JP2002341092A - Miscellaneous solid waste volume reduction method and high frequency induction furnace for miscellaneous solid waste fusion - Google Patents

Miscellaneous solid waste volume reduction method and high frequency induction furnace for miscellaneous solid waste fusion

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Publication number
JP2002341092A
JP2002341092A JP2001142936A JP2001142936A JP2002341092A JP 2002341092 A JP2002341092 A JP 2002341092A JP 2001142936 A JP2001142936 A JP 2001142936A JP 2001142936 A JP2001142936 A JP 2001142936A JP 2002341092 A JP2002341092 A JP 2002341092A
Authority
JP
Japan
Prior art keywords
canister
solid waste
metal
electromagnetic coil
miscellaneous solid
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
JP2001142936A
Other languages
Japanese (ja)
Other versions
JP3563041B2 (en
Inventor
Ichiro Kawaguchi
一郎 河口
Kazuki Kanai
和樹 金井
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.)
Kawasaki Heavy Industries Ltd
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Kawasaki Heavy Industries Ltd
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Filing date
Publication date
Application filed by Kawasaki Heavy Industries Ltd filed Critical Kawasaki Heavy Industries Ltd
Priority to JP2001142936A priority Critical patent/JP3563041B2/en
Publication of JP2002341092A publication Critical patent/JP2002341092A/en
Application granted granted Critical
Publication of JP3563041B2 publication Critical patent/JP3563041B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Processing Of Solid Wastes (AREA)
  • General Induction Heating (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a low-level radioactive miscellaneous solid waste volume reduction method capable of treating safely a large quantity of nonmetal solid waste by using a simpler constitution. SOLUTION: A lifting stand 2 for inserting a canister 10 into this induction furnace is equipped with a driving device 3 capable of stopping at an optional position and supporting the stand. At first, the low-level radioactive miscellaneous solid waste having much metal is stored in the canister 10, and an electromagnetic coil 1 is placed on the position of a metal layer 11 in the canister until the metal is fused, to thereby heat mainly the metal layer, and nonmetal is also fused by heat transfer. When a nonmetal layer 12 is formed, nonmetal waste is inputted, and the relative position of the electromagnetic coil 1 is moved up to the position especially facing to a conductive sleeve 4 in the nonmetal layer 12, to thereby heat mainly the nonmetal, and the output of the electromagnetic coil 1 is adjusted so that the temperature of the metal layer 11 is maintained at a lower value than a damage temperature of a furnace wall.

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、金属と非金属が混
在した固体廃棄物、特に原子力発電所で発生する低レベ
ル放射性の雑固体廃棄物の溶融方法および溶融用高周波
誘導炉に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for melting solid waste containing a mixture of metals and nonmetals, especially low-level radioactive solid waste generated in a nuclear power plant, and a high-frequency induction furnace for melting.

【0002】[0002]

【従来の技術】原子力発電所や放射性物質取扱施設など
で発生する低レベル放射性廃棄物のうち、断熱材や構造
材廃材等の雑固体廃棄物は埋設処分される。処分に際し
ては、廃棄物を200リットルドラム缶に詰め、隙間に
モルタルを充填した廃棄体を製造する。処分費用を軽減
するため、廃棄物をドラム缶に詰める前に減容すること
が望まれる。
2. Description of the Related Art Among low-level radioactive wastes generated in nuclear power plants and facilities handling radioactive materials, miscellaneous solid wastes such as heat insulation materials and structural material waste materials are disposed of by disposal. At the time of disposal, the waste is packed in a 200-liter drum, and a waste body in which the mortar is filled in the gap is produced. In order to reduce disposal costs, it is desirable to reduce the volume of waste before packing it in drums.

【0003】金属と非金属が混在した雑固体廃棄物の減
容方法の一つに、高周波誘導加熱炉を用いて廃棄物を溶
融固化する方法がある。高周波溶融炉内に設置したキャ
ニスタ内で雑固体廃棄物を誘導加熱により溶融して減容
し、そのままキャニスタ内で固化させ、キャニスタごと
ドラム缶に詰め隙間にモルタルを充填して廃棄体とする
ものである。従来、電磁誘導によりキャニスタ自体を発
熱させて固体廃棄物を溶融したので、高価な導電性セラ
ミックスで形成したキャニスタを使い捨てにしなければ
ならなかったが、金属廃棄物を活用することにより安価
で強度の高い一般的なセラミックスを使ったキャニスタ
が使用できるようになった。
[0003] One of the methods for reducing the volume of miscellaneous solid waste in which metal and nonmetal are mixed is a method of melting and solidifying the waste using a high-frequency induction heating furnace. It melts miscellaneous solid waste by induction heating in a canister installed in a high-frequency melting furnace and reduces its volume. is there. Conventionally, solid waste was melted by causing the canister itself to generate heat by electromagnetic induction.Thus, canisters made of expensive conductive ceramics had to be thrown away. Canisters using high general ceramics can now be used.

【0004】この方法で雑固体廃棄物を溶融する場合、
非金属成分を直接誘導加熱することはできない。したが
って、導電性を有する金属を誘導加熱し高温状態となっ
た溶融金属を熱源として、熱伝導により非金属成分を溶
融する。非金属成分が一緒に溶融できるようにするには
金属と非金属の混合割合に制限があり、非金属成分の割
合が大きな雑固体廃棄物を安定的に溶融処理することは
できない。そこで、本願の発明者等は先に、黒鉛等の導
電性物質性のスリーブを非金属溶融領域に配置し、その
発熱を利用して非金属成分を効果的に溶融する方法を考
案し、既に特願2000−335169に開示してい
る。
When melting miscellaneous solid waste by this method,
Non-metallic components cannot be directly induction heated. Therefore, the non-metal component is melted by heat conduction using the molten metal, which has been heated to a high temperature by induction heating the conductive metal, as a heat source. In order to allow the non-metal components to be melted together, the mixing ratio of the metal and the non-metal is limited, and the solid waste having a large non-metal component ratio cannot be melted stably. Therefore, the inventors of the present application have previously devised a method of arranging a sleeve made of a conductive material such as graphite in a non-metal melting region, and effectively melting the non-metal component using the heat generated. It is disclosed in Japanese Patent Application No. 2000-335169.

