JP3088515B2 - Induction heating residue melting furnace - Google Patents
Induction heating residue melting furnaceInfo
- Publication number
- JP3088515B2 JP3088515B2 JP26315491A JP26315491A JP3088515B2 JP 3088515 B2 JP3088515 B2 JP 3088515B2 JP 26315491 A JP26315491 A JP 26315491A JP 26315491 A JP26315491 A JP 26315491A JP 3088515 B2 JP3088515 B2 JP 3088515B2
- Authority
- JP
- Japan
- Prior art keywords
- melting chamber
- residue
- melting
- induction heating
- melting furnace
- 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 - Fee Related
Links
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/25—Process efficiency
Landscapes
- General Induction Heating (AREA)
- Gasification And Melting Of Waste (AREA)
- Manufacture And Refinement Of Metals (AREA)
- Furnace Details (AREA)
Description
【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 incombustibles to sandy treatment.
【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 Municipal garbage and industrial waste, which increase year by year,
Some incinerators, such as gas burners and heavy oil burners, are incinerated, but the incombustibles contained therein remain as residues, and the residues are discarded in dedicated dumps. It is a major social problem as a land problem and a 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。[0003] In such a conventional combustion type incinerator, the incineration material is put into a combustion chamber lined with refractory material and heated by a combustion burner for incineration. Since minerals cannot be incinerated, the amount of residue increases and the volume reduction rate is low, and as mentioned above, dumping has become 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。[0004] Since the non-combustible material that remains as such 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, or a plasma furnace, an oxygen reactor, or the like has also been proposed. In this case, the residue to be melted is thrown into a crucible-shaped melting chamber constructed of bricks and irregular-shaped refractory material and heated and melted, but the heating temperature must be 1700 ° C or less, which is the refractory temperature of the refractory material . As described above, there is a metal as a residue having a melting point of 1700 ° C or less, but among the incombustible residue, there are few metals and most are mineral substances similar to the furnace wall refractory material. Could not be melted.
【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。Further, since the melting chamber is a crucible, the size of the crucible is limited in terms of the crucible manufacturing technique. The molten residue must be discharged in a liquid state. However, there is a problem that it cannot be used as it is and the molten component 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。SUMMARY OF THE INVENTION The present invention eliminates the above-mentioned drawbacks, dissolves a high melting point residue which could not be melted conventionally, and treats it as sand-like particles to separate metal components. In addition, the present invention provides an induction heating type residue melting furnace in which mineral particles can be reused as gravel or the like laid on a 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。According to the present invention, there is provided an inductor in which a coil is wound around a leg of a U-shaped iron core, a closed melting chamber is disposed between the two legs, and a large number of graphites are provided in the melting chamber. It is characterized in that the block is housed, an inert gas supply pipe is attached thereto, and a die is formed at the bottom of the melting chamber, and a sealed water tank is provided below 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 incombustible residue and a graphite block is charged into a melting chamber, and then the inert gas is supplied from an inert gas supply pipe into the melting chamber while the core is supplied from a high frequency power supply. An alternating current is applied to the coil wound around the legs of the U-shaped iron core to generate Joule heat in the graphite block.
As a result, the non-combustible residue in contact with the graphite block heated to a high temperature in the inert gas atmosphere is also heated and melted. The molten incombustible residue becomes liquid and is dropped into water in a water tank disposed below, where it is quenched 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 One embodiment of the present invention will be described below in detail with reference to FIGS. In the figure, 1 is an inductor,
In this embodiment, coils 4, 4 are wound around both legs 3, 3, of a 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 disposed between the two legs 3, 3 around which the coil 4 is wound. The melting chamber 5 has a closed structure in which a side surface 5a and a ceiling surface 5b are formed by a carbon fiber refractory heat insulating board.
