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JP2855265B2 - Electric resistance melting furnace - Google Patents

Electric resistance melting furnace

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Publication number
JP2855265B2
JP2855265B2 JP9261496A JP9261496A JP2855265B2 JP 2855265 B2 JP2855265 B2 JP 2855265B2 JP 9261496 A JP9261496 A JP 9261496A JP 9261496 A JP9261496 A JP 9261496A JP 2855265 B2 JP2855265 B2 JP 2855265B2
Authority
JP
Japan
Prior art keywords
particles
carbon material
electric resistance
heat
melting tank
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP9261496A
Other languages
Japanese (ja)
Other versions
JPH09280750A (en
Inventor
健二 清水
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.)
Daiichi KK
Original Assignee
Daiichi KK
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 Daiichi KK filed Critical Daiichi KK
Priority to JP9261496A priority Critical patent/JP2855265B2/en
Publication of JPH09280750A publication Critical patent/JPH09280750A/en
Application granted granted Critical
Publication of JP2855265B2 publication Critical patent/JP2855265B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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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、電気抵抗式溶融炉
に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an electric resistance melting furnace.

【0002】[0002]

【従来の技術】従来の電気抵抗式溶融炉は、図7に示す
ように、炉体1内に3本の電極2a,2b,2cを配置
し、これら電極2a,2b,2cに電源設備3から3相
交流を印加して通電することにより炉体1内のごみ焼却
灰等の被溶融物4をジュール熱で発熱させて溶融し、得
られた溶融メタルは出湯口5より流出させ、溶融スラグ
4aはスラグ排出口6より排出させる構造であった。な
お、7は被溶融物投入口、8は排気口である。
2. Description of the Related Art In a conventional electric resistance melting furnace, as shown in FIG. 7, three electrodes 2a, 2b, 2c are arranged in a furnace body 1, and power supply equipment 3 is connected to these electrodes 2a, 2b, 2c. The molten metal 4 such as the refuse incineration ash in the furnace body 1 is heated and melted by Joule heat by applying a three-phase alternating current from the furnace, and the obtained molten metal is discharged from the tap hole 5 and melted. The slag 4a was configured to be discharged from the slag discharge port 6. Reference numeral 7 denotes an inlet for the material to be melted, and 8 denotes an exhaust port.

【0003】[0003]

【発明が解決しようとする課題】しかしながら、従来の
このような構造の電気抵抗式溶融炉では、隣接する電極
2a,2b,2c間にある被溶融物4は通電により容易
に発熱するが、電極2a,2b,2cと炉体1との間に
ある被溶融物4には通電がなされず、電極側で発生した
溶融メタルからの熱で徐々に加熱されて溶融するので、
溶融効率が非常に悪い問題点があった。
However, in the conventional electric resistance type melting furnace having such a structure, the material to be melted 4 between the adjacent electrodes 2a, 2b, 2c easily generates heat when energized. Electric current is not applied to the material 4 to be melted between the furnace body 1 and 2a, 2b, 2c, and is gradually heated and melted by the heat from the molten metal generated on the electrode side.
There was a problem that the melting efficiency was very poor.

【0004】本発明の目的は、溶融を効率よく行わせる
ことができる電気抵抗式溶融炉を提供することにある。
本発明の他の目的は、被溶融物をその周囲から効率よく
予熱できる電気抵抗式溶融炉を提供することにある。本
発明の他の目的は、加熱手段の消耗を抑制できる電気抵
抗式溶融炉を提供することにある。
[0004] An object of the present invention is to provide an electric resistance type melting furnace capable of performing melting efficiently.
Another object of the present invention is to provide an electric resistance type melting furnace capable of efficiently preheating a material to be melted from its surroundings. Another object of the present invention is to provide an electric resistance melting furnace capable of suppressing consumption of the heating means.

【0005】[0005]

【課題を解決するための手段】請求項1に記載の電気抵
抗式溶融炉は、耐熱性絶縁容器の対向面に電極板がそれ
ぞれ配置され、これら電極板の間の耐熱性絶縁容器内に
導電性溶融槽が配置され、該導電性溶融槽は各電極板に
対向する側の部分が1対の内部電極を構成するように耐
熱性絶縁材が介在されて電気的に分割され、各電極板と
導電性溶融槽との間の各空間にはカーボン物質の粒子が
充填されていることを特徴とする。
According to a first aspect of the present invention, there is provided an electric resistance melting furnace, wherein electrode plates are respectively arranged on opposing surfaces of a heat-resistant insulating container, and conductive melting is provided in the heat-resistant insulating container between the electrode plates. A tank is disposed, and the conductive melting tank is electrically divided with a heat-resistant insulating material interposed therebetween so that a portion on a side facing each electrode plate forms a pair of internal electrodes, and is electrically connected to each electrode plate. It is characterized in that each space between the conductive melting tank and the melting tank is filled with particles of a carbon material.

【0006】このような構造の電気抵抗式溶融炉では、
導電性溶融槽内に被溶融物を入れ、両電極板間に電圧を
かけると、電流は一方の電極板から該電極板と導電性溶
融槽がなす一方の内部電極との間のカーボン物質の粒子
層を通り、該一方の内部電極を通り、該導電性溶融槽内
の被溶融物を通り、該導電性溶融槽がなす他方の内部電
極を通り、該他方の内部電極と他方の電極板との間のカ
ーボン物質の粒子層を通り、該他方の電極板に流れるこ
とになる。各側のカーボン物質の粒子層に電流が流れる
と、隣接するカーボン物質の粒子間ではスパーク放電が
発生し、カーボン物質の粒子内では該カーボン物質の粒
子の抵抗によってジュール熱が発生するが、隣接するカ
ーボン物質の粒子間で発生するスパーク放電によりカー
ボン物質の粒子が発熱昇温され、昇温された結果カーボ
ン物質の粒子の電気抵抗が低下し、電流の流れが良くな
り多量のジュール熱が発生する。そして前記のスパーク
放電の熱とジュール熱が相加わってカーボン物質の粒子
の層内に高温が蓄熱され、これらカーボン物質の粒子の
層は非常に高温となる。
In an electric resistance melting furnace having such a structure,
When the material to be melted is placed in the conductive melting tank and a voltage is applied between the two electrode plates, a current flows from one electrode plate to the carbon material between the electrode plate and one internal electrode formed by the conductive melting tank. Through the particle layer, through the one internal electrode, through the material to be melted in the conductive melting tank, through the other internal electrode formed by the conductive melting tank, the other internal electrode and the other electrode plate And flows to the other electrode plate through the particle layer of the carbon material. When a current flows through the carbon material particle layer on each side, spark discharge occurs between adjacent carbon material particles, and Joule heat is generated within the carbon material particles due to the resistance of the carbon material particles. The carbon material particles are heated and heated by the spark discharge generated between the particles of the carbon material, and as a result, the electric resistance of the particles of the carbon material is reduced, the current flow is improved, and a large amount of Joule heat is generated. I do. Then, the heat of the spark discharge and the Joule heat are added to store a high temperature in the layer of the carbon material particles, and the layer of the carbon material particles becomes extremely high.

【0007】このような高温のカーボン物質の粒子層で
導電性溶融槽が包囲されて、該導電性溶融槽内の被溶融
物が均等に加熱される。
[0007] The conductive melting tank is surrounded by the particle layer of such a high-temperature carbon material, and the material to be melted in the conductive melting tank is uniformly heated.

【0008】被溶融物の電気抵抗は温度によって大きく
差があるが、この電気抵抗式溶融炉では導電性溶融槽内
の被溶融物は周囲のカーボン物質の粒子層により均等に
加熱されるため均等な電気抵抗となり、各部に均等に電
流が流れ、未溶融の被溶融物は高温のカーボン物質の粒
子層から均等な加熱と均等に流れる電流により、全体的
に速やかに昇温され溶融流動状態になり、従って被溶融
物の溶融を効率よく行わせることができる。
Although the electric resistance of the material to be melted greatly varies depending on the temperature, in this electric resistance type melting furnace, the material to be melted in the conductive melting tank is evenly heated by the surrounding carbon material particle layer, so that the electric resistance is uniform. The electric current flows uniformly in each part, and the unmelted material is quickly heated as a whole by the uniform heating and uniform current from the high-temperature carbon material particle layer, and the molten material is in a molten fluid state. Therefore, the material to be melted can be efficiently melted.

【0009】請求項2に記載の電気抵抗式溶融炉は、カ
ーボン物質の粒子が充填されている耐熱性絶縁容器内の
各箇所の上部がそれぞれ蓋で閉塞されていることを特徴
とする。
According to a second aspect of the present invention, there is provided an electric resistance melting furnace, wherein upper portions of respective portions in the heat-resistant insulating container filled with particles of the carbon material are closed with lids.

【0010】このようにカーボン物質の粒子が充填され
ている耐熱性絶縁容器内の各箇所の上部をそれぞれ蓋で
閉塞すると、空気が入りにくくなり、カーボン物質の粒
子の消耗を抑制することができる。
When the upper portions of the respective portions of the heat-resistant insulating container filled with the particles of the carbon material are closed with the lids, it becomes difficult for air to enter and the consumption of the particles of the carbon material can be suppressed. .

【0011】[0011]

【発明の実施の形態】図1乃至図4は、本発明に係る電
気抵抗式溶融炉における実施の形態の一例を示したもの
である。本例の電気抵抗式溶融炉は焼却灰や飛灰等を溶
融する溶融炉であって、底板9aと両側板9b,9cと
を備えたセラミックス製の耐熱性絶縁容器9の対向面の
空間にカーボン製の正負の電極板10a,10bがそれ
ぞれ取り付けられている。正負の電極板10a,10b
の外面には、通電導体11a,11bが接続されてい
る。
1 to 4 show an embodiment of an electric resistance melting furnace according to the present invention. The electric resistance type melting furnace of this example is a melting furnace for melting incineration ash, fly ash, and the like, and is provided in a space on a facing surface of a ceramic heat-resistant insulating container 9 having a bottom plate 9a and both side plates 9b and 9c. Positive and negative electrode plates 10a and 10b made of carbon are respectively attached. Positive and negative electrode plates 10a, 10b
Are connected to current-carrying conductors 11a and 11b.

【0012】これら正負の電極板10a,10bの間の
耐熱性絶縁容器9内の中央には、有底円筒状の導電性溶
融槽12が設置されている。該導電性溶融槽12は、正
負の電極板10a,10bに対向する側の部分が1対の
内部電極12a,12bを構成するように耐熱性絶縁材
12cが介在されて電気的に分割されている。内部電極
12a,12bはカーボンで形成され、耐熱性絶縁材1
2cはセラミックスで形成されている。該導電性溶融槽
12の側面には、溶融スラグ4aをオーバーフローさせ
るためにカーボン製のオーバーフロー管13が接続され
ている。
At the center of the heat-resistant insulating container 9 between the positive and negative electrode plates 10a and 10b, a bottomed cylindrical conductive melting tank 12 is provided. The conductive melting tank 12 is electrically divided with a heat-resistant insulating material 12c interposed therebetween such that a portion facing the positive and negative electrode plates 10a and 10b forms a pair of internal electrodes 12a and 12b. I have. The internal electrodes 12a and 12b are formed of carbon,
2c is formed of ceramics. An overflow pipe 13 made of carbon is connected to a side surface of the conductive melting tank 12 to overflow the molten slag 4a.

【0013】正負の電極板10a,10bと導電性溶融
槽12との間の各空間には、カーボン物質の粒子14
a,14bが充填されている。カーボン物質として、木
炭、石炭、活性炭、コークス等の加工炭が使用され、本
例では木炭が使用されている。カーボン物質の粒子14
a,14bの大きさは、5〜20mm程度である。導電性
溶融槽12が小さい場合には、5mm以下のカーボン物質
の粒子でも使用できる。カーボン物質の粒子14a,1
4bの大きさを大きくし過ぎると、隣接するカーボン物
質の粒子間の隙間が大きくなり過ぎ、カーボン物質の粒
子間の電流の流れが悪くなりジュール熱が高くならず、
好ましくない。
In each space between the positive and negative electrode plates 10a and 10b and the conductive melting tank 12, particles 14 of carbon material are provided.
a and 14b are filled. As the carbon substance, processed charcoal such as charcoal, coal, activated carbon, and coke is used, and in this example, charcoal is used. Particles of carbon material 14
The sizes of a and 14b are about 5 to 20 mm. When the conductive melting tank 12 is small, particles of a carbon material of 5 mm or less can be used. Particles 14a, 1 of carbon material
If the size of 4b is too large, the gap between the particles of the adjacent carbon material becomes too large, the current flow between the particles of the carbon material becomes poor, and the Joule heat does not increase,
Not preferred.

【0014】カーボン物質の粒子14a,14bが充填
されている耐熱性絶縁容器9内の各箇所の上部は、それ
ぞれ耐熱性絶縁材よりなる蓋15a,15bで閉塞され
ている。また、導電性溶融槽12の上部にも耐熱性絶縁
材よりなる蓋16が被せられている。蓋16を貫通して
被溶融物投入筒17が設けられ、蓋15bを貫通して排
気筒18が設けられている。導電性溶融槽12内の上部
側には、被溶融物4と溶融スラグを分離する隔壁19が
設けられている。
The upper portions of the respective portions in the heat-resistant insulating container 9 filled with the carbon material particles 14a and 14b are closed with lids 15a and 15b made of a heat-resistant insulating material, respectively. Further, a lid 16 made of a heat-resistant insulating material is also placed on the upper part of the conductive melting tank 12. A molten material charging cylinder 17 is provided through the lid 16, and an exhaust cylinder 18 is provided through the lid 15b. On the upper side in the conductive melting tank 12, a partition wall 19 for separating the molten material 4 and the molten slag is provided.

【0015】次に、このような構造の電気抵抗式溶融炉
の動作について説明する。導電性溶融槽12内に被溶融
物投入筒17から被溶融物4を投入し、正負の電極板1
0a,10bに通電導体11a,11bを経て図示しな
い直流電源設備から正負の直流電圧をかけると、電流は
正の電極板10aからカーボン物質の粒子14aの層、
一方の内部電極12a、被溶融物4、他方の内部電極1
2b、カーボン物質の粒子14bの層を経て負の電極板
10bに流れる。各側のカーボン物質の粒子14a,1
4bの層に電流が流れると、隣接するカーボン物質の粒
子間ではスパーク放電が発生し、カーボン物質の粒子1
4a,14b内では該カーボン物質の粒子14a,14
bの抵抗によってジュール熱が発生する。隣接するカー
ボン物質の粒子14a,14b間で発生するスパーク放
電によりカーボン物質の粒子14a,14bが発熱昇温
される。普通は隣接するカーボン物質の粒子14a,1
4b間の接点は電気抵抗が非常に高くなり電流の流れに
対して妨げとなるが、スパーク放電を起こすことにより
電流の流れの妨げにならないばかりか、スパーク放電に
より大きな発熱を起こす。
Next, the operation of the electric resistance type melting furnace having such a structure will be described. The molten material 4 is charged into the conductive melting tank 12 from the molten material charging cylinder 17, and the positive and negative electrode plates 1 are charged.
When a positive / negative DC voltage is applied from a DC power supply (not shown) via the current-carrying conductors 11a and 11b to the electrodes 0a and 10b, current flows from the positive electrode plate 10a to the layer of carbon material particles 14a,
One internal electrode 12a, the melt 4 and the other internal electrode 1
2b, flows to the negative electrode plate 10b through the layer of the carbon material particles 14b. Particles 14a, 1 of carbon material on each side
When a current flows through the layer 4b, a spark discharge is generated between adjacent carbon material particles, and the carbon material particles 1
4a, 14b, particles 14a, 14
Joule heat is generated by the resistance b. The particles 14a and 14b of the carbon material are heated and heated by spark discharge generated between the particles 14a and 14b of the adjacent carbon material. Usually, particles 14a, 1 of adjacent carbon material
The contact between the contacts 4b has a very high electric resistance and hinders the flow of current. However, spark discharge does not not only hinder the flow of current but also generates a large amount of heat due to spark discharge.

【0016】このように、スパーク放電により発熱昇温
された結果、カーボン物質の粒子14a,14bの電気
抵抗が低下し、電流の流れが良くなり多量のジュール熱
が発生する。そして前記のスパーク放電の熱とジュール
熱が相加わってカーボン物質の粒子14a,14bの層
内に高温が蓄熱され、これらカーボン物質の粒子14
a,14bの層は非常に高温となる。
As a result of the heat generated by the spark discharge, the electrical resistance of the carbon material particles 14a and 14b is reduced, the current flow is improved, and a large amount of Joule heat is generated. Then, the heat of the spark discharge and the Joule heat are added to store a high temperature in the layer of the particles 14a and 14b of the carbon material.
The layers a and 14b become very hot.

【0017】このような高温のカーボン物質の粒子14
a,14bの層で導電性溶融槽12が包囲されて、該導
電性溶融槽12内の被溶融物4が均等に加熱される。被
溶融物4の電気抵抗は温度によって大きく差があるが、
この電気抵抗式溶融炉では導電性溶融槽12内の被溶融
物4は周囲のカーボン物質の粒子14a,14bの層に
より均等に加熱されるため均等な電気抵抗となり、各部
に均等に電流が流れ、未溶融の被溶融物4は高温のカー
ボン物質の粒子14a,14bの層から均等な加熱と均
等に流れる電流により、全体的に速やかに溶融流動状態
になり、従って被溶融物4の溶融を効率よく行わせるこ
とができる。得られた溶融スラグ4aは、該導電性溶融
槽12内の底部側に溜まる。
The particles 14 of such a high-temperature carbon material
The conductive melting tank 12 is surrounded by the layers a and 14b, and the material to be melted 4 in the conductive melting tank 12 is uniformly heated. Although the electrical resistance of the material to be melted 4 greatly differs depending on the temperature,
In this electric resistance type melting furnace, the material 4 to be melted in the conductive melting tank 12 is uniformly heated by the layers of the surrounding carbon material particles 14a and 14b, so that the electric resistance is uniform, and the current flows uniformly in each part. The unmelted material 4 is quickly brought into a molten state as a whole by the uniform heating and the current flowing uniformly from the layer of the high-temperature carbon material particles 14a and 14b. It can be performed efficiently. The obtained molten slag 4 a accumulates on the bottom side in the conductive melting tank 12.

【0018】カーボン物質の粒子14a,14bが充填
されている耐熱性絶縁容器9内の各箇所の上部をそれぞ
れ蓋15a,15bで閉塞すると、空気が入りにくくな
り、カーボン物質の粒子14a,14bの消耗を抑制す
ることができる。カーボン物質の粒子14a,14bが
消耗して減少したら、減少分のカーボン物質の粒子14
a,14bを補充する。
When the upper portions of the respective portions in the heat-resistant insulating container 9 filled with the carbon material particles 14a and 14b are closed with lids 15a and 15b, respectively, it becomes difficult for air to enter, and the carbon material particles 14a and 14b Wear can be suppressed. When the carbon material particles 14a, 14b are consumed and reduced, the reduced carbon material particles 14 are reduced.
Refill a and 14b.

【0019】内径130 mmのカーボン製導電性溶融槽12
を用いた実験では、木炭よりなるカーボン物質の粒子1
4a,14bを用いた本発明の電気抵抗式溶融炉で、10
0 Aの定電流制御で直流電圧を正負の電極板10a,1
0bにかけた場合、該電極板10a,10b間は50Vに
荷電され、1時間に11.07 Kgの被溶融物4を溶融させる
ことができた。内径80 mm のカーボン製導電性溶融槽1
2を用いた実験では、木炭よりなるカーボン物質の粒子
14a,14bを用いた本発明の電気抵抗式溶融炉で、
60Aの定電流制御で直流電圧を正負の電極板10a,1
0bにかけた場合、該電極板10a,10b間は50Vに
荷電され、1時間に4.3 Kgの被溶融物4を溶融させるこ
とができた。
A carbon conductive melting tank 12 having an inner diameter of 130 mm
In the experiment using, particles 1 of carbon material consisting of charcoal
In the electric resistance melting furnace of the present invention using 4a and 14b, 10
The DC voltage is changed to the positive and negative electrode plates 10a, 1a by the constant current control of 0 A.
When the voltage was applied to 0b, the voltage between the electrode plates 10a and 10b was charged to 50 V, and 11.07 kg of the material to be melted 4 could be melted in one hour. 80mm inner diameter carbon conductive melting tank 1
2 using the electric resistance melting furnace of the present invention using carbon material particles 14a and 14b made of charcoal,
DC voltage is controlled by positive and negative electrode plates 10a, 1 by constant current control of 60A.
When the voltage was applied to 0b, the voltage between the electrode plates 10a and 10b was charged to 50 V, and 4.3 kg of the material to be melted 4 could be melted in one hour.

【0020】カーボン物質の粒子14a,14bを用い
ず、カーボン製導電性溶融槽12に直接荷電した場合に
は、被溶融物4内に溶融スラグの通路が形成され、100
Aの電流を流しても電圧が上昇されず、導電性溶融槽1
2内部に被溶融物4の溶融状態が形成されなかった。即
ち、特定の被溶融物4の中の通路に電流が流れ始め、そ
の部分ばかりが高温になって溶融し、電流が流れ易くな
り、ますます他の部分に電流が流れにくくなり、全体的
に電気的エネルギー入力が増加されないという結果にな
ったものと思われる。
When the carbon conductive melting tank 12 is directly charged without using the carbon material particles 14a and 14b, a molten slag passage is formed in the material 4 to be melted.
When the current of A flows, the voltage does not increase and the conductive melting tank 1
No molten state of the material to be melted 4 was formed inside 2. That is, current starts to flow in the passage in the specific material 4 to be melted, and only that portion becomes hot and melts, and the current easily flows, and the current hardly flows to other portions. It appears that the electrical energy input did not increase.

【0021】また、従来の3相交流の電気抵抗式溶融炉
と本発明の電気抵抗式溶融炉との被溶融物4の溶融能力
の比較をしたところ、従来の3相交流の電気抵抗式溶融
炉では炉表面積当たり300 Kg/m2 Hrの溶融能力であった
のに対し、本発明の電気抵抗式溶融炉では800 Kg/m2 Hr
の溶融能力であった。
A comparison of the melting ability of the object 4 to be melted between the conventional three-phase AC electric resistance melting furnace and the electric resistance melting furnace of the present invention shows that the conventional three-phase AC electric resistance melting furnace. The furnace had a melting capacity of 300 Kg / m 2 Hr per furnace surface area, whereas the electric resistance melting furnace of the present invention had a melting capacity of 800 Kg / m 2 Hr.
Melting ability.

【0022】図5,図6は、本発明で用いる導電性溶融
槽12の他の例を示したものである。本例の導電性溶融
槽12は、有底角筒状となっている。該導電性溶融槽1
2も、前述した例と同様に、正負の電極板10a,10
bに対向する側の部分が1対の内部電極12a,12b
を構成するように耐熱性絶縁材12cが介在されて電気
的に分割されている。このような構造の導電性溶融槽1
2でも、前述した例と同様な効果を得ることができる。
FIGS. 5 and 6 show another example of the conductive melting tank 12 used in the present invention. The conductive melting tank 12 of the present example has a bottomed rectangular tube shape. The conductive melting tank 1
2 also has positive and negative electrode plates 10a and 10
b is a pair of internal electrodes 12a and 12b
Are electrically divided with a heat-resistant insulating material 12c interposed therebetween. The conductive melting tank 1 having such a structure.
2, the same effect as in the above-described example can be obtained.

【0023】なお、図1及び図2に示す電気抵抗式溶融
炉では、耐熱性絶縁容器9の対向端面が開口されてい
て、そこを塞ぐように正負の電極板10a,10bがそ
れぞれ取り付けられているが、該耐熱性絶縁容器9の周
囲は閉じていて、その内部の対向内壁に正負の電極板1
0a,10bを配置する構造にすることもできる。ま
た、上記例では無いが、導電性溶融槽12の底部側に溶
融メタル4aを出湯させる出湯管を接続してもよい。ま
た、上記例では、直流通電方式について説明したが、本
発明の電気抵抗式溶融炉は、単相交流通電方式でも実施
することができる。また、この電気抵抗式溶融炉で溶融
される被溶融物はごみ焼却灰や飛灰等に限られるもので
はなく導電性のものであればよい。
In the electric resistance type melting furnace shown in FIGS. 1 and 2, the opposite end faces of the heat-resistant insulating container 9 are opened, and the positive and negative electrode plates 10a and 10b are respectively attached so as to close them. However, the periphery of the heat-resistant insulating container 9 is closed, and the positive and negative electrode plates 1
It is also possible to adopt a structure in which 0a and 10b are arranged. Although not the above example, a tapping pipe for tapping the molten metal 4a may be connected to the bottom side of the conductive melting tank 12. Further, in the above-described example, the DC energizing method has been described. However, the electric resistance type melting furnace of the present invention can also be implemented by a single-phase AC energizing method. The material to be melted in the electric resistance melting furnace is not limited to incineration ash or fly ash, but may be any conductive material.

【0024】[0024]

【発明の効果】請求項1に記載の電気抵抗式溶融炉は、
耐熱性絶縁容器の対向面に電極板をそれぞれ配置し、こ
れら電極板の間の耐熱性絶縁容器内に導電性溶融槽を配
置し、該導電性溶融槽は各電極板に対向する側の部分が
1対の内部電極を構成するように耐熱性絶縁材を介在さ
せて電気的に分割し、各電極板と導電性溶融槽との間の
各空間にはカーボン物質の粒子を充填した構造にしたの
で、両電極板間に電圧をかけるとこれら電極板間の構成
要素に電流が流れ、この電流の流れにより各側のカーボ
ン物質の粒子層の隣接するカーボン物質の粒子間ではス
パーク放電が発生し、カーボン物質の粒子内では該カー
ボン物質の粒子の抵抗によってジュール熱が発生する
が、隣接するカーボン物質の粒子間で発生するスパーク
放電によりカーボン物質の粒子が発熱昇温され、昇温さ
れた結果カーボン物質の粒子の電気抵抗が低下し、電流
の流れが良くなり多量のジュール熱が発生する。そして
前記のスパーク放電の熱とジュール熱が相加わってカー
ボン物質の粒子の層内に高温が蓄熱され、これらカーボ
ン物質の粒子の層は非常に高温となって導電性溶融槽を
周囲から加熱することができる。このため該導電性溶融
槽内の被溶融物を均等に加熱することができる。導電性
溶融槽内の被溶融物が周囲のカーボン物質の粒子層によ
り均等に加熱されると、該被溶融物の電気抵抗も略均等
となり、各部に均等に電流が流れ、未溶融の被溶融物は
均等な加熱と均等に流れる電流により、全体的に速やか
に溶融流動状態になり、従って被溶融物の溶融を効率よ
く行わせることができる。
The electric resistance type melting furnace according to claim 1 is
Electrode plates are arranged on the opposing surfaces of the heat-resistant insulating container, and a conductive melting tank is arranged in the heat-resistant insulating container between the electrode plates. Since the internal electrodes were electrically divided to form a pair of internal electrodes with a heat-resistant insulating material interposed between them, each space between each electrode plate and the conductive melting tank was filled with particles of carbon material. When a voltage is applied between the two electrode plates, a current flows through the components between the electrode plates, and a spark discharge occurs between particles of the adjacent carbon material in the carbon material particle layer on each side due to the flow of the current, Joule heat is generated in the particles of the carbon material due to the resistance of the particles of the carbon material, but the particles of the carbon material are heated and heated by spark discharge generated between the particles of the adjacent carbon material. Stuff The electrical resistance is lowered particles, a large amount of Joule heat better the flow of current is generated. Then, the heat of the spark discharge and the Joule heat are added to store a high temperature in the layer of the particles of the carbon material, and the layer of the particles of the carbon material becomes extremely high and heats the conductive melting tank from the surroundings. be able to. Therefore, the material to be melted in the conductive melting tank can be uniformly heated. When the material to be melted in the conductive melting tank is evenly heated by the surrounding carbon material particle layer, the electric resistance of the material to be melted is also substantially equal, an electric current flows uniformly to each part, and the unmelted material is melted. The object is quickly brought into a molten state as a whole by the uniform heating and the uniform flowing current, so that the object to be melted can be efficiently melted.

【0025】請求項2に記載の電気抵抗式溶融炉では、
カーボン物質の粒子が充填されている耐熱性絶縁容器内
の各箇所の上部をそれぞれ蓋で閉塞しているので、空気
が入りにくくなり、カーボン物質の粒子の消耗を抑制す
ることができる。
In the electric resistance type melting furnace according to the second aspect,
Since the upper portions of the respective portions in the heat-resistant insulating container filled with the particles of the carbon material are closed by the lids, it becomes difficult for air to enter and the consumption of the particles of the carbon material can be suppressed.

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

【図1】本発明に係る電気抵抗式溶融炉における実施の
形態の一例の縦断面図である。
FIG. 1 is a longitudinal sectional view of an example of an embodiment of an electric resistance melting furnace according to the present invention.

【図2】本例の電気抵抗式溶融炉で蓋を除去し側壁の一
部を破断した斜視図である。
FIG. 2 is a perspective view in which a lid is removed and a part of a side wall is cut off in the electric resistance melting furnace of the present example.

【図3】本例で用いている導電性溶融槽の平面図であ
る。
FIG. 3 is a plan view of a conductive melting tank used in this example.

【図4】本例で用いている導電性溶融槽の側面図であ
る。
FIG. 4 is a side view of a conductive melting tank used in this example.

【図5】本例で用いる導電性溶融槽の他の例を示す平面
図である。
FIG. 5 is a plan view showing another example of the conductive melting tank used in the present example.

【図6】本例で用いる導電性溶融槽の他の例を示す側面
図である。
FIG. 6 is a side view showing another example of the conductive melting tank used in the present example.

【図7】従来の電気抵抗式溶融炉の縦断面図である。FIG. 7 is a longitudinal sectional view of a conventional electric resistance melting furnace.

【符号の説明】[Explanation of symbols]

1 炉体 2a,2b,2c 電極 3 電源設備 4 被溶融物 4a 溶融スラグ 5 出湯口 6 スラグ排出口 7 被溶融物投入口 8 排気口 9 耐熱性絶縁容器 9a 底板 9b,9c 側板 10a,10b 正負の電極板 11a,11b 通電導体 12 導電性溶融槽 12a,12b 内部電極 12c 耐熱性絶縁材 13 オーバーフロー管 14a,14b カーボン物質の粒子 15a,15b 蓋 16 蓋 17 被溶融物投入筒 18 排気筒 19 隔壁 DESCRIPTION OF SYMBOLS 1 Furnace body 2a, 2b, 2c Electrode 3 Power supply equipment 4 Melted material 4a Melted slag 5 Tap hole 6 Slag discharge port 7 Melted material charging port 8 Exhaust port 9 Heat resistant insulating container 9a Bottom plate 9b, 9c Side plate 10a, 10b Positive / negative 11a, 11b Current-carrying conductor 12 Conductive melting tank 12a, 12b Internal electrode 12c Heat-resistant insulating material 13 Overflow tube 14a, 14b Particles of carbon material 15a, 15b Lid 16 Lid 17 Melting material charging cylinder 18 Exhaust cylinder 19 Partition wall

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 耐熱性絶縁容器の対向面に電極板がそれ
ぞれ配置され、前記電極板の間の前記耐熱性絶縁容器内
に導電性溶融槽が配置され、該導電性溶融槽は前記各電
極板に対向する側の部分が1対の内部電極を構成するよ
うに耐熱性絶縁材が介在されて電気的に分割され、前記
各電極板と前記導電性溶融槽との間の各空間にはカーボ
ン物質の粒子が充填されていることを特徴とする電気抵
抗式溶融炉。
1. An electrode plate is disposed on each of opposing surfaces of a heat-resistant insulating container, and a conductive melting tank is disposed in the heat-resistant insulating container between the electrode plates, and the conductive melting tank is provided on each of the electrode plates. A portion on the opposite side is electrically divided with a heat-resistant insulating material interposed therebetween so as to form a pair of internal electrodes, and a carbon material is provided in each space between each of the electrode plates and the conductive melting tank. An electric resistance type melting furnace characterized by being filled with particles.
【請求項2】 前記カーボン物質の粒子が充填されてい
る前記耐熱性絶縁容器内の各箇所の上部がそれぞれ蓋で
閉塞されていることを特徴とする請求項1記載の電気抵
抗式溶融炉。
2. The electric resistance type melting furnace according to claim 1, wherein upper portions of respective portions in the heat-resistant insulating container filled with the particles of the carbon material are closed by lids.
JP9261496A 1996-04-15 1996-04-15 Electric resistance melting furnace Expired - Lifetime JP2855265B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9261496A JP2855265B2 (en) 1996-04-15 1996-04-15 Electric resistance melting furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9261496A JP2855265B2 (en) 1996-04-15 1996-04-15 Electric resistance melting furnace

Publications (2)

Publication Number Publication Date
JPH09280750A JPH09280750A (en) 1997-10-31
JP2855265B2 true JP2855265B2 (en) 1999-02-10

Family

ID=14059323

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9261496A Expired - Lifetime JP2855265B2 (en) 1996-04-15 1996-04-15 Electric resistance melting furnace

Country Status (1)

Country Link
JP (1) JP2855265B2 (en)

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JP7253857B1 (en) * 2022-11-10 2023-04-07 有限会社 ベイテック three-phase kryptol furnace
CN119404071A (en) * 2023-03-06 2025-02-07 有限会社贝伊科技 Carbon pellet furnace and electric heating cupola system having the same

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5444001B2 (en) 2007-01-29 2014-03-19 テクノロジアン・トゥトキムスケスクス・ブイティティー Allergen-binding IgE monoclonal antibody and method for producing hypoallergenic substance
JP5525240B2 (en) 2008-11-25 2014-06-18 フィッシャー−ローズマウント システムズ,インコーポレイテッド Customized document creation method, apparatus, graphical user interface means, and machine accessible medium

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5444001B2 (en) 2007-01-29 2014-03-19 テクノロジアン・トゥトキムスケスクス・ブイティティー Allergen-binding IgE monoclonal antibody and method for producing hypoallergenic substance
JP5525240B2 (en) 2008-11-25 2014-06-18 フィッシャー−ローズマウント システムズ,インコーポレイテッド Customized document creation method, apparatus, graphical user interface means, and machine accessible medium

Also Published As

Publication number Publication date
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