【0005】この方法は、図4に示すように、誘導加熱
用コイルの間にキャニスタを設置し、金属層と分離した
非金属層に導電性スリーブを浮かばせて誘導加熱し、金
属層からの熱とスリーブの熱を加えて非金属を溶融する
ようにしたものである。スリーブは非金属層の上層に浮
くので、表面付近の発熱が大きくなり有利である。ここ
で、非金属廃棄物を追加投入したときなど非金属層の必
要熱量が増加すると、コイルの高周波出力を上げて金属
とスリーブの発熱を増加することにより対応する。とこ
ろがこのとき金属層における発熱も増加するので、金属
溶湯の温度が上昇して特に金属層と非金属層の界面付近
のキャニスタ壁が浸食されやすくなり、場合によっては
キャニスタ材質の耐熱温度を超えて壁が溶融し内部の溶
湯が漏洩することも生じ得る。このように、発明者等が
先に開示した上記方法では、金属溶湯とスリーブが発熱
源となるが、両者の発熱割合は決まっており、固体廃棄
物中の金属成分と非金属成分の混合割合の変化や追加投
入などの運転状況に応じて任意に調整することができ
ず、運転が難しい。
In this method, as shown in FIG. 4, a canister is provided between induction heating coils, a conductive sleeve is floated on a non-metal layer separated from a metal layer, and induction heating is performed. The non-metal is melted by applying heat and heat of the sleeve. Since the sleeve floats above the non-metal layer, heat generation near the surface is increased, which is advantageous. Here, when the required amount of heat of the non-metal layer increases, such as when additional non-metal waste is added, the high-frequency output of the coil is increased to increase the heat generated by the metal and the sleeve. However, since the heat generated in the metal layer also increases at this time, the temperature of the molten metal rises, and the canister wall particularly near the interface between the metal layer and the non-metal layer is easily eroded. The wall may melt and the molten metal inside may leak. As described above, in the above method disclosed by the inventors, the molten metal and the sleeve are heat sources, but the heat generation ratio of both is determined, and the mixing ratio of the metal component and the non-metal component in the solid waste is determined. It cannot be adjusted arbitrarily according to the operating conditions such as changes in the amount of water and additional throws, making driving difficult.

【0006】また、金属の溶融を加速して処理時間を短
くするためには初期における金属の発熱を促進する一
方、溶融後の金属が過熱しないようにしてキャニスタの
健全性を保つため、非金属成分を溶融するときには金属
における発熱割合を小さくしスリーブの発熱割合を大き
くするような運転を実施するには、金属層と非金属層の
発熱割合を調整することができることが好ましい。本願
発明者等は、この課題を解決する発明を特願2000−
278065に開示している。
In order to shorten the processing time by accelerating the melting of the metal, the heat generation of the metal in the initial stage is promoted. In order to reduce the heat generation rate of the metal and increase the heat generation rate of the sleeve when melting the components, it is preferable that the heat generation rate of the metal layer and the non-metal layer can be adjusted. The inventors of the present application have filed an invention to solve this problem with Japanese Patent Application No.
278065.

【0007】この開示発明は、キャニスタの外側に上下
に移動する補償熱源を設け、非金属廃棄物が追加したと
きに補償熱源を金属層と非金属層の境界の動きに追従さ
せて境界付近から上方におけるキャニスタ外壁を加熱す
ることにより、非金属固体廃棄物の溶融を促進するもの
である。この発明方法によれば、金属溶湯の温度が極端
に上昇しないように管理してキャニスタの安全を確保す
ることができる。
The disclosed invention provides a compensating heat source that moves up and down outside the canister, and when non-metal waste is added, causes the compensating heat source to follow the movement of the boundary between the metal layer and the non-metal layer, and from the vicinity of the boundary. Heating the outer canister wall at the top promotes the melting of the non-metallic solid waste. According to the method of the present invention, the safety of the canister can be ensured by controlling the temperature of the molten metal so as not to rise extremely.

【0008】しかし、この方法は、高周波溶融加熱炉に
可動式の補償熱源を設備するので、設備コストが上昇
し、廃棄処分のコストを抑制することが困難になる。さ
らに、アルミナなどのセラミックスの融点は雑廃棄物中
の非金属の融点に比べて著しく高いわけではないので、
キャニスタ外部から加熱してキャニスタ内の非金属を溶
融しようとするとキャニスタの外壁が溶損することがあ
り、安全に運転するためには高度な温度管理が必要とな
る。
However, in this method, since a movable compensation heat source is provided in the high-frequency melting and heating furnace, the equipment cost increases, and it becomes difficult to suppress the cost of disposal. Furthermore, the melting point of ceramics such as alumina is not significantly higher than the melting point of nonmetals in miscellaneous waste,
When the non-metal in the canister is melted by heating from the outside of the canister, the outer wall of the canister may be melted, and a high degree of temperature control is required for safe operation.

【0009】[0009]

【発明が解決しようとする課題】そこで、本発明が解決
しようとする課題は、より簡単な構成を用いて安全に大
量の非金属固体廃棄物を処理することができる低レベル
放射性雑固体廃棄物減容方法とそれに使用する雑固体廃
棄物溶融用高周波誘導炉を提供することである。
SUMMARY OF THE INVENTION Accordingly, an object of the present invention is to provide a low-level radioactive miscellaneous solid waste capable of safely treating a large amount of nonmetallic solid waste using a simpler configuration. An object of the present invention is to provide a volume reduction method and a high-frequency induction furnace for melting solid waste used in the method.