【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。As shown in FIG. 2, an uneven portion 6 is formed on the surfaces of the side surfaces 5a and 5a of the melting chamber 5 opposed to the coils 4 and 4. The ceiling surface 5b has an opening / closing structure, which is used as an input port. Further, an inert gas supply pipe 7 such as an argon gas is attached to an upper portion 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 the melting chamber 5, a large number of graphite blocks 8 are mixed with the non-combustible residue 9 and injected into the interior through an inlet opening the ceiling surface 5b. Melting chamber 5
At the bottom of the slab is a graphite 10 made of graphite as shown in FIG.
A water cooling beam 11 is attached to the bottom surface of the graphite scale 10 to cool the graphite scale 10.
Further, a closed water tank 12 is provided at a lower portion of the melting chamber 5, and water 13 is stored therein. The water tank 12 is detachably connected to the upper melting chamber 5 by a connector 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 above-mentioned induction heating type residue melting furnace, first, a water tank is used.
Put water 13 in 12, then put the melting chamber 5 on top and connect
Connect them together at 14. Next, the ceiling surface 5b of the melting chamber 5 is opened, and a mixture of the non-combustible residue 9 and the graphite block 8 is charged from the charging port. Next, the melting chamber 5 is moved and installed between the legs 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, when an alternating current is applied to the coil 4 from a high-frequency power supply (not shown) while supplying an inert gas such as an argon gas into the melting chamber 5 from the inert gas supply pipe 7, the opposed iron core legs 3, 3 A strong magnetic flux 15 is generated in between. The magnetic flux 15 penetrates through the melting chamber 5 and interlinks with the graphite block 8 inside, so that an induced current flows, and an eddy current loss is generated from the specific resistance of the graphite block 8 and the induced current, thereby generating Joule heat to generate the graphite block. 8 generates heat. 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 an inert gas atmosphere, the graphite block 8 does not oxidize and burn at 2000 ° C. By raising the temperature to the extent, most of the non-combustible residue 9 can be melted.
【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 melted incombustible residue 9 becomes liquid and drops into the water 13 of the water tank 12 disposed below from the gap between the graphite chips 10, where it is rapidly cooled to a sand-like solid 16. in this case,
Since the melting point differs depending on the type of the substance contained in the incombustible residue 9, the obtained sand-like solid 16 is formed with almost the same melting point. Since the solids 16 are in the form of solids, they can be effectively used by sorting them out 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, the eddy current of the induced current generated by the magnetic flux 15 interlinking with the side surface 5a can be prevented, and the heat generation of the side surface 5a itself can be suppressed. 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 on the bottom of the water tank 12 with the long rectangular melting chamber 5
A plurality of units which can be moved by attaching 17 are prepared, and the melting chamber 5 is slowly moved between the inductors 1 to sequentially melt the incombustible residue 9 in the melting chamber 5 along the longitudinal direction. I'm going to go. When the melting in one melting chamber 5 is completed, the melting chamber 5 is drawn out of the inductor 1 and the other waiting melting chamber 5 is moved into the inductor 1 so that the processing can be efficiently 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。In each of the above embodiments, a batch type residue melting furnace is shown. FIG. 4 shows a continuous type residue 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 to this upper part is provided.
Other configurations are the same as 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。In this method, the lid 19 is opened, and a mixture of the non-combustible residue 9 and the graphite block 8 is first charged from the hopper 20 and the graphite block 8 is sent into the melting chamber 5. And then the graphite block 8 is induction-heated to melt the non-combustible residue 9. When the incombustible residue 9 is melted and dropped into the water tank 12 to reduce the remaining amount, the incombustible residue 9 in the shooter 18 slides and is sequentially supplied into the melting chamber 5 to be continuously processed. I 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 which could not be melted conventionally is melted by indirectly heating the graphite block to a high temperature by induction heating the graphite block.
An induction heating type residue melting furnace that quenches this in water to make it a sandy solid, facilitates post-treatment, separates metal components, and reuses it as gravel laid on roads. Obtainable.
【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 cutaway front view of a melting chamber of an induction heating type residue melting furnace according to one embodiment of the present invention.
【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.
