JPH09105507A - Operating method for ash treating electric resistance melting furnace - Google Patents

Operating method for ash treating electric resistance melting furnace

Info

Publication number
JPH09105507A
JPH09105507A JP26188495A JP26188495A JPH09105507A JP H09105507 A JPH09105507 A JP H09105507A JP 26188495 A JP26188495 A JP 26188495A JP 26188495 A JP26188495 A JP 26188495A JP H09105507 A JPH09105507 A JP H09105507A
Authority
JP
Japan
Prior art keywords
ash
molten
furnace
electric resistance
slag
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP26188495A
Other languages
Japanese (ja)
Inventor
Mutsuo Maki
睦夫 牧
Takeji Nagasato
武治 長里
Yoshifumi Hasegawa
佳史 長谷川
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.)
Nippon Steel Corp
Nippon Steel Plant Designing Corp
Original Assignee
Nittetsu Plant Designing Corp
Nippon Steel Corp
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 Nittetsu Plant Designing Corp, Nippon Steel Corp filed Critical Nittetsu Plant Designing Corp
Priority to JP26188495A priority Critical patent/JPH09105507A/en
Publication of JPH09105507A publication Critical patent/JPH09105507A/en
Pending legal-status Critical Current

Links

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  • Control Of Resistance Heating (AREA)
  • Incineration Of Waste (AREA)
  • Gasification And Melting Of Waste (AREA)

Abstract

PROBLEM TO BE SOLVED: To make it possible to conduct the optimum melting operation and to largely improve the lives of electrodes by detecting the molten slag level in a furnace and the thickness of molten salt by a molten surface level gage installed in a perpendicular direction from a furnace cover, and controlling the operation of the furnace based on the slag level. SOLUTION: The electric resistance melting furnace comprises an ash inlet 1 connected to a hopper 9 of incinerated ash or scattered ash, an exhaust port 2, a molten slag exhaust port 3, a molten salt exhaust port 12 and elevating electrodes 4. The electrodes 4 are inserted through an incinerated ash layer 5, and dipped at the ends in a molten slag layer 6. A conduction detector 14 contained in a heat resistant insulating tube 13 is vertically moved up and down by a driver 17 to measure the level of the slag and the thickness of the molten salt layer according to the change of the detected current value. The power supplying amount of a power source facility, the ash charging amount and timing of the rotary valve 15 of the hopper 9 and the elevating of the electrodes 4 by an electrode elevator 16 are controlled based on the results of the measurements.

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、焼却灰及び飛灰を
溶融する灰処理用電気抵抗溶融炉の運転方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for operating an electric resistance melting furnace for ash treatment for melting incinerated ash and fly ash.

【0002】[0002]

【従来の技術】従来、都市ごみ等の廃棄物は、焼却施設
で焼却処分され、生じた焼却灰、ばいじんは、埋立て処
分されていたが、有害重金属類の溶出による地下水汚染
等の問題から、コークス、灯油、電力等による溶融処理
方式が提案され、一部では実処理が行われている。
2. Description of the Related Art Conventionally, waste such as municipal waste has been incinerated in an incineration facility, and the incinerated ash and dust produced have been landfilled. However, due to problems such as groundwater contamination due to elution of harmful heavy metals, etc. A melting treatment method using coke, kerosene, electric power, etc. has been proposed, and some of them are actually treated.

【0003】そのなかに、ダストを主体とする灰処理の
溶融炉として、灰処理用電気抵抗溶融炉が提案されてい
る。図4は、従来の焼却灰用の3相交流電気抵抗溶融炉
の概略図、図5は直流電気抵抗溶融炉の概略図で、両図
において、灰処理用電気抵抗溶融炉は、焼却灰あるいは
飛灰等の灰投入口1、排気口2、溶融スラグ排出口3及
び電極4を備えている。電極4は、3相交流電気抵抗溶
融炉の場合、炉天井から3本の電極が焼却灰層5を貫通
して挿入され、先端は溶融スラグ層6内に浸漬してお
り、直流電気抵抗炉の場合、炉天井から1本の電極が焼
却灰層5を貫通して挿入されるとともに先端は溶融スラ
グ層6内に浸漬しており、炉底に対向電極4が設けられ
ている。溶融スラグ層6は電気の導体となり、電気抵抗
によるジュール熱で灰を溶融する。焼却灰5は溶融スラ
グ層6を被覆するように供給し、重金属、塩類等の揮散
物の量を抑制する。溶融メタル7、溶融スラグ6及び溶
融塩8は、それぞれの取出口から排出される。
Among them, an electric resistance melting furnace for ash treatment has been proposed as a melting furnace for ash treatment mainly composed of dust. FIG. 4 is a schematic diagram of a conventional three-phase alternating current electrical resistance melting furnace for incineration ash, and FIG. 5 is a schematic diagram of a direct current electrical resistance melting furnace. In both figures, the electrical resistance melting furnace for ash treatment shows incineration ash or An ash input port 1 for fly ash, an exhaust port 2, a molten slag discharge port 3 and an electrode 4 are provided. In the case of a three-phase AC electric resistance melting furnace, the electrodes 4 have three electrodes inserted from the furnace ceiling through the incineration ash layer 5 and the tips are immersed in the molten slag layer 6 to form a DC electric resistance furnace. In this case, one electrode is inserted through the incineration ash layer 5 from the furnace ceiling, the tip is immersed in the molten slag layer 6, and the counter electrode 4 is provided on the furnace bottom. The molten slag layer 6 becomes an electric conductor and melts ash by Joule heat due to electric resistance. The incineration ash 5 is supplied so as to cover the molten slag layer 6 to suppress the amount of volatile substances such as heavy metals and salts. The molten metal 7, the molten slag 6, and the molten salt 8 are discharged from their respective outlets.

