JPH0574558A - Induction heating type residue melting furnace - Google Patents

Induction heating type residue melting furnace

Info

Publication number
JPH0574558A
JPH0574558A JP26315491A JP26315491A JPH0574558A JP H0574558 A JPH0574558 A JP H0574558A JP 26315491 A JP26315491 A JP 26315491A JP 26315491 A JP26315491 A JP 26315491A JP H0574558 A JPH0574558 A JP H0574558A
Authority
JP
Japan
Prior art keywords
residue
melting chamber
melting
water tank
incombustible
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.)
Granted
Application number
JP26315491A
Other languages
Japanese (ja)
Other versions
JP3088515B2 (en
Inventor
Koichi Nemoto
宏一 根本
Shinichi Miyajima
伸一 宮島
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.)
Toshiba Corp
Kitashiba Electric Co Ltd
Original Assignee
Toshiba Corp
Kitashiba Electric Co Ltd
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 Toshiba Corp, Kitashiba Electric Co Ltd filed Critical Toshiba Corp
Priority to JP26315491A priority Critical patent/JP3088515B2/en
Publication of JPH0574558A publication Critical patent/JPH0574558A/en
Application granted granted Critical
Publication of JP3088515B2 publication Critical patent/JP3088515B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/25Process efficiency

Landscapes

  • General Induction Heating (AREA)
  • Gasification And Melting Of Waste (AREA)
  • Manufacture And Refinement Of Metals (AREA)
  • Furnace Details (AREA)

Abstract

(57)【要約】 【目的】 高融点の残渣を溶解してこれを砂状の粒子に
処理して、金属成分を分離できると共に、鉱物質粒子は
道路に敷く砂利などとして再利用することができる。 【構成】 コ字形鉄心2の脚部3にコイル4を巻回した
インダクター1の、前記両脚部3の間に、密閉した溶融
室5を配置し、この溶融室5内に多数の黒鉛ブロック8
と不燃物残渣9を収納すると共に、不活性ガス供給管7
を取付け、且つ溶融室5の底部にすのこ10を形成して、
この下部に密閉した水槽2を設け、黒鉛ブロック8を誘
導加熱して、これと接する不燃物残渣9を間接的に加熱
溶融し、溶融残渣を水槽12に滴下させて水中で急冷し、
砂状固形物16とするものである。
(57) [Summary] [Purpose] It is possible to dissolve the high melting point residue and process it into sand-like particles to separate the metal components, and also to reuse the mineral particles as gravel laid on the road. it can. [Structure] A closed melting chamber 5 is arranged between the legs 3 of an inductor 1 in which a coil 4 is wound around a leg 3 of a U-shaped iron core 2, and a large number of graphite blocks 8 are arranged in the melting chamber 5.
And the incombustible residue 9 are stored, and the inert gas supply pipe 7
Attached, and forming the slats 10 at the bottom of the melting chamber 5,
A sealed water tank 2 is provided below this, and the graphite block 8 is induction-heated to indirectly heat and melt the incombustible residue 9 in contact therewith, and the melted residue is dropped into a water tank 12 and rapidly cooled in water,
The sandy solid matter 16 is used.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は黒鉛ブロックを加熱し
て、不燃物の残渣を間接的に加熱溶融して砂状処理する
誘導加熱式残渣溶融炉に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an induction heating type residue melting furnace for heating a graphite block to indirectly heat and melt the residue of an incombustible material to treat it with sand.

【0002】[0002]

【従来の技術】年々増大する都市ゴミや産業廃棄物は、
ガスバーナーや重油バーナーなどの焼却炉である程度焼
却しているが、この中に含まれる不燃物は残渣としてそ
のまま残り、この残渣は専用の捨て場に捨てているた
め、捨て場を確保するための土地問題や公害問題として
大きな社会問題となっている。
2. Description of the Related Art Urban waste and industrial waste, which are increasing year by year,
Although it is incinerated to some extent in an incinerator such as a gas burner or a heavy oil burner, the incombustibles contained in this remain as a residue, and this residue is discarded in a dedicated dump, so it is necessary to secure a dump. It has become a major social problem as a land problem and pollution problem.