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 DESCRIPTION OF SYMBOLS 1 Inductor 2 U-shaped iron core 3 Leg part 4 Coil 5 Melting chamber 6 Irregularity part 7 Inert gas supply pipe 8 Graphite block 9 Non-combustible residue 10 Graphite slender 11 Water cooling beam 12 Water tank 13 Water 14 Connector 15 Magnetic flux 16 Sandy solids 17 Wheels 18 Shooter 19 Lid 20 Hopper
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 ＦＩ Ｃ２２Ｂ 7/04 Ｃ２２Ｂ 7/04 Ａ 9/22 9/22 (58)調査した分野(Int.Cl.7，ＤＢ名) F23G 5/00 F23J 1/00 F27D 11/06 C22B 7/00 - 7/04 C22B 9/22 H05B 6/10 ──────────────────────────────────────────────────の Continued on the front page (51) Int.Cl. 7 identification code FI C22B 7/04 C22B 7/04 A 9/22 9/22 (58) Field surveyed (Int.Cl. 7 , DB name) F23G 5/00 F23J 1/00 F27D 11/06 C22B 7/00-7/04 C22B 9/22 H05B 6/10
Claims (1)
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 legs of a U-shaped iron core, a sealed melting chamber is disposed between the legs, and a large number of graphite blocks are accommodated in the melting chamber and inert. An induction-heating residue melting furnace, comprising: a gas supply pipe attached thereto; a bottom formed in a melting chamber; and a sealed water tank provided below the melting chamber.
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 JPH0574558A (en) | 1993-03-26 |
| JP3088515B2 true 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) |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP3196918B2 (en) * | 1994-09-12 | 2001-08-06 | 北芝電機株式会社 | Waste melting method and waste melting equipment |
| 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 |
| AT507262B1 (en) * | 2008-08-27 | 2011-04-15 | Sgl Carbon Se | METHOD FOR REPROCESSING SOLID OR MELTING SUBSTANCES |
| 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 |
| CN105865015B (en) * | 2016-06-03 | 2020-04-03 | 唐山航清新能源有限公司 | Electromagnetic assembly for carrying out eddy current heating at air gap by adopting water cooling mode |
-
1991
- 1991-09-13 JP JP26315491A patent/JP3088515B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0574558A (en) | 1993-03-26 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JP4563687B2 (en) | Melt-solidifying furnace and melt-solidifying method using two heating means | |
| JPH09505854A (en) | Method for treating solid residues from a refuse incineration plant and apparatus for implementing this method | |
| EA006623B1 (en) | Method and apparatus for melting metals | |
| JP3088515B2 (en) | Induction heating residue melting furnace | |
| JP2767189B2 (en) | Method for melting radioactive miscellaneous solid waste | |
| JP3483054B2 (en) | DC electric melting furnace for the production of reduced molten slag. | |
| JP3236885B2 (en) | Waste treatment equipment | |
| JPH0355410A (en) | Melting and disposing method for incinerated ash | |
| JP3196918B2 (en) | Waste melting method and waste melting equipment | |
| JP3350169B2 (en) | Waste melting method and apparatus | |
| JP3866086B2 (en) | Waste melting furnace discharge method and apparatus | |
| JP2002030354A (en) | Scrap melting method and scrap melting device | |
| JP2004069219A (en) | Waste melting treatment furnace | |
| JP3912717B2 (en) | Radioactive waste incineration melting processing apparatus and incineration melting processing method | |
| JPH0355411A (en) | Melting disposing device for incinerated ash | |
| JP2002048322A (en) | Melting processing method and melting processing furnace for waste | |
| JPH06273591A (en) | Equipment and method for incineration melting processing of waste | |
| JPH05237468A (en) | Incineration ash heating and melting treatment method and apparatus | |
| JPS60152813A (en) | Method for processing burnt ash of waste material | |
| Donaldson et al. | Melter development needs assessment for RWMC buried wastes | |
| JP2001330224A (en) | Method for melting treatment of waste | |
| JPS5920395B2 (en) | How to dispose of incinerated ash | |
| JP2016044823A (en) | Ash melting device and ash melting method | |
| JPH0355412A (en) | Plasma incinerated ash melting device | |
| JP2000162389A (en) | Melting device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |