JPH10130041A - Slag separating and recovering method and separating and recovering equipment - Google Patents
Slag separating and recovering method and separating and recovering equipmentInfo
- Publication number
- JPH10130041A JPH10130041A JP8285169A JP28516996A JPH10130041A JP H10130041 A JPH10130041 A JP H10130041A JP 8285169 A JP8285169 A JP 8285169A JP 28516996 A JP28516996 A JP 28516996A JP H10130041 A JPH10130041 A JP H10130041A
- Authority
- JP
- Japan
- Prior art keywords
- slag
- heavy liquid
- separation
- separating
- separated
- 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
- 239000002893 slag Substances 0.000 title claims abstract description 91
- 238000000034 method Methods 0.000 title claims description 7
- 239000007788 liquid Substances 0.000 claims abstract description 38
- 238000005406 washing Methods 0.000 claims abstract description 9
- 238000000926 separation method Methods 0.000 claims description 48
- 230000005484 gravity Effects 0.000 claims description 33
- 238000011084 recovery Methods 0.000 claims description 15
- 239000000463 material Substances 0.000 description 9
- 238000007885 magnetic separation Methods 0.000 description 6
- 238000002844 melting Methods 0.000 description 6
- 230000008018 melting Effects 0.000 description 6
- 239000002245 particle Substances 0.000 description 5
- 238000004140 cleaning Methods 0.000 description 4
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- LFYJSSARVMHQJB-QIXNEVBVSA-N bakuchiol Chemical compound CC(C)=CCC[C@@](C)(C=C)\C=C\C1=CC=C(O)C=C1 LFYJSSARVMHQJB-QIXNEVBVSA-N 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000002440 industrial waste Substances 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000004575 stone Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 239000010426 asphalt Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000005469 granulation Methods 0.000 description 1
- 230000003179 granulation Effects 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000010791 quenching Methods 0.000 description 1
- 230000000171 quenching effect Effects 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 239000010801 sewage sludge Substances 0.000 description 1
- 238000010583 slow cooling Methods 0.000 description 1
Landscapes
- Processing Of Solid Wastes (AREA)
- Curing Cements, Concrete, And Artificial Stone (AREA)
Abstract
Description
【０００１】[0001]
【発明の属する技術分野】本発明は、都市ごみや産業廃
棄物等の焼却残渣、下水汚泥等を溶融固化した後のスラ
グを分離回収するための、スラグの分離回収方法及び分
離回収設備に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a slag separation and recovery method and a slag separation and recovery facility for melting and solidifying incineration residues such as municipal waste and industrial waste, sewage sludge, and the like. It is.
【０００２】[0002]
【従来の技術】都市ごみや産業廃棄物等は焼却処分され
ることが多い。焼却減容された焼却残渣は、埋め立て処
分されている。しかし、埋め立て処分場の確保は次第に
困難になっているので、焼却残渣を溶融炉で溶融した後
固化し、路盤材、骨材、ブロック等として再利用するよ
うになりつつある。2. Description of the Related Art Municipal waste and industrial waste are often incinerated. The incineration residue whose volume has been reduced by incineration has been landfilled. However, as it becomes increasingly difficult to secure landfill sites, incineration residues are melted in a melting furnace, then solidified, and reused as roadbed materials, aggregates, blocks, and the like.
【０００３】一般に、溶融炉から高温溶融状態で出湯し
たスラグは、急冷するとガラス質スラグになるが、徐冷
すると結晶構造をもつ結晶化スラグになることが知られ
ている。比較的大規模な溶融炉におけるスラグ処理は、
処理の簡易さゆえに、急冷する水砕処理が主流であった
が、生成されるスラグは非結晶質のため脆く再利用しに
くい。そこで、近年はスラグを空冷もしくは徐冷して強
度の大きい結晶化スラグとし、需要の大きい路盤材やコ
ンクリート骨材等へ有効利用してゆく動きが活発化して
いる。In general, it is known that slag discharged from a melting furnace in a high-temperature molten state becomes a vitreous slag when rapidly cooled, and becomes a crystallized slag having a crystal structure when gradually cooled. Slag treatment in relatively large-scale melting furnaces
Due to the simplicity of the treatment, a water granulation treatment of quenching has been the mainstream, but the slag produced is non-crystalline and thus brittle and difficult to reuse. Therefore, in recent years, there has been an increasing movement to use slag as a crystallized slag having a high strength by air cooling or slow cooling and effectively utilizing the slag as a roadbed material, a concrete aggregate, and the like, which are in great demand.