【0010】[0010]

【課題を解決するための手段】上記課題を解決するた
め、本発明の雑固体廃棄物減容方法は、金属と非金属が
混合した低レベル放射性雑固体廃棄物をキャニスタに収
納して高周波誘導炉内に載置し、収納した雑固体廃棄物
を高周波誘導加熱によりキャニスタ内で溶融して減容す
るもので、キャニスタを前記高周波誘導炉内の電磁コイ
ルに対向する位置に置き、金属が溶融するまでは電磁コ
イルをキャニスタ内の金属層の位置に据えて主として金
属層の加熱を行いその熱で非金属をも溶融させ、生成し
た金属層の上の非金属層中に導電性スリーブを投入して
浮遊させ、非金属廃棄物を投入したときには電磁コイル
の相対的位置を非金属層に対向する位置まで動かして非
金属の加熱を主に行うとともに、電磁コイルの出力を金
属層の温度が所定の温度より低い値を維持するように調
整することを特徴とする。
In order to solve the above-mentioned problems, a method for reducing the volume of miscellaneous solid waste according to the present invention is provided by storing low-level radioactive miscellaneous solid waste containing a mixture of metal and nonmetal in a canister. It is placed in the furnace and the miscellaneous solid waste stored is melted in the canister by high-frequency induction heating to reduce the volume.The canister is placed at a position facing the electromagnetic coil in the high-frequency induction furnace, and the metal is melted. Until the electromagnetic coil is placed at the position of the metal layer in the canister, the metal layer is mainly heated, the non-metal is also melted by the heat, and the conductive sleeve is poured into the non-metal layer on the generated metal layer When the non-metal waste is introduced, the relative position of the electromagnetic coil is moved to a position facing the non-metal layer to mainly heat the non-metal, and the output of the electromagnetic coil is reduced by the temperature of the metal layer. Predetermined And adjusting so as to maintain a lower degree value.

【0011】本発明の雑固体廃棄物減容方法では、まず
キャニスタに主に金属からなる廃棄物を装荷し、高周波
加熱で溶融して金属溶湯を作る。次に、非金属を含む雑
固体廃棄物を順次投入して加熱を続け、廃棄物を溶融さ
せる。金属の方が非金属より比重が大きいため溶湯は下
部の金属層と上部の非金属層に分離する。キャニスタが
非導電性セラミックスで形成されている場合でも、導電
性スリーブを投入して一緒に誘導加熱すると、金属の誘
導発熱にスリーブの発熱が加算され非金属の溶融を促進
することができる。なお、導電性スリーブを非金属層の
比重より小さくなるように構成すると、常に非金属層の
表面に浮遊するようになるので、非金属雑固体をより容
易に溶融することができる。
In the method for reducing the volume of miscellaneous solid waste according to the present invention, first, waste mainly composed of metal is loaded in a canister and melted by high-frequency heating to produce a molten metal. Next, miscellaneous solid waste containing non-metals is sequentially charged and heating is continued to melt the waste. Since metal has a higher specific gravity than nonmetal, the molten metal is separated into a lower metal layer and an upper nonmetal layer. Even when the canister is made of non-conductive ceramics, if the conductive sleeve is put in and induction-heated together, the heat generation of the sleeve is added to the induction heat of the metal, so that the melting of the non-metal can be promoted. When the conductive sleeve is configured to have a specific gravity smaller than that of the nonmetal layer, the conductive sleeve always floats on the surface of the nonmetal layer, so that the nonmetallic solid can be more easily melted.

【0012】従来の雑固体廃棄物減容方法ではキャニス
ターを電磁コイル内部空間に据える位置が固定されてい
たので、非金属廃棄物の割合が大きくなるとこれらを溶
融するために高周波コイルへの電力供給量を増加させる
と、金属層における温度が上昇し、炉材の溶損が生じる
おそれがあった。
In the conventional method for reducing volume of miscellaneous solid waste, the position where the canister is placed in the internal space of the electromagnetic coil is fixed. Therefore, when the ratio of nonmetallic waste increases, power is supplied to the high-frequency coil in order to melt them. When the amount is increased, the temperature in the metal layer is increased, and there is a possibility that melting of the furnace material may occur.

【0013】しかし、本発明方法では、金属成分が溶融
する間は電磁コイルを金属層に対応する位置に置いて金
属溶湯の温度が十分高くなるまで加熱し金属層からの伝
熱により非金属廃棄物を溶融する。その後、非金属成分
の多い雑固体廃棄物を投入して処理する。さらに、投入
した廃棄物が溶融して減容すれば、新しく廃棄物を追加
して、可能な限り大量の廃棄物を収納するようにする。
このように非金属廃棄物の量を増やしたため印加電力を
増加しなければならなくなったときに、電磁コイルの位
置を非金属層の方に移動させて印加電力の配分を非金属
廃棄物側が大きくなるように変更した上で、金属溶湯が
過熱しないように温度を監視しながら電力調整して主と
してスリーブの誘導加熱により非金属廃棄物を溶融す
る。
However, in the method of the present invention, while the metal component is molten, the electromagnetic coil is placed at a position corresponding to the metal layer and heated until the temperature of the molten metal becomes sufficiently high, and the non-metal waste is transferred by the heat transfer from the metal layer. Melt the material. Then, miscellaneous solid waste containing a large amount of non-metallic components is introduced and treated. Further, if the input waste is melted and reduced in volume, new waste is added to store as much waste as possible.
When the applied power has to be increased because the amount of non-metal waste has been increased in this way, the position of the electromagnetic coil is moved toward the non-metal layer to distribute the applied power to the non-metal waste side. Then, the power is adjusted while monitoring the temperature so that the molten metal does not overheat, and the non-metallic waste is melted mainly by induction heating of the sleeve.

【0014】このように、本発明方法では、非金属廃棄
物の量に応じて電磁コイルの位置を調整することにより
供給エネルギーを適切に配分するので、金属溶湯をキャ
ニスタの壁に損傷を与えないような温度に抑えて運転す
ることができる。したがって、雑固体廃棄物を減容して
収納したキャニスタは頑丈に長期の保存に耐えることが
できる。なお、キャニスタの位置の調整は、キャニスタ
を搭載する台を昇降することにより行うことができる。
また、キャニスターを高周波誘導炉に搬入する前に、予
め雑固体廃棄物を仕込んでおいてもよい。特に、溶融処
理の初期に必要となる金属リッチの廃棄物と導電性スリ
ーブは初めからキャニスター内に有っても問題がなく、
また処理対象とする雑固体廃棄物の金属含有割合が十分
に大きければ、処理中に分けて投入しなくても溶融処理
を行うことができる。
As described above, in the method of the present invention, the supply energy is appropriately distributed by adjusting the position of the electromagnetic coil in accordance with the amount of nonmetallic waste, so that the molten metal does not damage the wall of the canister. It can be operated at such a temperature. Therefore, the canister storing the reduced volume of miscellaneous solid waste can sturdily endure long-term storage. Adjustment of the position of the canister can be performed by raising and lowering the base on which the canister is mounted.
Further, before carrying the canister into the high-frequency induction furnace, miscellaneous solid waste may be charged in advance. In particular, there is no problem even if the metal-rich waste and conductive sleeve required in the early stage of the melting process are in the canister from the beginning,
In addition, if the metal content of the miscellaneous solid waste to be treated is sufficiently large, the melting treatment can be performed without having to separately charge the waste during treatment.

【0015】また、本発明の雑固体廃棄物溶融用高周波
誘導炉は、キャニスタを囲い込んでキャニスタの内容物
に高周波エネルギーを供給する電磁コイルと、電磁コイ
ルに電力を供給する高周波電源装置と、キャニスタを載
置して電磁コイル内を昇降する昇降台を備える。本発明
の高周波誘導炉では、昇降台が高さ偏向機構と溶湯温度
測定装置を備えて、誘導加熱工程中にキャニスタを適宜
の高さに変更でき、また金属溶湯温度に基づいて供給電
力を調整することができるように構成されていることを
特徴とする。
Further, the high frequency induction furnace for melting miscellaneous solid waste of the present invention comprises: an electromagnetic coil surrounding the canister and supplying high frequency energy to the contents of the canister; a high frequency power supply for supplying power to the electromagnetic coil; An elevator is provided for mounting the canister and elevating the electromagnetic coil. In the high-frequency induction furnace according to the present invention, the lifting table includes a height deflection mechanism and a molten metal temperature measuring device, so that the canister can be changed to an appropriate height during the induction heating process, and the supply power is adjusted based on the molten metal temperature. It is characterized by being constituted so that it can be done.

【0016】本発明の雑固体廃棄物溶融用高周波誘導炉
を用いることにより、電磁コイルを必要に応じて金属層
と非金属層の位置に変更し、金属溶湯の温度が所定の温
度を超えないように監視しながら供給電力を調整して、
上記発明の雑固体廃棄物減容方法を適切に実施すること
ができる。また、本発明の雑固体廃棄物溶融用高周波誘
導炉は、キャニスタを電磁コイルの位置に取り込む昇降
台が途中の高さでも保持できるようになっているところ
に大きな特徴を有するもので、従来の高周波誘導炉に対
して僅かな改良を施せば足り、また既存の高周波誘導炉
の改造によっても構成することができる。
By using the high frequency induction furnace for melting solid wastes of the present invention, the position of the electromagnetic coil is changed to the position of the metal layer and the non-metal layer as required, so that the temperature of the molten metal does not exceed a predetermined temperature. And adjust the power supply while monitoring
The miscellaneous solid waste volume reduction method of the present invention can be appropriately performed. Further, the high-frequency induction furnace for melting miscellaneous solid waste of the present invention has a great feature in that the lifting platform that takes the canister into the position of the electromagnetic coil can be held at an intermediate height, and the conventional It is enough to make a small improvement to the high-frequency induction furnace, or it can be constructed by modifying an existing high-frequency induction furnace.

【0017】本発明の雑固体廃棄物溶融用高周波誘導炉
は、さらに、キャニスタに雑廃棄物を供給する雑固体供
給装置を付属して、誘導加熱工程中適宜に前記キャニス
タ内に雑固体廃棄物を追加することができるようにする
ことが好ましい。なお、雑固体廃棄物溶融用誘導炉に使
用するキャニスタは、非導電性セラミックスから形成さ
れ、中に導電性のスリーブを収納できるようなものであ
ることが好ましい。
The high-frequency induction furnace for melting miscellaneous solid waste according to the present invention further includes a miscellaneous solid supply device for supplying miscellaneous waste to the canister, and the miscellaneous solid waste is appropriately stored in the canister during the induction heating step. Is preferably added. It is preferable that the canister used for the induction furnace for melting miscellaneous solid wastes is formed of non-conductive ceramics and can store a conductive sleeve therein.

【0018】[0018]

【発明の実施の形態】以下、本発明について実施例に基
づき図面を参照して詳細に説明する。図1は本発明の1
実施例における雑固体廃棄物溶融用高周波誘導炉の構成
図である。また、図2と図3は、本実施例の高周波誘導
炉の運転方法を説明する図面である。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, the present invention will be described in detail based on embodiments with reference to the drawings. FIG. 1 shows one embodiment of the present invention.
It is a lineblock diagram of the high frequency induction furnace for miscellaneous solid waste melting in an example. FIG. 2 and FIG. 3 are diagrams for explaining a method of operating the high-frequency induction furnace of the present embodiment.

【0019】図1にあるように、電磁コイル1の下に昇
降台2が設置されていて、距離設定が可能な駆動装置3
により上下方向に駆動される。電磁コイル1には高周波
電源5から出力調整された高周波電流が供給される。高
周波誘導炉の上方には、雑固体供給装置6が設備されて
いて、適宜に雑固体廃棄物をキャニスタ10に投入する
ことができる。さらに、キャニスター10の中に導電性
スリーブ4が投入される。
As shown in FIG. 1, a driving device 3 in which a lift 2 is installed under an electromagnetic coil 1 and a distance can be set.
Driven in the vertical direction. A high-frequency current whose output has been adjusted is supplied to the electromagnetic coil 1 from a high-frequency power supply 5. Above the high-frequency induction furnace, a miscellaneous solids supply device 6 is provided so that miscellaneous solid waste can be appropriately charged into the canister 10. Further, the conductive sleeve 4 is put into the canister 10.

【0020】また、昇降台2には熱電対などの温度検出
端7が設けられていてキャニスター10底部の温度を計
測し温度計8に表示する。この温度から金属溶湯の温度
を推定することができる。なお、図には表示していない
が、誘導炉の周囲は断熱材で囲繞して無駄な放熱を防ぐ
ようになっていることはいうまでもない。また、キャニ
スター10を高周波誘導炉の下に搬入するコンベヤと搬
出するコンベヤが設備されている。
The lift 2 is provided with a temperature detecting end 7 such as a thermocouple. The temperature at the bottom of the canister 10 is measured and displayed on a thermometer 8. From this temperature, the temperature of the molten metal can be estimated. Although not shown in the figure, it goes without saying that the periphery of the induction furnace is surrounded by a heat insulating material to prevent useless heat radiation. Further, a conveyor for carrying the canister 10 under the high-frequency induction furnace and a conveyor for carrying out the canister 10 are provided.

【0021】キャニスタ10は、例えばアルミナや酸化
ケイ素等の安価で比較的融点が高い非導電性物質で形成
され、導電性スリーブ4は例えば黒鉛等の比重が小さい
導電性物質で形成されている。非金属溶湯の平均比重は
約3.0であり、黒鉛系材料の比重は例えば約1.8で
あるので、導電性スリーブ4は非金属溶湯層12に対し
て十分に浮力を得ることができる。
The canister 10 is formed of an inexpensive and non-conductive material having a relatively high melting point, such as alumina or silicon oxide, and the conductive sleeve 4 is formed of a conductive material having a small specific gravity, such as graphite. Since the average specific gravity of the non-metallic molten metal is about 3.0 and the specific gravity of the graphite-based material is, for example, about 1.8, the conductive sleeve 4 can sufficiently obtain buoyancy with respect to the non-metallic molten layer 12. .

【0022】誘導加熱を用いた雑固体廃棄物の溶融処理
では、初めに金属成分を溶融させて、その後に金属溶湯
の温度を上昇させて伝熱により非金属成分を溶融させ
る。このため、初めは、金属成分の割合を大きくした雑
固体廃棄物をキャニスターに仕込み、図2(a)に説明
するように、キャニスター10の下層部に電磁コイル1
を当て高周波電力を供給して誘導加熱する。
In the melting treatment of miscellaneous solid waste using induction heating, the metal component is first melted, and then the temperature of the molten metal is raised to melt the non-metal component by heat transfer. For this reason, first, the miscellaneous solid waste having a large proportion of the metal component is charged into the canister, and as shown in FIG.
And induction heating by supplying high frequency power.

【0023】処理工程を開始する前に、昇降台2をコン
ベヤの上面位置まで下げて、コンベヤにより搬入されて
きたキャニスタ10を台上に受け入れる。キャニスター
10を搭載した昇降台2は、駆動装置3により電磁コイ
ル2の中にせり上げられて、キャニスタ10の底部が電
磁コイル1に対応する位置で停止する。雑固体供給装置
6により、キャニスター10の中に金属成分の割合の大
きい雑固体廃棄物が投入される。次に、雑固体廃棄物の
上に導電性スリーブ4が載せられる。なお、初めの内容
物は誘導炉に搬入する前にキャニスター10に仕込んで
おいても良い。
Before starting the processing steps, the lifting platform 2 is lowered to the upper surface of the conveyor, and the canister 10 carried in by the conveyor is received on the platform. The lift 2 on which the canister 10 is mounted is lifted into the electromagnetic coil 2 by the driving device 3, and the bottom of the canister 10 stops at a position corresponding to the electromagnetic coil 1. By the miscellaneous solid supply device 6, miscellaneous solid waste having a high metal component ratio is charged into the canister 10. Next, the conductive sleeve 4 is mounted on the miscellaneous solid waste. The initial contents may be charged in the canister 10 before being carried into the induction furnace.

【0024】キャニスター10を取り囲んだ電磁コイル
1に高周波電源5から高周波電流を流すと、金属成分が
誘導発熱して溶融し雑固体廃棄物の空間を縫って滴り下
り、底に溜まって金属溶湯層11を形成する。非金属成
分は非導電性物質であるから電磁コイル1による誘導発
熱はないが、金属溶湯が誘導発熱により非金属成分の融
点以上に昇温して、伝熱により非金属成分を溶融し非金
属層12を形成する。非金属成分が金属層を覆って保温
効果を持つので、金属溶湯の温度上昇は容易である。
When a high-frequency current is supplied from the high-frequency power supply 5 to the electromagnetic coil 1 surrounding the canister 10, the metal component is induced to generate heat, melts, sews down the space of the miscellaneous solid waste, and drops down at the bottom to form a molten metal layer. 11 is formed. Since the non-metallic component is a non-conductive substance, there is no induction heat generated by the electromagnetic coil 1, but the molten metal rises to a temperature equal to or higher than the melting point of the non-metallic component due to the induced heat and melts the non-metallic component by heat transfer. The layer 12 is formed. Since the non-metal component covers the metal layer and has a heat retaining effect, the temperature rise of the molten metal is easy.

【0025】キャニスタ10の中に形成される非金属溶
湯層12には導電性スリーブ4が浮んでいる。導電性ス
リーブ4は円筒状をしており、電磁コイル2に高周波電
流が流れるために発生する磁場により自然にキャニスタ
1の中央位置に納まる。なお、非金属成分の加熱には、
表面に浮遊する導電性スリーブ4に発生する誘導熱も寄
与するが、初期の状態では電磁コイル1がキャニスター
10の下層部にあって導電性スリーブ4から離れていて
エネルギーは僅かしか分配されないので、導電性スリー
ブ4の寄与は限られる。
The conductive sleeve 4 is floating on the non-metallic melt layer 12 formed in the canister 10. The conductive sleeve 4 has a cylindrical shape, and is naturally located at the center of the canister 1 due to a magnetic field generated when a high-frequency current flows through the electromagnetic coil 2. The heating of the non-metallic component
The induction heat generated in the conductive sleeve 4 floating on the surface also contributes, but in the initial state, the electromagnetic coil 1 is located below the canister 10 and is separated from the conductive sleeve 4 and only a small amount of energy is distributed. The contribution of the conductive sleeve 4 is limited.

【0026】雑固体中の非金属成分は断熱材やコンクリ
ートなどであるが、途中で追加される雑固体の溶融を効
率よく行うためにも非金属成分の温度を1400°から
1500℃程度と、溶融点よりかなり高温にして処理す
ることが好ましい。一方、キャニスタ10がアルミナ系
の材料で形成される場合、キャニスタ10の耐熱温度は
1700°から1800℃程度であるので、キャニスタ
10内の金属溶湯温度は1500°から1600℃程度
に抑えている。
The non-metal component in the miscellaneous solid is a heat insulating material, concrete, or the like. In order to efficiently melt the miscellaneous solid added in the middle, the temperature of the non-metal component is set to about 1400 ° to 1500 ° C. Preferably, the treatment is performed at a temperature considerably higher than the melting point. On the other hand, when the canister 10 is formed of an alumina-based material, the heat-resistant temperature of the canister 10 is about 1700 ° C. to 1800 ° C., so that the temperature of the molten metal in the canister 10 is suppressed to about 1500 ° C. to 1600 ° C.

【0027】非金属成分の溶融が進んだところで、非金
属廃棄物を雑固体供給装置6からキャニスター10に投
入する。従来の方法では、新たに供給された非金属成分
を溶融するため供給電力を増加するので、金属溶湯層の
温度が上昇して炉壁に損傷を与える場合があった。本実
施例では、図2(b)に示すように、昇降台2を降下さ
せて電磁コイル4を非金属溶融層12に浮かぶ導電性ス
リーブ4に対応する位置に移動し、電磁スリーブ4に誘
導される発熱量の割合をより大きくして、十分な熱量が
非金属廃棄物に伝導するようにする。このとき、金属溶
湯層11に割り当てられるエネルギーの割合は減少する
ので、高周波電源5の出力を調整して金属溶湯層11の
温度が炉壁を損傷させない温度になるようにする。
When the melting of the nonmetallic component has progressed, the nonmetallic waste is charged from the miscellaneous solid supply device 6 into the canister 10. In the conventional method, the supply power is increased in order to melt the newly supplied non-metal component, so that the temperature of the molten metal layer rises and may damage the furnace wall. In this embodiment, as shown in FIG. 2B, the elevator 2 is lowered to move the electromagnetic coil 4 to a position corresponding to the conductive sleeve 4 floating on the non-metallic molten layer 12 and guide the electromagnetic coil 4 to the electromagnetic sleeve 4. The proportion of generated heat is increased so that sufficient heat is conducted to the non-metallic waste. At this time, since the ratio of the energy allocated to the molten metal layer 11 decreases, the output of the high-frequency power supply 5 is adjusted so that the temperature of the molten metal layer 11 becomes a temperature that does not damage the furnace wall.

【0028】図3は、雑固体廃棄物を追加投入したとき
の状態変化を図式的に説明するグラフである。図3
(a)はキャニスター10に対する電磁コイル1の高さ
の変化を表し、図3(b)は高周波電源5の出力を表
し、図3(c)は金属溶湯層11と非金属溶湯層12の
それぞれに電磁誘導により供給される誘導発熱量の変化
を表し、図3(d)は金属溶湯層11の温度と非金属溶
湯層12の表層温度の変化を表す。
FIG. 3 is a graph schematically illustrating a state change when miscellaneous solid waste is additionally charged. FIG.
3A shows a change in height of the electromagnetic coil 1 with respect to the canister 10, FIG. 3B shows an output of the high-frequency power supply 5, and FIG. FIG. 3D shows a change in the amount of induced heat supplied by electromagnetic induction, and FIG. 3D shows a change in the temperature of the metal melt layer 11 and the surface temperature of the non-metal melt layer 12.

【0029】電磁コイル1の高さは、初期における金属
廃棄物の誘導発熱により金属と非金属の溶湯層が形成さ
れた後、新たに雑固体廃棄物が追加されたときに、導電
性スリーブ4の位置まで持ち上げられる。高周波出力
は、雑固体廃棄物の追加投入により低下した金属溶湯層
11の温度を回復するように増加させられる。金属溶湯
層と非金属溶湯層への供給熱量は、コイル高さと高周波
出力の変化により変化し、これらの温度もこれに伴って
変化する。
The height of the electromagnetic coil 1 is set such that when a molten solid layer of metal and non-metal is formed by the induced heat generation of the metal waste in the initial stage, and a new miscellaneous solid waste is added, the conductive sleeve 4 Up to the position. The high-frequency output is increased so as to recover the temperature of the molten metal layer 11 lowered by the additional introduction of the miscellaneous solid waste. The amount of heat supplied to the molten metal layer and the non-metallic molten layer changes according to changes in the coil height and the high-frequency output, and their temperatures also change accordingly.

【0030】さらに詳しく説明すると、始めに金属成分
を溶融しきるするまでは、キャニスター10に対する電
磁コイル1の高さはキャニスター10の底付近に対応す
る低い位置に固定され、高周波電源5も金属溶湯層11
の温度が炉壁の危険温度より低い適当な温度になるよう
な出力を維持する。この状態で新たに雑固体廃棄物がキ
ャニスター10の中に投入されると、非金属溶湯層11
の表面温度が低下し、これに伴い金属溶湯層11からの
伝熱量も増加するので金属溶湯層11の温度も若干低下
する。
More specifically, the height of the electromagnetic coil 1 with respect to the canister 10 is fixed at a low position corresponding to the vicinity of the bottom of the canister 10 until the metal component is completely melted first, and the high frequency power supply 5 is also connected to the molten metal layer. 11
Is maintained at an appropriate temperature such that the temperature is lower than the dangerous temperature of the furnace wall. When new miscellaneous solid waste is put into the canister 10 in this state, the non-metallic molten layer 11
, The amount of heat transferred from the molten metal layer 11 increases, and the temperature of the molten metal layer 11 also slightly decreases.