【0003】このような従来の燃焼式の焼却炉は、耐火
材で内張りした燃焼室に、焼却物を投入して燃焼バーナ
ーで加熱して焼却しているため、焼却温度に限度があり
金属や鉱物は焼却できないので残渣の量が多くなり減容
率が低く、前述のように捨て場が問題となっていた。
In such a conventional combustion type incinerator, an incinerator is put in a combustion chamber lined with a refractory material and heated by a combustion burner to incinerate, so that the incineration temperature is limited and metal and Since minerals cannot be incinerated, the amount of residue increases and the volume reduction rate is low, and as mentioned above, the dump site has been a problem.

【0004】このように残渣となった不燃物は高温で溶
融することにより更に減容することができることから、
アーク炉や抵抗炉、プラズマ炉などの電気炉や酸素反応
炉などで溶融する方法も提案されている。この場合、溶
融する残渣をレンガや不定形耐火材で構築したるつぼ形
の溶融室に投入して加熱溶融することになるが、加熱温
度は耐火材の耐火温度である1700℃以下でなければなら
ない。このように融点が1700℃以下の残渣としては金属
があるが、不燃物残渣に含まれるもののうち金属は少な
く大部分は炉壁耐火材と同類の鉱物質であり、このため
炉壁耐火材以上の高融点の残渣は溶融処理することがで
きなかった。
Since the incombustible material which has become a residue as described above can be further reduced in volume by melting at a high temperature,
A method of melting in an electric furnace such as an arc furnace, a resistance furnace, a plasma furnace, or an oxygen reaction furnace has also been proposed. In this case, the residue to be melted is put into a crucible-shaped melting chamber constructed of bricks and irregular-shaped refractory materials and heated and melted, but the heating temperature must be 1700 ° C or lower, which is the refractory temperature of the refractory materials. .. In this way, there are metals as the residue with a melting point of 1700 ° C or less, but there are few metals contained in the incombustible residue residue, and most of them are mineral substances similar to furnace wall refractory materials. The high melting point residue of could not be melt processed.

【0005】しかも溶融室はるつぼ形であるためるつぼ
の製造技術上、大きさに制限があり、また溶融した残渣
は液状のまま排出しなければならず、排出した溶融残渣
は冷却してブロック状に固化するので減容するが、その
まま利用することができず、また溶融成分の分離もでき
ないなどの問題もあった。
Moreover, since the melting chamber has a crucible shape, there is a limit to the size of the crucible manufacturing technology, and the molten residue must be discharged in a liquid state, and the discharged molten residue is cooled to form a block. Since it solidifies to a small volume, the volume is reduced, but it cannot be used as it is, and there is a problem that the molten components cannot be separated.

【0006】[0006]

【発明が解決しようとする課題】本発明は上記欠点を除
去し、従来溶融することができなかった高融点の残渣を
溶解してこれを砂状の粒子に処理して、金属成分を分離
できると共に、鉱物質粒子は道路に敷く砂利などとして
再利用することができる誘導加熱式残渣溶融炉を提供す
るものである。
DISCLOSURE OF THE INVENTION The present invention eliminates the above-mentioned drawbacks, dissolves a high melting point residue that could not be conventionally melted, and treats it as sandy particles to separate metal components. At the same time, the mineral particles provide an induction heating type residual melting furnace that can be reused as gravel laid on the road.

【0007】[0007]

【課題を解決するための手段】本発明は、コ字形鉄心の
脚部にコイルを巻回したインダクターの、前記両脚部の
間に、密閉した溶融室を配置し、この溶融室内に多数の
黒鉛ブロックを収納すると共に、不活性ガス供給管を取
付け、且つ溶融室の底部にすのこを形成して、この下部
に密閉した水槽を設けたことを特徴とするものである。
SUMMARY OF THE INVENTION According to the present invention, an inductor having a coil wound around a leg portion of a U-shaped iron core is provided with a hermetically sealed melting chamber between the both legs, and a large number of graphite particles are provided in the melting chamber. The present invention is characterized in that a block is housed, an inert gas supply pipe is attached, a sludge is formed at the bottom of the melting chamber, and a sealed water tank is provided at the bottom of this.

【0008】[0008]

【作用】本発明の残渣溶融炉では、不燃物残渣と黒鉛ブ
ロックを混合したものを溶融室に投入してから、溶融室
内に不活性ガス供給管から不活性ガスを供給しながら高
周波電源よりコ字形鉄心の脚部に巻回したコイルに交番
電流を流して黒鉛ブロックにジュール熱を発生させる。
この結果、不活性ガス雰囲気に保持されて高温に加熱さ
れた黒鉛ブロックと接している不燃物残渣も加熱されて
溶融する。溶融した不燃物残渣は液状になって下方に配
置した水槽の水中に滴下し、ここで急冷されて砂状固形
物となって回収される。
In the residue melting furnace of the present invention, a mixture of the incombustible residue and the graphite block is put into the melting chamber, and then an inert gas is supplied from the high frequency power supply to the melting chamber while supplying the inert gas. An alternating current is applied to the coil wound around the leg of the U-shaped core to generate Joule heat in the graphite block.
As a result, the incombustible residue remaining in contact with the graphite block heated in the inert gas atmosphere and heated to a high temperature is also heated and melted. The molten incombustible residue is liquefied and dropped into the water in the water tank arranged below, where it is rapidly cooled and recovered as a sandy solid.

【0009】[0009]

【実施例】以下本発明の一実施例を図1及び図2を参照
して詳細に説明する。図において1はインダクターで、
これはコ字形鉄心2の両脚部3、3にコイル4、4を巻
回し、このコイル4を図示しない高周波電源に接続した
ものである。5は溶融室でコイル4を巻回した前記両脚
部3、3の間に配置されている。この溶融室5は炭素繊
維耐火断熱ボードで側面5aと天井面5bとが形成され
て密閉構造となっている。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described in detail below with reference to FIGS. In the figure, 1 is an inductor,
In this configuration, coils 4 and 4 are wound around both legs 3 and 3 of the U-shaped iron core 2, and the coil 4 is connected to a high frequency power source (not shown). Reference numeral 5 denotes a melting chamber which is arranged between the leg portions 3 and 3 around which the coil 4 is wound. The melting chamber 5 has a side wall 5a and a ceiling surface 5b formed of a carbon fiber refractory heat insulating board, and has a closed structure.

【0010】また両コイル4、4と対向する溶融室5の
側面5a、5aの表面には図2に示すように凹凸部6が
形成されている。また天井面5bは開閉構造になってお
り、ここを投入口としている。更に溶融室5の上部には
アルゴンガスなどの不活性ガス供給管7が取付けられ溶
融室5内を不活性ガス雰囲気に保持するようになってい
る。
Further, as shown in FIG. 2, an uneven portion 6 is formed on the surfaces of the side surfaces 5a, 5a of the melting chamber 5 facing the coils 4, 4. Further, the ceiling surface 5b has an opening / closing structure, which serves as a charging port. Further, an inert gas supply pipe 7 such as argon gas is attached to the upper part of the melting chamber 5 so as to maintain the inside of the melting chamber 5 in an inert gas atmosphere.

【0011】またこの溶融室5内には多数の黒鉛ブロッ
ク8が不燃物残渣9と混合して天井面5bを開いた投入
口から内部に投入するようになっている。また溶融室5
の底部には図1に示すように黒鉛で形成されたすのこ10
が設けられ、この黒鉛すのこ10の底面に水冷ビーム11が
取付けられ黒鉛すのこ10を冷却するようになっている。
更にこの溶融室5の下部には密閉した水槽12が設けら
れ、ここに水13が溜められおり、この水槽12は上部の溶
融室5と連結具14で取外し自在に接続されている。
In addition, a large number of graphite blocks 8 are mixed with the incombustible residue 9 in the melting chamber 5 and are introduced into the interior through an opening through which the ceiling surface 5b is opened. Also the melting chamber 5
As shown in Fig. 1, the bottom part of the drainboard 10 is made of graphite.
Is provided, and a water cooling beam 11 is attached to the bottom surface of the graphite slats 10 to cool the graphite slats 10.
Further, a sealed water tank 12 is provided in the lower portion of the melting chamber 5, and water 13 is stored therein, and the water tank 12 is detachably connected to the upper melting chamber 5 by a connecting tool 14.

【0012】上記誘導加熱式残渣溶融炉では、先ず水槽
12に水13を入れてから、上部に溶融室5を載せて連結具
14で一体に接続する。次に溶融室5の天井面5bを開放
してこの投入口から不燃物残渣9と黒鉛ブロック8を混
合したものを投入する。次にこの溶融室5を移動させて
インダクター1の脚部3、3の間に設置する。
In the induction heating type residue melting furnace, first, a water tank is used.
Put water 13 in 12, then put melting chamber 5 on top and connect
Connect together at 14. Next, the ceiling surface 5b of the melting chamber 5 is opened, and a mixture of the incombustible residue 9 and the graphite block 8 is charged from this charging port. Next, the melting chamber 5 is moved and installed between the leg portions 3 of the inductor 1.

【0013】次に不活性ガス供給管7からアルゴンガス
などの不活性ガスを溶融室5内に供給しながら、図示し
ない高周波電源からコイル4に交番電流を流すと対向す
る鉄心脚部3、3間に強力な磁束15が発生する。この磁
束15は溶融室5を貫通し内部の黒鉛ブロック8と鎖交す
ることにより誘導電流が流れ、黒鉛ブロック8の固有抵
抗と誘導電流から渦電流損を生じてジュール熱を発生し
て黒鉛ブロック8が発熱する。この結果、高温の黒鉛ブ
ロック8と接している不燃物残渣9も間接的に加熱さ
れ、しかも溶融室5内は不活性ガス雰囲気に保持されて
いるので黒鉛ブロック8は酸化燃焼せずに2000℃程度ま
で昇温して、大部分の不燃物残渣9を溶融することがで
きる。
Next, while supplying an inert gas such as argon gas from the inert gas supply pipe 7 into the melting chamber 5, an alternating current is passed through the coil 4 from a high frequency power source (not shown), the iron core legs 3 and 3 facing each other. A strong magnetic flux 15 is generated between them. This magnetic flux 15 penetrates the melting chamber 5 and links with the internal graphite block 8 so that an induced current flows, and eddy current loss is generated from the specific resistance of the graphite block 8 and the induced current to generate Joule heat to generate the graphite block. 8 heats up. As a result, the incombustible residue 9 in contact with the high temperature graphite block 8 is also indirectly heated, and since the inside of the melting chamber 5 is maintained in the inert gas atmosphere, the graphite block 8 does not undergo oxidative combustion and is 2000 ° C. It is possible to raise the temperature to some extent and melt most of the incombustible residue 9.

【0014】溶融した不燃物残渣9は液状になって黒鉛
すのこ10の隙間から下方に配置した水槽12の水13に滴下
し、ここで急冷されて砂状固形物16となる。この場合、
不燃物残渣9に含まれる物質の種類に応じて融点が相違
するので、得られた砂状固形物16は融点がほぼ同一のも
ので形成され、特に金属質のものはその成分が単独で砂
状固形物16となるので、これを比重差により選別するこ
とにより有効利用することができる。また溶融室5の側
面5aは凹凸部6が形成されているので、側面5aと鎖
交する磁束15による発生する誘導電流の渦電流を防止し
て、側面5a自体の発熱を抑えることができるようにな
っている。
The molten incombustible residue 9 becomes a liquid and is dripped into the water 13 in the water tank 12 arranged below from the gap of the graphite sludge 10 and is rapidly cooled to become a sandy solid matter 16. in this case,
Since the melting point differs depending on the type of substance contained in the non-combustible residue 9, the obtained sandy solid substance 16 is formed to have substantially the same melting point. Since the solid matter 16 is formed, it can be effectively used by selecting it according to the difference in specific gravity. Further, since the side surface 5a of the melting chamber 5 is formed with the uneven portion 6, it is possible to prevent the eddy current of the induced current generated by the magnetic flux 15 interlinking with the side surface 5a and suppress the heat generation of the side surface 5a itself. It has become.