【０００４】従来、このような結晶化スラグは、破砕、
磁選、分級工程を経て、路盤材等の用途によって、その
規格に適合するように粒度調整した後使用されていた。Conventionally, such crystallized slag has been crushed,
After being subjected to magnetic separation and classification processes, it was used after adjusting the particle size so as to conform to the standards according to the use of the roadbed material and the like.
【０００５】[0005]
【発明が解決しようとする課題】しかし、実際のところ
結晶化スラグは比重や強度等にかなりのばらつきがあ
り、破砕後粒度調整しただけでは、粒度基準は満たし得
るとしても比重や強度等他の規格基準を満すことが難し
く、例えば路盤材として使用する場合、大半が下層路盤
材としてしか使用できず、付加価値の低いものとなって
いた。However, crystallized slag actually has a considerable variation in specific gravity, strength and the like. Even if the particle size is adjusted only after crushing, other slags such as specific gravity and strength can be satisfied even if the particle size standard can be satisfied. It is difficult to satisfy the standard and, for example, when used as a roadbed material, most of them can only be used as a lower layer roadbed material, and have low added value.
【０００６】本発明は、結晶化スラグの利用における上
記課題を解決するものであって、結晶化スラグから付加
価値の高いのスラグ製品を得ることのできるスラグの分
離回収方法及び分離回収設備を提供することを目的とす
る。The present invention solves the above-mentioned problems in using crystallized slag, and provides a slag separation / recovery method and a separation / recovery facility capable of obtaining high value-added slag products from crystallized slag. The purpose is to do.
【０００７】[0007]
【課題を解決するための手段】本発明のスラグの分離回
収方法では、結晶化スラグを破砕した後、破砕されたス
ラグを重液を用いて比重差により分離回収することによ
り、上記課題を解決している。According to the method for separating and recovering slag of the present invention, the above-mentioned problem is solved by crushing crystallized slag and then separating and recovering the crushed slag with a specific gravity difference using a heavy liquid. doing.
【０００８】溶融炉で溶融した後徐冷固化した結晶化ス
ラグは、比重や強度等にかなりのばらつきがあり、一般
的に比重の小さいスラグは多孔質で強度が小であり、比
重の大きいスラグは孔隙が少なく稠密で強度が大であ
る。従って、破砕後比重差により分離回収されたスラグ
は、比重が小さく多孔質のスラグが透水性コンクリート
骨材等として、比重が大きく強度が大であるスラグが上
層路盤材やアスファルト舗装における表層・基層用舗装
材、第一種道路用砕石等として、その比重、強度等の性
質を活かした製品に利用される。[0008] Crystallized slag which has been melted in a melting furnace and then gradually cooled and solidified has a considerable variation in specific gravity, strength, and the like. Generally, slag having a small specific gravity is porous, low in strength, and slag having a large specific gravity. Has small pores, high density and high strength. Therefore, the slag separated and recovered due to the difference in specific gravity after crushing, the slag having a low specific gravity and porous slag is used as permeable concrete aggregate, etc. It is used as a paving material for roads, as a first-class crushed stone for roads, etc., for products that make use of its properties such as specific gravity and strength.
【０００９】本発明のスラグの分離回収設備は、結晶化
スラグを破砕する破砕機と、破砕されたスラグを重液を
用いて比重差により分離する分離槽と、重液の濃度を調
整する濃度調整装置と、濃度調整装置によって濃度が調
整された重液を分離槽に供給する循環ポンプと、分離槽
で分離されたスラグを洗浄する洗浄ホッパとを備えてい
る。The slag separation and recovery equipment of the present invention includes a crusher for crushing crystallized slag, a separation tank for separating crushed slag by using a heavy liquid and a specific gravity difference, and a concentration for adjusting the concentration of the heavy liquid. An adjusting device, a circulation pump for supplying the heavy liquid whose concentration has been adjusted by the concentration adjusting device to the separation tank, and a washing hopper for washing the slag separated in the separation tank are provided.