【0031】ここで、電磁コイル1の相対位置を導電性
スリーブ4に対応するところまで移動させると、金属溶
湯層11の発熱量が減少し、導電性スリーブ4側の誘導
発熱量が増大して、非金属溶湯層12の温度は若干回復
する。さらに、金属溶湯層11の温度が炉壁の損傷温度
以下の適当な温度になるまで高周波電力を増加させる。
すると、導電性スリーブ4を介して非金属雑固体廃棄物
に供給される熱量が増加し、新たに追加された廃棄物は
迅速に溶融する。なお、電磁コイル1の位置調整後に金
属溶湯層の温度変化を観測することにより最適の高周波
電力増加量を算出して高周波出力を調整するようにして
も良いが、追加投入する雑固体廃棄物の量に基づいて最
適な高周波電力を推定して電磁コイル位置調整と同時に
高周波出力調整することもできる。
Here, when the relative position of the electromagnetic coil 1 is moved to a position corresponding to the conductive sleeve 4, the calorific value of the molten metal layer 11 decreases, and the induced calorific value on the conductive sleeve 4 side increases. Then, the temperature of the non-metallic molten layer 12 slightly recovers. Further, the high-frequency power is increased until the temperature of the molten metal layer 11 becomes an appropriate temperature equal to or lower than the damage temperature of the furnace wall.
Then, the amount of heat supplied to the non-metallic miscellaneous solid waste via the conductive sleeve 4 increases, and the newly added waste quickly melts. The optimum high-frequency power increase may be calculated by observing the temperature change of the molten metal layer after adjusting the position of the electromagnetic coil 1 to adjust the high-frequency output. The optimum high-frequency power can be estimated based on the amount, and the high-frequency output can be adjusted simultaneously with the adjustment of the position of the electromagnetic coil.

【0032】廃棄物が溶融したら、昇降台2をコンベヤ
の位置まで下降させて搬出コンベヤに移し冷却場所に移
動して、自然放冷により冷却する。冷却したキャニスタ
ー10は、ドラム缶に入れて隙間をモルタルで塞いで廃
棄体とする。なお、導電性スリーブ4は冷却前に回収し
て繰り返し利用することもできる。
When the waste is melted, the elevator 2 is lowered to the position of the conveyor, moved to the carry-out conveyor, moved to the cooling place, and cooled by natural cooling. The cooled canister 10 is put into a drum and the gap is closed with mortar to be a waste. The conductive sleeve 4 can be collected before cooling and used repeatedly.

【0033】このようにして、雑固体廃棄物をすべて溶
融することにより、形状を有する固体物が流体化して空
間を埋め、容積が著しく減少するので、非金属成分割合
の大きな低レベル放射性廃棄物についても経済的な処理
が可能となる。また、キャニスター内部の温度は炉壁を
損傷する温度以下に管理されるので、キャニスターは十
分頑丈で炉壁の崩壊や漏洩を起こさず安全に廃棄物を収
納して長期保管することができる。なお、上記実施例に
おいては、設備改良の容易性に鑑みて、電磁コイル1の
相対高さ変更を電磁コイル1を搭載する昇降台2に途中
位置で停止して保持できるような駆動装置3により行う
ものについて記載したが、電磁コイル1の方を上下方向
に移動させるようにしても良いことはいうまでもない。
[0033] In this way, by melting all the miscellaneous solid waste, the solid matter having a shape becomes fluid and fills the space, and the volume is remarkably reduced. Can also be economically processed. Further, since the temperature inside the canister is controlled to a temperature lower than the temperature at which the furnace wall is damaged, the canister is sufficiently strong and can safely store waste and store it for a long period without causing collapse or leakage of the furnace wall. In the above embodiment, in view of the facility improvement, the drive device 3 is capable of stopping the change of the relative height of the electromagnetic coil 1 at an intermediate position on the lift 2 on which the electromagnetic coil 1 is mounted. Although what is performed has been described, it goes without saying that the electromagnetic coil 1 may be moved in the vertical direction.

【0034】[0034]

【発明の効果】以上説明したとおり、本発明の雑固体廃
棄物溶融用高周波誘導炉によれば、金属溶湯の温度を管
理してキャニスターに損傷を与えないようにして非金属
が含まれる雑固体廃棄物の溶融減容処理をすることがで
きる。また、従来の高周波誘導炉に多少の改良を加える
だけで、本発明の装置にすることができるので、経済的
であり、さらに、金属溶湯層を過剰に加熱することがな
いので運転費用も節減することができる。
As described above, according to the high-frequency induction furnace for melting miscellaneous solid waste of the present invention, the temperature of the molten metal is controlled so as not to damage the canister, and the miscellaneous solid containing non-metals is prevented. Melt volume reduction of waste can be performed. Further, the apparatus of the present invention can be made by only slightly improving the conventional high-frequency induction furnace, so that the apparatus is economical. Further, since the molten metal layer is not excessively heated, the operating cost is reduced. can do.

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

【図1】本発明の1実施例における雑固体廃棄物溶融用
高周波誘導炉の断面図である。
FIG. 1 is a cross-sectional view of a high-frequency induction furnace for melting miscellaneous solid waste in one embodiment of the present invention.

【図2】本実施例の雑固体廃棄物溶融用高周波誘導炉内
の熱の流れを示す図である。
FIG. 2 is a diagram showing a flow of heat in a high-frequency induction furnace for melting miscellaneous solid waste according to the present embodiment.

【図3】本実施例の運転状態における状態変化を示すグ
ラフである。
FIG. 3 is a graph showing a state change in an operation state of the embodiment.

【図4】従来の雑固体廃棄物溶融用高周波誘導炉の断面
図である。
FIG. 4 is a cross-sectional view of a conventional high-frequency induction furnace for melting miscellaneous solid waste.

【符号の説明】[Explanation of symbols]

1 電磁コイル 2 昇降台 3 昇降台駆動装置 4 導電性スリーブ 5 高周波電源 6 雑固体供給装置 7 温度検出端 8 温度計 10 キャニスタ 11 金属溶湯層 12 非金属溶湯層 REFERENCE SIGNS LIST 1 electromagnetic coil 2 elevator 3 elevator driver 4 conductive sleeve 5 high-frequency power supply 6 miscellaneous solids supply device 7 temperature detector 8 thermometer 10 canister 11 molten metal layer 12 non-metal molten layer

フロントページの続き Fターム(参考) 3K059 AB03 AB08 AB14 AB16 AB19 AB20 AB27 AB28 AC33 AD03 AD34 4D004 AA16 AA31 AA33 AB09 CA29 CB33 CB41 Continued on the front page F term (reference) 3K059 AB03 AB08 AB14 AB16 AB19 AB20 AB27 AB28 AC33 AD03 AD34 4D004 AA16 AA31 AA33 AB09 CA29 CB33 CB41

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 金属と非金属が混合した低レベル放射性
雑固体廃棄物をキャニスタに収納して高周波誘導炉内に
載置し、該雑固体廃棄物を高周波誘導加熱によりキャニ
スタ内で溶融して減容する低レベル放射性雑固体廃棄物
減容方法において、前記キャニスタを前記高周波誘導炉
内の電磁コイルに対向する位置に置き、初めに金属の割
合が大きい雑固体廃棄物と導電性スリーブを前記キャニ
スターに投入し、前記キャニスタに投入した金属が溶融
するまでは前記電磁コイルを前記キャニスタ内の底部に
対応する位置に据え主として金属層の加熱を行って非金
属をも溶融させ生成した金属層の上に前記導電性スリー
ブを浮遊させ、その後非金属の割合が大きい廃棄物を投
入したときに前記電磁コイルの相対的位置を前記導電性
スリーブに対応する位置まで動かして非金属の加熱を主
に行うとともに、電磁コイルの出力を金属層の温度が所
定の温度より低い値を維持するように調整することを特
徴とする雑固体廃棄物減容方法。
1. A low-level radioactive miscellaneous solid waste in which a metal and a non-metal are mixed is housed in a canister and placed in a high-frequency induction furnace, and the miscellaneous solid waste is melted in the canister by high-frequency induction heating. In the method for reducing the volume of low-level radioactive miscellaneous solid waste to reduce the volume, the canister is placed at a position facing the electromagnetic coil in the high-frequency induction furnace, and the miscellaneous solid waste having a large proportion of metal and a conductive sleeve are first placed on the canister Until the metal charged into the canister melts into the canister, the electromagnetic coil is placed at a position corresponding to the bottom in the canister and mainly heats the metal layer to melt the non-metal, thereby forming the metal layer. The conductive sleeve is floated on the top, and then the relative position of the electromagnetic coil corresponds to the conductive sleeve when a large amount of non-metal waste is thrown in. A method for reducing the volume of miscellaneous solid waste, characterized in that the heating of the non-metal is mainly performed by moving to a position, and the output of the electromagnetic coil is adjusted so that the temperature of the metal layer is maintained at a value lower than a predetermined temperature.
【請求項2】 前記キャニスタを搭載する台を昇降する
ことにより前記電磁コイルと前記キャニスタの相対的位
置を調整することを特徴とする請求項1記載の雑固体廃
棄物減容方法。
2. The method according to claim 1, wherein a relative position between the electromagnetic coil and the canister is adjusted by moving up and down a table on which the canister is mounted.
【請求項3】 請求項1または2記載の雑固体廃棄物減
容方法において、前記キャニスターを高周波誘導炉内に
据えてから内容物を添加する代わりに、前記キャニスタ
ーに予め処理対象の雑固体廃棄物と導電性スリーブを仕
込んでおくことを特徴とする雑固体廃棄物減容方法。
3. The method for reducing the volume of miscellaneous solid waste according to claim 1 or 2, instead of adding the content after placing the canister in a high-frequency induction furnace, adding the content to the canister in advance. A method for reducing the volume of miscellaneous solid waste, which comprises charging a material and a conductive sleeve.
【請求項4】 キャニスタを囲い込んでキャニスタの内
容物に高周波エネルギーを供給する電磁コイルと、前記
電磁コイルに電力を供給する高周波電源装置と、キャニ
スタを載置して前記電磁コイル内を昇降する昇降台を備
える高周波誘導炉であって、前記昇降台が誘導加熱工程
中に適宜の高さに変更でき、キャニスタ内の金属溶湯温
度の測定装置を備え、前記高周波電源装置が該金属溶湯
温度に基づいて前記電磁コイルに供給する電力を調整す
ることができるように構成されていることを特徴とする
雑固体廃棄物溶融用高周波誘導炉。
4. An electromagnetic coil that surrounds the canister and supplies high-frequency energy to the contents of the canister, a high-frequency power supply that supplies electric power to the electromagnetic coil, and a canister mounted thereon and moved up and down in the electromagnetic coil. A high-frequency induction furnace including a lift table, wherein the lift table can be changed to an appropriate height during an induction heating step, and a measuring device for measuring a metal melt temperature in a canister is provided. A high-frequency induction furnace for melting solid wastes, characterized in that the power supplied to the electromagnetic coil can be adjusted based on the electric power.
【請求項5】 さらに、キャニスタに雑廃棄物を供給す
る雑固体供給装置を付属して、誘導加熱工程中適宜に前
記キャニスタ内に雑固体廃棄物を追加することができる
ようにしたことを特徴とする請求項3記載の雑固体廃棄
物溶融用高周波誘導炉。
5. A miscellaneous solid waste supply device for supplying miscellaneous waste to the canister is provided, so that miscellaneous solid waste can be appropriately added to the canister during the induction heating step. The high-frequency induction furnace for melting solid wastes according to claim 3.
【請求項6】 前記雑固体廃棄物溶融用誘導炉に使用す
るキャニスタは、非導電性セラミックスから形成され、
中に導電性のスリーブを収納できるようになっているこ
とを特徴とする請求項3または4記載の雑固体廃棄物溶
融用高周波誘導炉。
6. A canister used for the induction furnace for melting solid wastes is formed of non-conductive ceramics,
The high-frequency induction furnace for melting solid wastes according to claim 3 or 4, wherein a conductive sleeve can be accommodated therein.
JP2001142936A 2001-05-14 2001-05-14 Miscellaneous solid waste volume reduction method and high-frequency induction furnace for melting miscellaneous solid waste Expired - Lifetime JP3563041B2 (en)

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JP2008197068A (en) * 2007-02-15 2008-08-28 Toshiba Corp Waste cable disposal device and method
JP2008267733A (en) * 2007-04-23 2008-11-06 Tohoku Univ High frequency induction furnace and solid melting method
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Publication number Priority date Publication date Assignee Title
JP2008197068A (en) * 2007-02-15 2008-08-28 Toshiba Corp Waste cable disposal device and method
JP4672685B2 (en) * 2007-02-15 2011-04-20 株式会社東芝 Waste cable processing apparatus and method
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