JP3374709B2 - Separation method and apparatus for granulated slag in waste melting furnace - Google Patents

Separation method and apparatus for granulated slag in waste melting furnace

Info

Publication number
JP3374709B2
JP3374709B2 JP18977097A JP18977097A JP3374709B2 JP 3374709 B2 JP3374709 B2 JP 3374709B2 JP 18977097 A JP18977097 A JP 18977097A JP 18977097 A JP18977097 A JP 18977097A JP 3374709 B2 JP3374709 B2 JP 3374709B2
Authority
JP
Japan
Prior art keywords
slag
solidified
melting furnace
granulated
water
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.)
Expired - Lifetime
Application number
JP18977097A
Other languages
Japanese (ja)
Other versions
JPH1133529A (en
Inventor
修 荒木
裕之 卯西
展夫 高須
直 中村
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
JFE Engineering Corp
Original Assignee
JFE Engineering Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by JFE Engineering Corp filed Critical JFE Engineering Corp
Priority to JP18977097A priority Critical patent/JP3374709B2/en
Publication of JPH1133529A publication Critical patent/JPH1133529A/en
Application granted granted Critical
Publication of JP3374709B2 publication Critical patent/JP3374709B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

  • Processing Of Solid Wastes (AREA)
  • Curing Cements, Concrete, And Artificial Stone (AREA)
  • Gasification And Melting Of Waste (AREA)

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、一般ごみや産業廃
棄物を直接溶融する廃棄物溶融炉において、この溶融炉
から出滓された溶融物を処理する廃棄物溶融炉の水砕ス
ラグの分別方法及び分別装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a waste melting furnace for directly melting general waste and industrial waste, and a granulated slurry of the waste melting furnace for treating the melt discharged from the melting furnace.
TECHNICAL FIELD The present invention relates to a lug sorting method and a sorting apparatus .

【0002】[0002]

【従来の技術】従来、廃棄物溶融炉から排出される溶融
物の処理装置として、例えば、図2に示すものがある
(特開平8−187485)。これでは、溶融炉1の開
放された出滓口2の下方に、溶融物3を水砕固化すろ水
砕装置4が設置されている。水砕装置4内に堆積した固
化物5を水中からかき上げた後、スラグの固化物6とメ
タルの固化物7に分離するための、回転ドラム式磁選機
8が接続されている。
2. Description of the Related Art Conventionally, there is, for example, an apparatus for treating a melt discharged from a waste melting furnace as shown in FIG. 2 (JP-A-8-187485). Here, below the open outlet port 2 of the melting furnace 1, a water granulation device 4 for granulating and solidifying the melt 3 is installed. A rotary drum type magnetic separator 8 is connected to scrape the solidified material 5 accumulated in the water granulator 4 from water and then separate it into a solidified material 6 of slag and a solidified material 7 of metal.

【0003】溶融炉1から常時出滓された溶融物3は、
水砕装置4中の水9中に落下する。水9中で急冷されて
細粒化した固化物5は、水中からかき出ずために設置さ
れたコンベア10上に沈降し、その下流に設置された回
転ドラム式磁選機8に供給される。メタルの固化物7は
磁性を示すため、ドラム11内に装備された永久磁石1
2に吸引されてドラム表面13に吸着すると共に、非磁
性のスラグの固化物6は比較的高速で回転するドラム1
1の遠心力によって飛ばされる。また、回転ドラム式磁
選機8のドラム表面13に吸着されたメタルの固化物7
は、ドラム表面13に近接して設置されたスクレーパ1
4によつてドラム表面から掻き取られる。こうした一連
のプロセスによって、スラグの固化物6とメタルの固化
物7に分別され、スラグの固化物6は路盤材や骨材など
に再利用される。
The melt 3 constantly discharged from the melting furnace 1 is
It falls into the water 9 in the water granulator 4. The solidified product 5 that has been rapidly cooled in water 9 and made into fine particles settles on a conveyor 10 installed so as not to be scratched out from the water, and is supplied to a rotary drum type magnetic separator 8 installed downstream thereof. Since the solidified metal 7 exhibits magnetism, the permanent magnet 1 installed in the drum 11
The non-magnetic slag solidified product 6 is attracted to the drum surface 13 and adsorbed to the drum surface 13, and the nonmagnetic slag solidified product 6 rotates at a relatively high speed.
It is blown away by the centrifugal force of 1. In addition, solidified metal 7 adsorbed on the drum surface 13 of the rotary drum type magnetic separator 8
Is a scraper 1 installed close to the drum surface 13.
4 scraped off the drum surface. Through such a series of processes, the solidified product 6 of slag and the solidified product 7 of metal are separated, and the solidified product 6 of slag is reused as a roadbed material or an aggregate.

【0004】[0004]

【発明が解決しようとする課題】ここで、実際に水砕し
た溶融物を観察してみると、メタルの固化物はスラグの
固化物に比して粒径の大きいものが多い。粒径の大きい
メタルの固化物は他に比して磁選機に強く吸着され、磁
選機のドラム表面を覆ってしまう。それゆえ、粒径の小
さいメタル分は十分な吸引力が得られず、高速で回転す
るドラムの遠心力によって磁選機から振るい落とされて
しまう。ドラムに吸着しない固化物は、再利用を目的と
して回収されるスラグに不純物として混入する結果とな
り、これを回避するためには、吸着面が広い磁選機を導
入するか、ドラムの回転数を遅くして遠心力を低下させ
る必要がある。しかし、これによって装置の大型化もし
くは処理能力の低下は免れない。
Here, when observing the molten product that is actually granulated by water, the solidified product of metal often has a larger particle size than the solidified product of slag. A solidified product of a metal having a large particle size is more strongly adsorbed by the magnetic separator and covers the drum surface of the magnetic separator. Therefore, a sufficient amount of suction force cannot be obtained for the metal particles having a small particle diameter, and the metal component is shaken off from the magnetic separator due to the centrifugal force of the drum rotating at a high speed. Solidified substances that do not adsorb to the drum result in being mixed as impurities into the slag that is recovered for the purpose of reuse.To avoid this, either introduce a magnetic separator with a wide adsorption surface, or slow down the rotation speed of the drum. Therefore, it is necessary to reduce the centrifugal force. However, this inevitably increases the size of the device or decreases the processing capacity.

【0005】本発明は、上記の従来技術の問題点に鑑み
てなされたもので、水砕された粒体固化物からメタル分
を効率良く除去し、高品質なスラグを安定して回収する
ための廃棄物溶融炉の水砕スラグの分別方法及び分別装
置を提供することを目的とする。
The present invention has been made in view of the above problems of the prior art. In order to efficiently remove the metal component from the granulated solidified product of water and to stably recover high quality slag. Method and equipment for water granulated slag in waste melting furnace in Japan
The purpose is to provide storage .

【0006】[0006]

【課題を解決するための手段】請求項1の発明は、廃棄
物を直接溶融する溶融炉からの出滓溶融物の処理におい
て、スラグとメタルよりなる溶融物を水中で冷却して粒
化した固化物を生成し、粒化した固化物をその粒径によ
って細粒と粗粒の2段階に分別しながら、粒化した固化
物のうちスラグの固化物を細粒化して細粒側に分別し、
更に細粒の固化物のみを磁選してメタルの固化物を除去
することによって、スラグの固化物を効率よく回収する
ことを特徴とする廃棄物溶融炉の水砕スラグの分別方法
である。
According to a first aspect of the present invention, in the processing of molten slag from a melting furnace that directly melts waste, the molten material consisting of slag and metal is cooled in water to form particles.
It generates a phased solidified product, while fractionating solidified product was granulated in two stages of fine and coarse particles by the particle size, solidified and granulated
Of the things, the solidified product of slag is finely divided and separated into fine particles,
Furthermore, a method for separating granulated slag in a waste melting furnace, characterized in that the solidified product of slag is efficiently recovered by magnetically separating only the solidified product of fine particles to remove the solidified product of metal Is.

【0007】また、請求項2の発明は、廃棄物を直接溶
融する溶融炉からの出滓溶融物の処理において、廃棄物
の溶融炉の出滓口の下方に設置した水砕装置と、水中か
ら掻き出された固化物を粒径によって細粒、粗粒の2段
階に分別しながら、粒化した固化物のうちスラグの固化
物を細粒化して細粒側に分別する粒径選別機と、粒径選
別機により分別された細粒側に設置された磁選機とによ
って構成される廃棄物溶融炉の溶融物の水砕スラグの分
別装置である。
Further, in the invention of claim 2, in the treatment of slag melt from a melting furnace for directly melting waste, a water granulating device installed below the slag opening of the waste melting furnace and an underwater The slag is solidified from the granulated solidified material while separating the solidified material scraped out from the granulated material into two stages of fine particles and coarse particles.
And grain径選another machine for sorting objects to be comminuted to a fine particle side, particle径選
It is a device for separating water granulated slag of a melt of a waste melting furnace, which is composed of a magnetic separator installed on the fine grain side separated by a separate machine .

【0008】[0008]

【発明の実施の形態】本発明では、水砕された固化物の
うち、メタル分の多くは粒径の大きい粒として固化し、
一方スラグは細粒化の度合いが高く、強度的にもろい事
もあって粒径の小さい粒となるという知見に基づいてな
されたものである。
BEST MODE FOR CARRYING OUT THE INVENTION In the present invention, most of the metal content of the water-solidified solidified product is solidified as large-sized particles,
On the other hand, slag is made based on the finding that the degree of grain refinement is high and the strength is brittle, so that the grain size becomes small.

【0009】以下に本発明の実施の形態の一例を図1に
より説明する。廃棄物の溶融炉1の下方に常時開放され
た出滓口2から、連続的に出滓された溶融物3は、水砕
装置4の水9中に落下する。溶融物3は水中で急冷さ
れ、粒化した固化物5となる。
An example of an embodiment of the present invention will be described below with reference to FIG. From the slag port 2 that is always opened below the waste melting furnace 1, the continuously smelted melt 3 falls into the water 9 of the water granulation device 4. The melt 3 is rapidly cooled in water to become a granulated solidified product 5.

【0010】固化物5は、沈降し、固形物を連続的に搬
出するコンベア10上に落下して、水9中からかき出さ
れる。搬出された固化物5は、その下流にある粒径選別
機15例えば振動篩やトロンメル型回転篩などで、細粒
と粗粒の2種類に選別される。このとき、粒径選別機中
の篩16の振動や回転によって、強度的にもろいスラグ
の固形物7は更に細粒化が進み、結果として篩16を通
過する。
The solidified material 5 settles, falls onto a conveyor 10 for continuously carrying out solid material, and is scraped out of the water 9. The solidified product 5 carried out is sorted into two types, that is, fine particles and coarse particles, by a particle size selector 15 located downstream thereof, for example, a vibrating screen or a trommel type rotary screen. At this time, due to the vibration and rotation of the sieve 16 in the particle size sorter, the solid slag solid 7 that is fragile in strength is further refined, and as a result, passes through the sieve 16.

【0011】固形物の粒径は、溶融対象の廃棄物の質、
溶融炉の運転条件、および水砕の条件によって異なる。
このため粒径分別の境界粒径は、例えば1〜10mmの
間でこれらの条件を加味して設定する。篩16を通過で
きない固形物は、粒径の大きいメタルの粒18であるの
で、通路17を通ってメタル用受け容器19に収納され
る。
The particle size of the solids depends on the quality of the waste to be melted,
It depends on the operating conditions of the melting furnace and the conditions of water granulation.
Therefore, the boundary grain size for grain size separation is set, for example, in the range of 1 to 10 mm in consideration of these conditions. The solid material that cannot pass through the sieve 16 is the metal particles 18 having a large particle diameter, and thus is stored in the metal receiving container 19 through the passage 17.

【0012】篩16を通過した固形物中には、スラグの
固形物6と水砕の段階で細粒となったメ夕ルの固形物7
が共に含まれていろ。メタルの固形物7は磁性体である
ので、篩16の後段に設置した磁選機8によって最終的
に分別される。磁選機8には、ここで図示した回転ドラ
ム型以外にも、コンベア型や他の公知の物を用いる事が
できる。磁選機8によって分別された固形物は、それぞ
れメタル用受け容器19、スラグ用受け容器2Oに収納
される。
In the solid matter that has passed through the sieve 16, the solid matter 6 of the slag and the solid matter 7 of the fine granules that have become fine particles at the stage of water granulation.
Should be included together. Since the solid metal 7 is a magnetic substance, it is finally separated by the magnetic separator 8 installed in the latter stage of the sieve 16. The magnetic separator 8 may be a conveyor type or any other known type other than the rotary drum type shown here. The solids separated by the magnetic separator 8 are stored in a metal receiving container 19 and a slag receiving container 20 respectively.

【0013】(実施例)図1は本発明の1実施例であ
る。溶融炉1の下方に常時開放された出滓口2から、連
続的に出滓された溶融物3は、水砕装置4の水9中に落
下する。溶融物3は水中で急冷され、細粒化した固化物
5になろ。固化物5は、水中からかき出すために設置さ
れたコンベア10上に沈降し、その下流にある粒径選別
機である振動篩15で細粒と粗粒の2段階に分けられ
る。
(Embodiment) FIG. 1 shows an embodiment of the present invention. From the slag port 2 which is always opened below the melting furnace 1, the continuously melted melt 3 falls into the water 9 of the water granulation device 4. The melt 3 is rapidly cooled in water to form a solidified product 5 which has been made into fine particles. The solidified product 5 is settled on a conveyor 10 installed to scrape it out of water, and is divided into two stages of fine particles and coarse particles by a vibrating screen 15 which is a particle size selector located downstream thereof.

【0014】また、投入前には粗粒の固形物5であって
も、強度的にもろいスラグであれば、振動で割れや欠け
が生じて細粒化が進み、結果的に篩16を通過する。固
形物の粒径は、溶融対象の廃棄物の質、溶融炉の運転条
件、および水砕の条件によって異なるため、粒径分別の
境界粒径は1〜10mmの範囲でこれらの条件を加味し
て設定する。篩16を通過できない粗粒のメタル固形物
18は、この段階で通路17を経てメタル用受け18容
器に収納される。
Further, even if the solid material 5 is a coarse particle before being charged, if the slag is brittle in terms of strength, cracking or chipping occurs due to vibration, and the particle is further refined, resulting in passing through the sieve 16. To do. Since the particle size of solids varies depending on the quality of the waste to be melted, the operating conditions of the melting furnace, and the conditions of water granulation, the boundary particle size for particle size separation is 1 to 10 mm. To set. Coarse-grained metal solids 18 that cannot pass through the sieve 16 are stored in the metal receiving container 18 via the passage 17 at this stage.

【0015】篩16を通過した固形物中には、スラグの
固形物6と細粒のメタルの固形物7が共に含まれてお
り、篩16の後段に設置したドラム回転型磁選機8によ
って最終的な分別を行なう。ドラム回転型磁選機8は、
軸20を中心として回転可能なドラム11と、ドラムの
内部に装備された永久磁石12と、粒体の固形物5をド
ラム11に供給するフィーダ21と、ドラム11に近接
して設置されたスクレー.パ14で構成される。フィー
ダ21によってドラム表面13に供給された固形物のう
ち、ドラム11内の永久磁石12に吸着されない非磁性
のスラグ分は、ドラム11の回転に伴う遠心力によって
飛ばされ、スラグ用受け容器2Oに回収される。一方、
磁性体であろメタルの固形物7はドラム13表面に吸着
され、さらにスクレーパ14によってドラム表面13か
ら引き剥がされ、その下方に設置されたスラグ用受け容
器19に収納される。
The solid matter that has passed through the sieve 16 contains both the slag solid matter 6 and the fine-grained metal solid matter 7. Make a proper separation. The drum rotary type magnetic separator 8
A drum 11 rotatable about a shaft 20, a permanent magnet 12 mounted inside the drum, a feeder 21 for supplying the solid particles 5 to the drum 11, and a scraper installed near the drum 11. . It is composed of a par 14. Of the solid matter supplied to the drum surface 13 by the feeder 21, the non-magnetic slag that is not adsorbed by the permanent magnets 12 in the drum 11 is blown off by the centrifugal force associated with the rotation of the drum 11 and stored in the slag receiving container 2O. Be recovered. on the other hand,
The solid matter 7 of a magnetic metal, which is a magnetic material, is adsorbed on the surface of the drum 13, is peeled off from the drum surface 13 by the scraper 14, and is housed in a slag receiving container 19 installed below the drum.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明の実施の形態の一例の例の説明図。FIG. 1 is an explanatory diagram of an example of an example of an embodiment of the present invention.

【図2】従来の溶融物の処理装置の説明図。FIG. 2 is an explanatory view of a conventional melt processing apparatus.

【符号の説明】[Explanation of symbols]

1…溶融炉、2…出滓口、3…溶融物、4…水砕装置、
6…スラグ、7…メタル、12…磁選機、15…振動篩
(粒径選別機)、16…篩、18…メタル(粒径大)。
DESCRIPTION OF SYMBOLS 1 ... Melting furnace, 2 ... Slag port, 3 ... Melt material, 4 ... Granulating device,
6 ... Slag, 7 ... Metal, 12 ... Magnetic separator, 15 ... Vibrating sieve (particle size selector), 16 ... Sieve, 18 ... Metal (large particle size).

───────────────────────────────────────────────────── フロントページの続き (72)発明者 中村 直 東京都千代田区丸の内一丁目1番2号 日本鋼管株式会社内 (56)参考文献 特開 昭62−172107(JP,A) 特開 平9−59046(JP,A) 特開 平9−59047(JP,A) 特開 昭61−37930(JP,A) (58)調査した分野(Int.Cl.7,DB名) B09B 3/00 - 5/00 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Nao Nakamura 1-2-1, Marunouchi, Chiyoda-ku, Tokyo Inside Nippon Steel Pipe Co., Ltd. (56) Reference JP-A-62-172107 (JP, A) JP-A-9 -59046 (JP, A) JP 9-59047 (JP, A) JP 61-37930 (JP, A) (58) Fields investigated (Int.Cl. 7 , DB name) B09B 3/00- 5/00

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 廃棄物を直接溶融する溶融炉からの出滓
溶融物の処理において、 スラグとメタルよりなる溶融物を水中で冷却して粒化し
た固化物を生成し、粒化した固化物をその粒径によって
細粒と粗粒の2段階に分別しながら、粒化した固化物の
うちスラグの固化物を細粒化して細粒側に分別し、更に
細粒の固化物のみを磁選してメタルの固化物を除去する
ことによって、スラグの固化物を効率よく回収すること
を特徴とする廃棄物溶融炉の水砕スラグの分別方法。
1. In the treatment of slag melt from a melting furnace for directly melting waste, the melt consisting of slag and metal is cooled in water and granulated.
Of the granulated solidified material is generated, and the granulated solidified material is classified into two stages of fine particles and coarse particles according to the particle size.
Among them, the solidified product of slag is finely divided and separated to the fine particle side, and only the solidified product of fine grain is magnetically separated to remove the solidified metal, thereby efficiently recovering the solidified product of slag. Method for separating water granulated slag in a waste melting furnace.
【請求項2】 廃棄物を直接溶融する溶融炉からの出滓
溶融物の処理において、 廃棄物の溶融炉の出滓口の下方に設置した水砕装置と、
水中から掻き出された固化物を粒径によって細粒、粗粒
の2段階に分別しながら、粒化した固化物のうちスラグ
の固化物を細粒化して細粒側に分別する粒径選別機と、
粒径選別機により分別された細粒側に設置された磁選機
とによって構成される廃棄物溶融炉の溶融物の水砕スラ
グの分別装置。
2. In the treatment of slag melt from a melting furnace for directly melting waste, a water granulating device installed below the slag outlet of the waste melting furnace,
The slag of the granulated solidified matter is separated into two stages of finely divided and coarsely divided solidified matter scraped out from water according to the particle size.
A particle size sorter that atomizes the solidified product of and separates it into fine particles ,
An apparatus for separating water granulated slag from a melt in a waste melting furnace, which is composed of a magnetic separator installed on the fine grain side separated by a particle size selector .
JP18977097A 1997-07-15 1997-07-15 Separation method and apparatus for granulated slag in waste melting furnace Expired - Lifetime JP3374709B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP18977097A JP3374709B2 (en) 1997-07-15 1997-07-15 Separation method and apparatus for granulated slag in waste melting furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18977097A JP3374709B2 (en) 1997-07-15 1997-07-15 Separation method and apparatus for granulated slag in waste melting furnace

Publications (2)

Publication Number Publication Date
JPH1133529A JPH1133529A (en) 1999-02-09
JP3374709B2 true JP3374709B2 (en) 2003-02-10

Family

ID=16246910

Family Applications (1)

Application Number Title Priority Date Filing Date
JP18977097A Expired - Lifetime JP3374709B2 (en) 1997-07-15 1997-07-15 Separation method and apparatus for granulated slag in waste melting furnace

Country Status (1)

Country Link
JP (1) JP3374709B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006102663A (en) * 2004-10-06 2006-04-20 Kawasaki Heavy Ind Ltd Method for treating molten slag

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101831515A (en) * 2010-05-28 2010-09-15 陈子耀 Blast furnace water granulated slag collector
JP6015335B2 (en) * 2012-10-16 2016-10-26 Jfeスチール株式会社 Magnetic sorting method and magnetic sorting equipment
CN106853454B (en) * 2015-12-09 2020-03-31 上海烟草集团有限责任公司 Discarded tobacco leaf fragmentation and classification utilization device
JP6907155B2 (en) * 2018-06-04 2021-07-21 荏原環境プラント株式会社 Cleaning device and cleaning method
JP7401758B2 (en) * 2020-02-18 2023-12-20 日本製鉄株式会社 Blast furnace raw material sorting method and blast furnace raw material sorting device

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006102663A (en) * 2004-10-06 2006-04-20 Kawasaki Heavy Ind Ltd Method for treating molten slag
JP4515214B2 (en) * 2004-10-06 2010-07-28 川崎重工業株式会社 Method for processing molten slag.

Also Published As

Publication number Publication date
JPH1133529A (en) 1999-02-09

Similar Documents

Publication Publication Date Title
US5961055A (en) Method for upgrading iron ore utilizing multiple magnetic separators
EP2128279B1 (en) Method for separating metal-containing fractions from dry slag and the use of this method for waste incineration slag.
JP3969048B2 (en) Recycling method for waste home appliances
US8267336B2 (en) System and method for treating shredder residues and use of a granulate fraction thus produced
JPS62294140A (en) Treatment of slag produced in iron making plant
JP6465825B2 (en) Method and apparatus for recovering precious metals from incinerated ash
JP2013117058A (en) Apparatus for producing iron-based material and regenerated sand
JPH11253889A (en) Method and device for recovering metal from solid waste
JPH0741874A (en) Method for recovering metal slag of waste
JP2006520689A (en) Method for recovering non-ferrous metal-containing particles from a particle stream
JP2002537992A (en) Apparatus and method for utilizing shredder waste or equivalent composite material and use of rotor crusher
JP6502274B2 (en) Incineration ash sorting method and apparatus
JP6421765B2 (en) Method for sorting steel slag, method for reusing steel slag, and method for producing raw materials for iron making
JP3374709B2 (en) Separation method and apparatus for granulated slag in waste melting furnace
JP6056617B2 (en) Method and apparatus for separating ferromagnetic material
JP2014180595A (en) Contaminated soil treating method
CA2279633A1 (en) Process for separating radioactive and hazardous metal contaminants from soils
JPH0647315A (en) Method for beneficiation of kish graphite
JPS60135533A (en) Treatment of stainless steel slag
JPH09196352A (en) Device for solidifying and treating melted item in waste product melting furnace
JP3233907B2 (en) How to treat shredder dust dry matter
JPH05123605A (en) Method for recovering ground metal contained in slag
JPH11179333A (en) Method and apparatus for separating water granulated slag of waste melting furnace
JPH11179334A (en) Method and apparatus for collecting slag from melt of waste melting furnace
JP6938414B2 (en) How to dispose of parts waste

Legal Events

Date Code Title Description
S111 Request for change of ownership or part of ownership

Free format text: JAPANESE INTERMEDIATE CODE: R313121

R371 Transfer withdrawn

Free format text: JAPANESE INTERMEDIATE CODE: R371

S111 Request for change of ownership or part of ownership

Free format text: JAPANESE INTERMEDIATE CODE: R313121

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20071129

Year of fee payment: 5

S531 Written request for registration of change of domicile

Free format text: JAPANESE INTERMEDIATE CODE: R313531

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20071129

Year of fee payment: 5

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20071129

Year of fee payment: 5

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20081129

Year of fee payment: 6

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20091129

Year of fee payment: 7

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20091129

Year of fee payment: 7

S111 Request for change of ownership or part of ownership

Free format text: JAPANESE INTERMEDIATE CODE: R313115

S531 Written request for registration of change of domicile

Free format text: JAPANESE INTERMEDIATE CODE: R313531

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20091129

Year of fee payment: 7

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20101129

Year of fee payment: 8

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20101129

Year of fee payment: 8

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20111129

Year of fee payment: 9

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20121129

Year of fee payment: 10

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20121129

Year of fee payment: 10

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20131129

Year of fee payment: 11

EXPY Cancellation because of completion of term