【００１０】結晶化スラグは、まず破砕機で破砕され
る。破砕されたスラグは分離槽に投入される。分離槽内
には、濃度調整装置によって所定比重となるように濃度
を調整された重液が循環ポンプで供給されており、投入
されたスラグは比重の小さいものが浮上し、比重の大き
いものは沈降するので比重差により分離される。分離さ
れたスラグはそれぞれ分離槽から排出され、洗浄ホッパ
で付着した重液が洗浄除去された後、製品として利用さ
れる。[0010] The crystallized slag is first crushed by a crusher. The crushed slag is put into a separation tank. In the separation tank, a heavy liquid whose concentration has been adjusted by the concentration adjusting device so as to have a predetermined specific gravity is supplied by a circulation pump. As they settle, they are separated by specific gravity. The separated slag is discharged from the separation tank, and the heavy liquid adhering to the washing hopper is washed and removed, and then used as a product.
【００１１】このスラグの分離回収設備において、分離
槽を多段に設置し、各段の分離槽にそれぞれ比重の異な
る重液を供給すれば、スラグを比重の異なる多種の製品
に分離して、それぞれを最適な用途に利用することがで
きる。In this slag separation and recovery equipment, if separation tanks are installed in multiple stages and heavy liquids having different specific gravities are supplied to the separation tanks at each stage, the slag is separated into various products having different specific gravities, and Can be used for optimal use.
【００１２】[0012]
【発明の実施の形態】図１は、この発明の実施の一形態
であるスラグの分離回収設備の構成図である。FIG. 1 is a configuration diagram of a slag separation and recovery facility according to an embodiment of the present invention.
【００１３】このスラグの分離回収設備では、破砕機１
の後段に一次スクリーン３が設けられており、破砕機１
と一次スクリーン３との間には、破砕機１で破砕された
スラグを一次スクリーン３へ搬送する磁選コンベヤ２が
敷設されている。この磁選コンベヤ２は、メタル分を分
離除去するための公知のマグネットプーリ２１を備えて
いる。In this slag separation and recovery equipment, a crusher 1
A primary screen 3 is provided at the subsequent stage, and the crusher 1
Between the and the primary screen 3, a magnetic separation conveyor 2 for conveying the slag crushed by the crusher 1 to the primary screen 3 is laid. The magnetic separation conveyor 2 includes a known magnet pulley 21 for separating and removing metal components.
【００１４】一次スクリーン３の下には、一次スクリー
ン３の篩下をホッパ５に搬送する搬送コンベヤ４と、一
次スクリーン３の篩上を分離槽７に投入するための投入
コンベヤ６が敷設されている。Below the primary screen 3, a conveyor 4 for transporting the screen of the primary screen 3 to the hopper 5 and a charging conveyor 6 for charging the screen of the primary screen 3 into the separation tank 7 are provided. I have.
【００１５】分離槽７には濃度調整装置１１から重液供
給管１３が配管されており、重液供給管１３の途中には
循環ポンプ１２が設置されている。濃度調整装置１１で
所定比重となるよう濃度を調整された重液が循環ポンプ
１２で分離槽７に供給され、分離槽７内にはこの重液が
満たされている。A heavy liquid supply pipe 13 is connected to the separation tank 7 from the concentration controller 11, and a circulation pump 12 is provided in the middle of the heavy liquid supply pipe 13. The heavy liquid whose concentration has been adjusted to a predetermined specific gravity by the concentration adjusting device 11 is supplied to the separation tank 7 by the circulation pump 12, and the separation tank 7 is filled with the heavy liquid.
【００１６】分離槽７の上部と底部には、分離されたス
ラグを排出するための排出管１４Ａ、１４Ｂが設けられ
ている。この排出管１４Ａ、１４Ｂはスラグの排出量を
調節するための調節ゲート８Ａ、８Ｂを備えており、排
出量を調節しながら二次スクリーン９Ａ、９Ｂにスラグ
を排出するようになっている。二次スクリーン９Ａ、９
Ｂは、固液分離を行うものであり、二次スクリーン９
Ａ、９Ｂの下には篩上のスラグが投入される洗浄ホッパ
１０Ａ、１０Ｂと、分離された重液を濃度調整装置１１
へ返送する重液返送管１５が設けられている。Discharge pipes 14A and 14B for discharging the separated slag are provided at the top and bottom of the separation tank 7. The discharge pipes 14A and 14B are provided with adjustment gates 8A and 8B for adjusting the amount of slag discharged, and discharge the slag to the secondary screens 9A and 9B while adjusting the amount of discharge. Secondary screen 9A, 9
B is for performing solid-liquid separation, and the secondary screen 9 is used.
A washing hoppers 10A and 10B into which slag on a sieve is introduced under A and 9B, and a separated heavy liquid is supplied to a concentration adjusting device 11;
There is provided a heavy liquid return pipe 15 for returning the liquid.
【００１７】このスラグの分離回収設備で結晶化スラグ
を分離回収する場合には、まずブレーカ等で粗破砕した
塊状のスラグを破砕機１で粒径約４０ｍｍ以下に破砕す
る。破砕されたスラグは、磁選コンベヤ２で搬送され、
磁選コンベヤ２のマグネットプーリ２１でメタル分（主
成分：鉄）が分離除去された後、一次スクリーン３に投
入される。When the crystallized slag is separated and recovered by the slag separation and recovery equipment, first, a massive slag roughly crushed by a breaker or the like is crushed by the crusher 1 to a particle size of about 40 mm or less. The crushed slag is conveyed by the magnetic separation conveyor 2,
After the metal component (main component: iron) is separated and removed by the magnet pulley 21 of the magnetic separation conveyor 2, it is put into the primary screen 3.
【００１８】一次スクリーン３では、破砕されたスラグ
を篩分け、粒径２．３６ｍｍ以下の篩下を搬送コンベヤ
４でホッパ５へ搬送する。この篩下製品は、タイル混
合、流動床炉用砂等として再利用される。In the primary screen 3, the crushed slag is sieved, and the sifter having a particle size of 2.36 mm or less is conveyed to a hopper 5 by a conveyor 4. This sieved product is reused as tile mixing, fluid bed furnace sand, and the like.
【００１９】一次スクリーン３の篩上は、投入コンベヤ
６で分離槽７に投入される。分離槽７内の重液は、濃度
調整装置１１で所定比重（２．０〜２．３程度）となる
よう濃度を調整されており、投入されたスラグは、比重
の小さいものは浮上し、比重の大きいものは沈降して比
重差により分離される。重液の比重を変更すれば、スラ
グの分離範囲を容易に変更することができる。The screen of the primary screen 3 is charged into a separation tank 7 by a charging conveyor 6. The concentration of the heavy liquid in the separation tank 7 is adjusted to a predetermined specific gravity (about 2.0 to 2.3) by the concentration adjusting device 11. Those with a large specific gravity settle and are separated by a specific gravity difference. If the specific gravity of the heavy liquid is changed, the slag separation range can be easily changed.
【００２０】分離されたスラグは、調節ゲート８Ａ、８
Ｂで排出量を調節されて排出管１４Ａ、１４Ｂから二次
スクリーン９Ａ、９Ｂへ排出される。排出されたスラグ
は、二次スクリーン９Ａ、９Ｂで固液分離され、篩上の
スラグが洗浄ホッパ１０Ａ、１０Ｂに供給される。供給
されたスラグは、洗浄ホッパ１０Ａ、１０Ｂにおいて付
着した重液が水で洗浄除去された後回収され製品として
利用される。The separated slag is supplied to the control gates 8A, 8A.
The discharge amount is adjusted by B and discharged from the discharge pipes 14A and 14B to the secondary screens 9A and 9B. The discharged slag is solid-liquid separated by the secondary screens 9A and 9B, and the slag on the sieve is supplied to the cleaning hoppers 10A and 10B. The supplied slag is collected and used as a product after the heavy liquid attached in the cleaning hoppers 10A and 10B is washed and removed with water.
【００２１】分離槽７の上部の排出管１４Ａから排出さ
れ洗浄ホッパ１０Ａ側に回収されたスラグは、分離槽７
で浮上した比重が小さく多孔質のスラグであるので、透
水性コンクリート骨材等として利用される。The slag discharged from the discharge pipe 14A at the upper part of the separation tank 7 and collected on the side of the washing hopper 10A is supplied to the separation tank 7A.
Since the slag is a porous slag having a small specific gravity, it is used as a permeable concrete aggregate.
【００２２】分離槽７の底部の排出管１４Ｂから排出さ
れ洗浄ホッパ１０Ｂ側に回収されたスラグは、分離槽７
で沈降した比重が大きく強度が大で稠密なスラグである
ので、上層路盤材やアスファルト舗装における表層・基
層用舗装材、第一種道路用砕石等として利用される。The slag discharged from the discharge pipe 14B at the bottom of the separation tank 7 and collected on the cleaning hopper 10B side is supplied to the separation tank 7B.
It is a dense slag that has a large specific gravity and a high strength, and is used as an upper roadbed material, a surface / base layer pavement material in asphalt pavement, a first-class road crushed stone, and the like.