【0015】図3は本発明の他の実施例を示すもので、
長方形状の長い溶融室5を取付けた水槽12の底部に車輪
17を取付けて移動できるようにしたものを複数台用意し
て、溶融室5をインダクター1の間にゆっくり走行させ
て、溶融室5内の不燃物残渣9を長手方向に沿って順次
溶融して行くようになっている。1台の溶融室5で溶融
が完了したらインダクター1から引出して、別に待機し
ている溶融室5をインダクター1内に走行させて、稼働
を停止することなく効率よく処理できるようにしたもの
である。
FIG. 3 shows another embodiment of the present invention.
Wheels are attached to the bottom of the water tank 12 equipped with a long rectangular melting chamber 5.
Prepare a plurality of units with 17 attached so that they can move, and slowly run the melting chamber 5 between the inductors 1 to melt the incombustible residue 9 in the melting chamber 5 sequentially along the longitudinal direction. I'm supposed to go. When melting is completed in one melting chamber 5, it is pulled out from the inductor 1 and the melting chamber 5 that is on standby is run inside the inductor 1 so that efficient processing can be performed without stopping the operation. ..

【0016】上記実施例は何れもバッチ式の残渣溶融炉
について示したが、図4は連続式の残渣溶融炉を示すも
ので、これは溶融室5の側方にシューター18を接続し、
この上部に蓋19を取付けたホッパー20を設けたもので、
他の構成は図1と同様である。
Although all of the above-mentioned embodiments have shown a batch type residual melting furnace, FIG. 4 shows a continuous type residual melting furnace in which a shooter 18 is connected to the side of the melting chamber 5,
A hopper 20 with a lid 19 attached is provided on top of this.
Other configurations are similar to those in FIG.

【0017】これは蓋19を開放して先ず不燃物残渣9と
黒鉛ブロック8を混合したものをホッパー20から投入し
て黒鉛ブロック8を溶融室5内に送り、この後、不燃物
残渣9だけを投入してから黒鉛ブロック8を誘導加熱し
て不燃物残渣9を溶融する。不燃物残渣9が溶融して水
槽12に滴下して残量が減少して行くと、シューター18内
の不燃物残渣9が滑って溶融室5内に順次供給されて連
続的に処理することができるようになっている。
The lid 19 is opened, a mixture of the incombustible residue 9 and the graphite block 8 is first introduced from the hopper 20 and the graphite block 8 is fed into the melting chamber 5, after which only the incombustible residue 9 is left. And then the graphite block 8 is induction-heated to melt the incombustible residue 9. When the incombustible residue 9 melts and drops into the water tank 12 and the remaining amount decreases, the incombustible residue 9 in the shooter 18 slips and is sequentially supplied into the melting chamber 5 for continuous processing. You can do it.

【0018】[0018]

【発明の効果】以上説明した如く本発明によれば、従来
溶融することができなかった高融点の残渣を、黒鉛ブロ
ックを誘導加熱して間接的に高温度に加熱して溶融し、
これを水中で急冷して砂状固形物とすることにより後処
理を容易にして、金属成分を分離できると共に、これを
道路に敷く砂利などとして再利用することができる誘導
加熱式残渣溶融炉を得ることができる。
As described above, according to the present invention, a high melting point residue that could not be conventionally melted is melted by inductively heating the graphite block to a high temperature,
By rapidly cooling this in water to form a sandy solid, post-treatment can be facilitated, and metal components can be separated, and this can be reused as gravel laid on the road. Obtainable.

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

【図1】本発明の一実施例による誘導加熱式残渣溶融炉
の溶融室を破断して示す正面図である。
FIG. 1 is a front view showing a melting chamber of an induction heating type residue melting furnace according to an embodiment of the present invention in a cutaway manner.

【図2】図1の水平断面図である。FIG. 2 is a horizontal sectional view of FIG.

【図3】本発明の他の実施例による誘導加熱式残渣溶融
炉を示す側面図である。
FIG. 3 is a side view showing an induction heating type residue melting furnace according to another embodiment of the present invention.

【図4】本発明の異なる他の実施例による誘導加熱式残
渣溶融炉を示す縦断側面図である。
FIG. 4 is a vertical sectional side view showing an induction heating type residue melting furnace according to another embodiment of the present invention.

【符合の説明】[Explanation of sign]

1 インダクター 2 コ字形鉄心 3 脚部 4 コイル 5 溶融室 6 凹凸部 7 不活性ガス供給管 8 黒鉛ブロック 9 不燃物残渣 10 黒鉛すのこ 11 水冷ビーム 12 水槽 13 水 14 連結具 15 磁束 16 砂状固形物 17 車輪 18 シューター 19 蓋 20 ホッパー 1 inductor 2 U-shaped iron core 3 leg 4 coil 5 melting chamber 6 uneven part 7 inert gas supply pipe 8 graphite block 9 incombustible residue 10 graphite sludge 11 water cooling beam 12 water tank 13 water 14 connector 15 magnetic flux 16 sandy solid 17 Wheels 18 Shooters 19 Lids 20 Hoppers

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 コ字形鉄心の脚部にコイルを巻回したイ
ンダクターの、前記両脚部の間に、密閉した溶融室を配
置し、この溶融室内に多数の黒鉛ブロックを収納すると
共に、不活性ガス供給管を取付け、且つ溶融室の底部に
すのこを形成して、この下部に密閉した水槽を設けたこ
とを特徴とする誘導加熱式残渣溶融炉。
1. An inductor in which a coil is wound around a leg portion of a U-shaped iron core is provided with a sealed melting chamber between the both legs, and a large number of graphite blocks are housed in the melting chamber and the inertness is maintained. An induction heating type residue melting furnace, characterized in that a gas supply pipe is attached, a drain is formed at the bottom of the melting chamber, and a sealed water tank is provided below this.
JP26315491A 1991-09-13 1991-09-13 Induction heating residue melting furnace Expired - Fee Related JP3088515B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP26315491A JP3088515B2 (en) 1991-09-13 1991-09-13 Induction heating residue melting furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP26315491A JP3088515B2 (en) 1991-09-13 1991-09-13 Induction heating residue melting furnace

Publications (2)

Publication Number Publication Date
JPH0574558A true JPH0574558A (en) 1993-03-26
JP3088515B2 JP3088515B2 (en) 2000-09-18

Family

ID=17385552

Family Applications (1)

Application Number Title Priority Date Filing Date
JP26315491A Expired - Fee Related JP3088515B2 (en) 1991-09-13 1991-09-13 Induction heating residue melting furnace

Country Status (1)

Country Link
JP (1) JP3088515B2 (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0882408A (en) * 1994-09-12 1996-03-26 Kitashiba Denki Kk Waste melting method and waste melting facility
WO2006079132A1 (en) * 2005-01-27 2006-08-03 Patco Engineering Gmbh Method for reducing metal oxide slags or glasses and/or for degassing mineral melts and device for carrying out said method
WO2010022425A1 (en) * 2008-08-27 2010-03-04 Alfred Edlinger Method for processing solid or molten materials
KR101341178B1 (en) * 2011-12-22 2013-12-13 재단법인 포항산업과학연구원 Method for reducing valuable metal from steelmaking slag and cement clinker provided from the same
CN105865015A (en) * 2016-06-03 2016-08-17 唐山航清新能源有限公司 Electromagnetic assembly for carrying out vortex heating at air gap by adopting water cooling manner

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0882408A (en) * 1994-09-12 1996-03-26 Kitashiba Denki Kk Waste melting method and waste melting facility
WO2006079132A1 (en) * 2005-01-27 2006-08-03 Patco Engineering Gmbh Method for reducing metal oxide slags or glasses and/or for degassing mineral melts and device for carrying out said method
US7905940B2 (en) 2005-01-27 2011-03-15 Sgl Carbon Se Method for reducing metal oxide slags or glasses and/or for degassing mineral melts, and device for carrying out said method
WO2010022425A1 (en) * 2008-08-27 2010-03-04 Alfred Edlinger Method for processing solid or molten materials
CN102187001A (en) * 2008-08-27 2011-09-14 Sgl碳欧洲股份公司 Method for processing solid or molten materials
JP2012500717A (en) * 2008-08-27 2012-01-12 エスジーエル カーボン エスイー Method for processing solid or molten material
US8568507B2 (en) 2008-08-27 2013-10-29 Sgl Carbon Se Method for processing solid or molten materials
KR101341178B1 (en) * 2011-12-22 2013-12-13 재단법인 포항산업과학연구원 Method for reducing valuable metal from steelmaking slag and cement clinker provided from the same
CN105865015A (en) * 2016-06-03 2016-08-17 唐山航清新能源有限公司 Electromagnetic assembly for carrying out vortex heating at air gap by adopting water cooling manner

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