 cm × 30 cm stainless steel container equipped with a conductive hose having an inner diameter of 19 mmφ at the bottom. Thereafter, the state of attachment of the explosive to the nylon bag was confirmed.
【0013】[0013]
【評価法2】 ステンレス容器付着確認試験 評価法1の爆薬が入ったステンレス容器を加圧し、爆薬
を全て導電性ホースより排出した。この後、ステンレス
容器への爆薬の付着状況を確認した。更に、ステンレス
容器またはホースに爆薬が付着している場合は、水で流
したり、水で洗い流せない場合は界面活性剤などの洗浄
剤で洗浄した。[Evaluation method 2] Stainless steel container adhesion confirmation test The stainless steel container containing the explosive of Evaluation method 1 was pressurized, and all the explosive was discharged from the conductive hose. Thereafter, the state of attachment of the explosive to the stainless steel container was confirmed. Further, when explosives were attached to the stainless steel container or hose, the explosives were flushed with water. If the explosives could not be washed out with water, the explosives were washed with a detergent such as a surfactant.
【0014】[0014]
【評価法3】 耐水試験 評価法2でステンレス容器から排出された爆薬を、径2
mmの穴が12個ランダムに開いた鋼管(内径35mm
×長さ350mm、片方は密閉)に密に詰め、鋼管の開
いている一端を2号榎ダイナマイト30gで塞ぎ、一時
間水中に漬けた。その後水中より取り出し、ダイナマイ
トに6号電気雷管を装着して起爆するかしないかを確認
した[Evaluation method 3] Water resistance test
12mm holes randomly opened steel pipe (inner diameter 35mm
× 350 mm in length, one of which is sealed), the open end of the steel pipe was closed with 30 g of No. 2 Enoki dynamite, and immersed in water for one hour. After that, it was taken out of the water, and a No. 6 electric detonator was attached to the dynamite to check whether it would detonate.
【0015】[0015]
【実施例1】硝酸アンモニウム58重量%、硝酸ナトリ
ウム7重量%、水4重量%、乳化剤(花王(株)製−商
品名:エキセル300)9重量%、油剤(日本精蝋製−
商品名:Hi−Mic2095)22重量%を乳化機を
用いて乳化した。乳化後直ちにその乳化混合物2kgと
常温のプリル硝安5kgをアルミニウム製パンの中で迅
速に混合し、その混合物を目開き3.35mmのメッシ
ュを通して押しだし、回転数40r.p.m.で回転中
のステンレス製回転パンの中に投入した。ステンレス製
パンの中に25℃の乾燥空気(75立米/時)を送りな
がら冷却し、1mmから5mm粒状爆薬を得た。また、
造粒中に凝集防止のためタルク60gを添加した。得ら
れた爆薬を上記評価法にて評価した。結果を表1に示
す。EXAMPLE 1 58% by weight of ammonium nitrate, 7% by weight of sodium nitrate, 4% by weight of water, 9% by weight of an emulsifier (trade name: EXCEL 300 manufactured by Kao Corporation), an oil agent (manufactured by Nippon Seiro Co., Ltd.)
(Trade name: Hi-Mic 2095) 22% by weight was emulsified using an emulsifier. Immediately after the emulsification, 2 kg of the emulsified mixture and 5 kg of prilled ammonium nitrate at room temperature are rapidly mixed in an aluminum pan, and the mixture is extruded through a mesh having an aperture of 3.35 mm and rotated at 40 rpm. p. m. And put into a rotating stainless steel pan. Cooling was performed while feeding dry air (75 cubic meters / hour) at 25 ° C. into a stainless steel pan to obtain a granular explosive of 1 to 5 mm. Also,
During granulation, 60 g of talc was added to prevent aggregation. The obtained explosive was evaluated by the above evaluation method. Table 1 shows the results.