【００２３】二次スクリーン９Ａ、９Ｂでスラグと分離
された重液は、重液返送管１５で濃度調整装置１１へ返
送され、濃度調整装置１１において液中のごみ（微粉
末）を回収するとともに濃度調整され、再度分離槽７へ
供給される。このように重液は循環使用されるので排出
負荷が低い。The heavy liquid separated from the slag by the secondary screens 9A and 9B is returned to the concentration controller 11 through the heavy liquid return pipe 15, and the concentration controller 11 collects dust (fine powder) in the liquid. The concentration is adjusted and supplied to the separation tank 7 again. As described above, since the heavy liquid is circulated and used, the discharge load is low.
【００２４】溶融炉で溶融した後固化した結晶化スラグ
は、比重や強度等にかなりのばらつきがあるが、このよ
うに重液を用いて分離回収することにより、その比重、
強度等の性質を活かせる製品に利用できるようになる。The crystallized slag solidified after being melted in the melting furnace has a considerable variation in specific gravity, strength and the like.
It can be used for products that can take advantage of properties such as strength.
【００２５】このスラグの分離回収設備において、分離
槽７を多段に設置し、各段の分離槽７にそれぞれ比重の
異なる重液を供給すれば、スラグを比重の異なる多種の
製品に分離して、それぞれを最適な用途に利用すること
ができる。In this slag separation and recovery equipment, if the separation tanks 7 are installed in multiple stages and heavy liquids having different specific gravities are supplied to the separation tanks 7 in each stage, the slag is separated into various products having different specific gravities. , Each can be used for optimal use.
【００２６】[0026]
【発明の効果】以上説明したように、本発明のスラグの
分離回収方法によれば、比重や強度等にばらつきがある
結晶化スラグを、その品質によって分離回収でき、その
比重、強度等の性質を活かした適材適所の再利用が可能
となる。As described above, according to the method for separating and recovering slag of the present invention, crystallized slag having variations in specific gravity and strength can be separated and recovered according to its quality, and its properties such as specific gravity and strength can be improved. This makes it possible to reuse the right material in the right place.
【００２７】本発明のスラグの分離回収設備によれば、
重液が所定比重となるように濃度を調整され循環ポンプ
で分離槽へ供給されるので、最適の比重範囲でスラグを
分離回収でき、付加価値の高いのスラグ製品を得ること
ができる。According to the slag separation and recovery equipment of the present invention,
Since the concentration of the heavy liquid is adjusted so as to have a predetermined specific gravity and supplied to the separation tank by the circulation pump, slag can be separated and recovered within an optimum specific gravity range, and a slag product with high added value can be obtained.
【００２８】このスラグの分離回収設備において、分離
槽を多段に設置し、各段の分離槽にそれぞれ比重の異な
る重液を供給すれば、スラグを比重の異なる多種の製品
に分離して、それぞれを最適な用途に利用することがで
きる。In this slag separation and recovery equipment, if separation tanks are installed in multiple stages and heavy liquids having different specific gravities are supplied to the separation tanks in each stage, the slag is separated into various products having different specific gravities, and Can be used for optimal use.
【図１】本発明の実施の一形態であるスラグの分離回収
設備の構成図である。FIG. 1 is a configuration diagram of a slag separation and recovery facility according to an embodiment of the present invention.
１ 破砕機 ２ 磁選コンベヤ ３ 一次スクリーン ４ 搬送コンベヤ ５ ホッパ ６ 投入コンベヤ ７ 分離槽 ８Ａ、８Ｂ 調節ゲート ９Ａ、９Ｂ 二次スクリーン １０Ａ、１０Ｂ 洗浄ホッパ １１ 濃度調整装置 １２ 循環ポンプ １３ 重液供給管 １４Ａ、１４Ｂ 排出管 １５ 重液返送管 DESCRIPTION OF SYMBOLS 1 Crusher 2 Magnetic separation conveyor 3 Primary screen 4 Conveyor 5 Hopper 6 Input conveyor 7 Separation tank 8A, 8B Control gate 9A, 9B Secondary screen 10A, 10B Cleaning hopper 11 Concentration adjusting device 12 Circulation pump 13 Heavy liquid supply pipe 14A 14B drain pipe 15 heavy liquid return pipe
───────────────────────────────────────────────────── フロントページの続き (72)発明者 間瀬 努 栃木県小山市花垣町１−13−２ (72)発明者 井上 典幸 千葉県千葉市花見川区幕張町５−417−16 幕張ファミールハイツ１−607 (72)発明者 兼子 康男 茨城県下館市小川1206−１ ──────────────────────────────────────────────────続 き Continuing on the front page (72) Inventor Tsutomu Mase 1-13-2 Hanagaki-cho, Oyama City, Tochigi Prefecture (72) Inventor Noriyuki Inoue 5-417-16 Makuhari-cho, Hanamigawa-ku, Chiba City, Chiba Prefecture Makuhari Famil Heights 1- 607 (72) Inventor Yasuo Kaneko 1206-1 Ogawa, Shimodate City, Ibaraki Prefecture
Claims (3)
スラグを重液を用いて比重差により分離回収するスラグ
の分離回収方法。1. A method for separating and recovering slag in which crystallized slag is crushed, and the crushed slag is separated and recovered by using a heavy liquid according to a difference in specific gravity.
されたスラグを重液を用いて比重差により分離する分離
槽と、重液の濃度を調整する濃度調整装置と、濃度調整
装置によって濃度が調整された重液を分離槽に供給する
循環ポンプと、分離槽で分離されたスラグを洗浄する洗
浄ホッパとを備えたスラグの分離回収設備。2. A crusher for crushing crystallized slag, a separation tank for separating the crushed slag by a specific gravity difference using heavy liquid, a concentration adjusting device for adjusting the concentration of the heavy liquid, and a concentration adjusting device. A slag separation and recovery facility comprising a circulating pump for supplying a heavy liquid having an adjusted concentration to a separation tank, and a washing hopper for washing the slag separated in the separation tank.
はそれぞれ比重の異なる重液が供給されている請求項２
記載のスラグの分離回収設備。3. The separation tanks are provided in multiple stages, and heavy liquids having different specific gravities are supplied to the respective separation tanks.
A slag separation and recovery facility as described.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8285169A JPH10130041A (en) | 1996-10-28 | 1996-10-28 | Slag separating and recovering method and separating and recovering equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8285169A JPH10130041A (en) | 1996-10-28 | 1996-10-28 | Slag separating and recovering method and separating and recovering equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH10130041A true JPH10130041A (en) | 1998-05-19 |
Family
ID=17688000
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP8285169A Pending JPH10130041A (en) | 1996-10-28 | 1996-10-28 | Slag separating and recovering method and separating and recovering equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH10130041A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2012050932A (en) * | 2010-09-01 | 2012-03-15 | Fujitsu Ltd | Waste treatment apparatus |
| WO2014061256A1 (en) | 2012-10-16 | 2014-04-24 | Ｊｆｅスチール株式会社 | Magnetic sorting apparatus, magnetic sorting method, and method for manufacturing iron source |
| WO2017094803A1 (en) | 2015-11-30 | 2017-06-08 | Ｊｆｅスチール株式会社 | Magnetic separator, magnetic separation method, and method for manufacturing iron source |
-
1996
- 1996-10-28 JP JP8285169A patent/JPH10130041A/en active Pending
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2012050932A (en) * | 2010-09-01 | 2012-03-15 | Fujitsu Ltd | Waste treatment apparatus |
| WO2014061256A1 (en) | 2012-10-16 | 2014-04-24 | Ｊｆｅスチール株式会社 | Magnetic sorting apparatus, magnetic sorting method, and method for manufacturing iron source |
| KR20180035951A (en) | 2012-10-16 | 2018-04-06 | 제이에프이 스틸 가부시키가이샤 | Magnetic separator, magnetic separation method, and method for manufacturing iron source |
| WO2017094803A1 (en) | 2015-11-30 | 2017-06-08 | Ｊｆｅスチール株式会社 | Magnetic separator, magnetic separation method, and method for manufacturing iron source |
| JPWO2017094803A1 (en) * | 2015-11-30 | 2017-11-30 | Ｊｆｅスチール株式会社 | Magnetic sorting apparatus, magnetic sorting method, and iron source manufacturing method |
| KR20180072803A (en) | 2015-11-30 | 2018-06-29 | 제이에프이 스틸 가부시키가이샤 | Magnetic force selection device, magnetic force selection method and manufacturing method of iron source |
| US10857548B2 (en) | 2015-11-30 | 2020-12-08 | Jfe Steel Corporation | Magnetic separator, magnetic separation method, and iron source manufacturing method |
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