【0016】[0016]
【実施例2】硝酸アンモニウム58重量%、硝酸ナトリ
ウム7重量%、水4重量%、乳化剤(花王(株)製−商
品名:エキセル300)9重量%、油剤(日本精蝋製−
商品名:Hi−Mic2095)22重量%を乳化機を
用いて乳化した。乳化後直ちにこの乳化混合物2kgと
ガラスマイクロバルーン100g混合し、更に常温のプ
リル硝安5kgとアルミニウム製パンの中で迅速に混合
した。その混合物を目開き3.35mmのメッシュを通
して押しだし、回転数40r.p.m.で回転中のステ
ンレス製回転パンの中に投入した。ステンレス製パンの
中に25℃の乾燥空気(75立米/時)を送りながら冷
却し、1mmから5mm粒状爆薬を得た。また、造粒中
に凝集防止のためタルク60gを添加した。得られた爆
薬を上記評価法にて評価した。結果を表1に示す。Example 2 Ammonium nitrate 58% by weight, sodium nitrate 7% by weight, water 4% by weight, emulsifier (manufactured by Kao Corporation-trade name: Exel 300) 9% by weight, oil agent (Nippon Seiro-
(Trade name: Hi-Mic 2095) 22% by weight was emulsified using an emulsifier. Immediately after the emulsification, 2 kg of this emulsified mixture was mixed with 100 g of glass microballoons, and further rapidly mixed with 5 kg of prilled ammonium nitrate at room temperature in an aluminum pan. The mixture was extruded through a mesh having an opening of 3.35 mm and rotated at 40 rpm. p. m. And put into a rotating stainless steel pan. Cooling was performed while feeding dry air (75 cubic meters / hour) at 25 ° C. into a stainless steel pan to obtain a granular explosive of 1 to 5 mm. During granulation, 60 g of talc was added to prevent aggregation. The obtained explosive was evaluated by the above evaluation method. Table 1 shows the results.
【0017】[0017]
【実施例3】硝酸アンモニウム35重量%、硝酸ナトリ
ウム4重量%、水40重量%、乳化剤(花王(株)製−
商品名:エキセル300)6重量%、油剤(日本精蝋製
−商品名:Hi−Mic2095)15重量%を乳化機
を用いて乳化した。この乳化混合物3.5kgを、90
g/minから180g/minの添加量でステンレス
製回転パン(回転数40r.p.m.)の中で回転中の
プリル硝安5kgに添加していき、1mmから5mm粒
状爆薬を得た。なお、造粒中添加される乳化混合物の温
度は80℃で、100℃の乾燥空気(100立米/時)
をパンの中に送りながらプリル硝安を80℃から100
℃に保った。また、造粒中に凝集防止のためタルク60
gを添加した。得られた爆薬を上記評価法にて評価し
た。結果を表1に示す。Example 3 Ammonium nitrate 35% by weight, sodium nitrate 4% by weight, water 40% by weight, emulsifier (manufactured by Kao Corporation)
6% by weight of trade name: Exel 300) and 15% by weight of an oil agent (manufactured by Nippon Seiwa Co., Ltd .; trade name: Hi-Mic 2095) were emulsified using an emulsifier. 3.5 kg of this emulsified mixture is
It was added to 5 kg of prill nitrate rotating in a stainless steel rotating pan (rotation speed 40 rpm) at an addition amount of g / min to 180 g / min to obtain a granular explosive of 1 mm to 5 mm. The temperature of the emulsified mixture added during granulation is 80 ° C., and dry air at 100 ° C. (100 cubic meters / hour)
Prill nitrate from 80 ° C to 100
C. In addition, talc 60 is used to prevent agglomeration during granulation.
g was added. The obtained explosive was evaluated by the above evaluation method. Table 1 shows the results.
【0018】[0018]
【実施例4】硝酸アンモニウム7.8重量%、硝酸ナト
リウム0.7重量%、水87重量%、乳化剤(花王
(株)製−商品名:エマルゲン106)1重量%、油剤
(日本精蝋製−商品名:Hi−Mic2095)3.5
重量%を乳化機を用いて乳化した。この乳化混合物16
kgを、60g/minから130g/minの添加量
でステンレス製回転パン(回転数40r.p.m.)の
中で回転中のプリル硝安5kgに添加していき、1mm
から5mm粒状爆薬を得た。なお、造粒中添加される乳
化混合物の温度は90℃で、100℃の乾燥空気(10
0立米/時)をパンの中に送りながらプリル硝安を90
℃から100℃に保った。また、造粒中に凝集防止のた
めタルク60gを添加した。得られた爆薬を上記評価法
にて評価した。結果を表1に示す。Example 4 7.8% by weight of ammonium nitrate, 0.7% by weight of sodium nitrate, 87% by weight of water, 1% by weight of an emulsifier (trade name: Emulgen 106, manufactured by Kao Corporation) (Product name: Hi-Mic2095) 3.5
% By weight was emulsified using an emulsifier. This emulsified mixture 16
kg was added to 5 kg of rotating prill nitrate in a stainless steel rotating pan (rotation speed 40 rpm) at an addition amount of 60 g / min to 130 g / min, and 1 mm
To obtain a 5 mm granular explosive. The temperature of the emulsified mixture added during granulation is 90 ° C.
0 p.m./hour) into the bread and prill nitrate 90
C. to 100.degree. During granulation, 60 g of talc was added to prevent aggregation. The obtained explosive was evaluated by the above evaluation method. Table 1 shows the results.
【0019】[0019]
【実施例5】硝酸アンモニウム58重量%、硝酸ナトリ
ウム7重量%、水4重量%、乳化剤(花王(株)製−商
品名:エキセル300)9重量%、油剤(日本精蝋製−
商品名:Hi−Mic2095)22重量%を乳化機を
用いて乳化した。乳化後直ちにこの乳化混合物2kgと
ガラスマイクロバルーン100g混合し、更に予め軽油
1.5%を混合した常温のプリル硝安5kgとアルミニ
ウム製パンの中で迅速に混合した。その混合物を目開き
3.35mmのメッシュを通して押しだし、回転数40
r.p.m.で回転中のステンレス製回転パンの中に投
入した。ステンレス製パンの中に25℃の乾燥空気(7
5立米/時)を送りながら冷却し、1mmから5mm粒
状爆薬を得た。また、造粒中に凝集防止のためタルク6
0gを添加した。得られた爆薬を上記評価法にて評価し
た。結果を表1に示す。Example 5 Ammonium nitrate 58% by weight, sodium nitrate 7% by weight, water 4% by weight, emulsifier (manufactured by Kao Corporation-trade name: Exel 300) 9% by weight, oil agent (manufactured by Nippon Seiro)
(Trade name: Hi-Mic 2095) 22% by weight was emulsified using an emulsifier. Immediately after the emulsification, 2 kg of the emulsified mixture was mixed with 100 g of glass microballoons, and further rapidly mixed with 5 kg of prilled ammonium nitrate at room temperature previously mixed with 1.5% of light oil in an aluminum pan. The mixture was extruded through a 3.35 mm mesh and the number of rotations was 40.
r. p. m. And put into a rotating stainless steel pan. Dry air at 25 ° C (7
(5 cubic meters / hour) while cooling to obtain 1 to 5 mm granular explosives. In addition, talc 6 is used to prevent agglomeration during granulation.
0 g was added. The obtained explosive was evaluated by the above evaluation method. Table 1 shows the results.
【0020】[0020]
【比較例1】硝酸アンモニウム70重量%、硝酸ナトリ
ウム10重量%、水13重量%、乳化剤(花王(株)製
−商品名:エキセル300)2重量%、油剤(日本精蝋
製−商品名:Hi−Mic2095)5重量%、ガラス
マイクロバルーン5重量%(外割)を乳化機にて乳化し
エマルション爆薬を得た。その爆薬を上記評価法にて評
価した。結果を表1に示す。Comparative Example 1 Ammonium nitrate 70% by weight, sodium nitrate 10% by weight, water 13% by weight, emulsifier (manufactured by Kao Corporation-trade name: Exel 300) 2% by weight, oil agent (manufactured by Nippon Seiwa-trade name: Hi) -Mic 2095) and 5% by weight of glass microballoons (outer part) were emulsified by an emulsifier to obtain an emulsion explosive. The explosive was evaluated by the above evaluation method. Table 1 shows the results.
【0021】[0021]
【比較例2】プリル硝安94重量%、軽油6重量%をア
ルミ製パンの中で混合し硝安油剤爆薬を得た。その爆薬
を上記評価法にて評価した。結果を表1に示す。COMPARATIVE EXAMPLE 2 94% by weight of prill nitrate and 6% by weight of light oil were mixed in an aluminum pan to obtain an ammonium nitrate explosive. The explosive was evaluated by the above evaluation method. Table 1 shows the results.
【0022】[0022]
【表1】 [Table 1]
【0023】重袋付着確認試験 付着なし :○ 付着あり、洗浄液にて洗浄を要する :× ステンレス容器付着確認試験 付着なし :○ 付着あり、洗浄液にて洗浄を要する :× 耐水試験 起爆可能 :○ 起爆不可能 :×Heavy bag adhesion confirmation test No adhesion: ○ Adhesion required, cleaning with washing liquid: × Stainless steel container adhesion confirmation test No adhesion: ○ Adhesion, cleaning required with cleaning liquid: × Water resistance test Explosion possible: ○ Explosion Impossible: ×
【0024】表1から、実施例の爆薬はいずれも重袋及
びステンレス容器等に付着しなかった。また耐水試験で
も起爆することができた。比較例1の爆薬は重袋及びス
テンレス容器等に付着し、洗浄には洗浄液を必要とし困
難な作業であった。比較例2の爆薬は重袋、ステンレス
容器等に付着しなかったが、耐水性はなかった。以上か
ら、本発明の粒状爆薬は、重袋や金属容器等への付着が
なく、作業効率、装薬時の安全性、付着残留薬の問題な
どを改善することができることが分かった。From Table 1, none of the explosives of the examples adhered to the heavy bags and the stainless steel containers. In addition, it was able to detonate in the water resistance test. The explosive of Comparative Example 1 adhered to heavy bags, stainless steel containers, etc., and required a cleaning liquid for cleaning, which was a difficult operation. The explosive of Comparative Example 2 did not adhere to heavy bags, stainless steel containers, etc., but did not have water resistance. From the above, it has been found that the granular explosive of the present invention does not adhere to heavy bags, metal containers, and the like, and can improve work efficiency, safety at the time of charging, problems of residual drug adhered, and the like.
【0025】[0025]
【発明の効果】本発明は、油剤、酸化剤及び水からなる
乳化混合物をプリル硝安等の粒子表面に被覆して粒状爆
薬を得ることにより、重袋や金属容器等への付着がな
く、作業効率、装薬時の安全性、付着残留薬の問題など
を改善することができる。According to the present invention, a granular explosive is obtained by coating an emulsified mixture comprising an oil agent, an oxidizing agent and water on the surface of particles such as prilled nitrate, so that it does not adhere to heavy bags, metal containers, etc. Efficiency, safety at the time of charging, and problems of residual drug adhesion can be improved.
Claims (3)
油剤、酸化剤、水及び乳化剤からなる乳化混合物によっ
て被覆されており、乳化混合物の組成は、酸化剤と油剤
の重量比が9.0以下対1.0以上であることを特徴と
する粒状爆薬。1. The surface of a porous particle mainly composed of ammonium nitrate is coated with an emulsified mixture comprising an oil agent, an oxidizing agent, water and an emulsifier, and the composition of the emulsified mixture is such that the weight ratio of the oxidizing agent to the oil agent is 9%. A granular explosive characterized in that the ratio is not more than 0.0 to not less than 1.0.
量比が9.0以下1.0以上対1.0以上9.0以下で
ある請求項1に記載の爆薬。2. The explosive according to claim 1, wherein the composition of the emulsified mixture has a weight ratio of the oxidizing agent to the oil agent of 1.0 or more to 9.0 or less and 1.0 or more to 9.0 or less.
含有する請求項1に記載の爆薬。3. The explosive according to claim 1, wherein the porous particles mainly composed of ammonium nitrate contain a fuel.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11225699A JP2001048689A (en) | 1999-08-09 | 1999-08-09 | Granular explosive powder |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11225699A JP2001048689A (en) | 1999-08-09 | 1999-08-09 | Granular explosive powder |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JP2001048689A true JP2001048689A (en) | 2001-02-20 |
Family
ID=16833421
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP11225699A Pending JP2001048689A (en) | 1999-08-09 | 1999-08-09 | Granular explosive powder |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2001048689A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
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| US7645351B2 (en) * | 2003-11-04 | 2010-01-12 | Nof Corporation | Explosive material composition and method for preparing the same |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7645351B2 (en) * | 2003-11-04 | 2010-01-12 | Nof Corporation | Explosive material composition and method for preparing the same |
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