【0004】[0004]

【発明が解決しようとする課題】ところが、前記従来の
灰処理用電気抵抗溶融炉では、溶融スラグ層上部に析出
されるNaCl、KCl等の塩類が表層に形成され、溶
融塩が電極を損耗したり、電極の短絡の原因となった
り、あるいは電力費が高くつくという問題がある。
However, in the conventional electric resistance melting furnace for ash treatment, salts such as NaCl and KCl deposited on the upper portion of the molten slag layer are formed on the surface layer, and the molten salt wears the electrode. There is a problem that it may cause a short circuit of the electrodes, or the power cost becomes high.

【0005】そこで、本発明は、灰処理用電気抵抗溶融
炉内の溶融塩及び溶融スラグレベルを検知して、最適か
つ安定な運転方法を提供するものである。
Therefore, the present invention provides an optimum and stable operation method by detecting the level of molten salt and molten slag in the electric resistance melting furnace for ash treatment.

【0006】[0006]

【課題を解決するための手段】本発明は、灰処理用電気
抵抗溶融炉の炉蓋に垂直方向に設置された通電検出器に
より、炉内の溶融塩及び溶融スラグレベルを検知するこ
とで、灰供給量及び電力投入量を制御して最適かつ安定
な運転を図るものである。
According to the present invention, by detecting a molten salt and a molten slag level in a furnace by an electric current detector installed vertically in a furnace lid of an electric resistance melting furnace for ash treatment, The ash supply amount and the power input amount are controlled to achieve optimum and stable operation.

【0007】[0007]

【発明の実施の形態】図1は本発明による灰処理用電気
抵抗溶融炉の断面図、図2は通電検出器の構造を示す断
面図で、電気抵抗溶融炉は、ロータリーバルブ等を有す
る、焼却灰あるいは飛灰等のホッパー9に接続された灰
投入口1、排気口2、溶融スラグ排出口3、溶融塩排出
口12及び昇降する電極4を備えている。電極4は、焼
却灰層5を貫通して挿入されるとともに先端は溶融スラ
グ層6内に浸漬しており、炉底に対向電極4が設けら
れ、両電極4は電源設備に接続されている。溶融スラグ
層6は電気の導体となり、電気抵抗によるジュール熱で
灰を溶融する。焼却灰5は溶融スラグ層6を被覆するよ
うに供給し、重金属、塩類等の揮散物の量を抑制する。
溶融メタル7、溶融スラグ6及び溶融塩8は、それぞれ
の取出口から排出される。
1 is a sectional view of an electric resistance melting furnace for ash treatment according to the present invention, and FIG. 2 is a sectional view showing a structure of an energization detector. The electric resistance melting furnace has a rotary valve and the like. It is provided with an ash inlet 1, an exhaust outlet 2, a molten slag outlet 3, a molten salt outlet 12, and an electrode 4 which moves up and down, which are connected to a hopper 9 for incinerated ash or fly ash. The electrode 4 is inserted through the incineration ash layer 5, the tip is immersed in the molten slag layer 6, the counter electrode 4 is provided on the furnace bottom, and both electrodes 4 are connected to the power supply equipment. . The molten slag layer 6 becomes an electric conductor and melts ash by Joule heat due to electric resistance. The incineration ash 5 is supplied so as to cover the molten slag layer 6 to suppress the amount of volatile substances such as heavy metals and salts.
The molten metal 7, the molten slag 6, and the molten salt 8 are discharged from their respective outlets.

【0008】図2は耐熱絶縁管13の内部に通電検出端
子14が収納された通電検出器を示す。通電検出器を駆
動装置17で上下することにより、検出される電流値の
変化により溶融スラグのレベル及び溶融塩層の厚みを計
測し、その結果に基づき、電源設備により電力投入量、
ホッパー9のロータリーバルブ15等により灰の装入量
及び装入タイミング、電極昇降装置16により電極の昇
降が制御される。
FIG. 2 shows an energization detector in which the energization detection terminal 14 is housed inside the heat resistant insulation tube 13. By moving the energization detector up and down by the driving device 17, the level of the molten slag and the thickness of the molten salt layer are measured by the change in the detected current value, and based on the result, the amount of power input by the power supply facility,
The amount and timing of ash charging are controlled by the rotary valve 15 and the like of the hopper 9, and the elevation of the electrode is controlled by the electrode elevating device 16.

【0009】本発明が適用できる灰処理用電気抵抗溶融
炉は、縦電極型の炉だけでなく横電極型の炉にも適用で
きる。
The electric resistance melting furnace for ash treatment to which the present invention can be applied can be applied not only to a vertical electrode type furnace but also to a horizontal electrode type furnace.

【0010】[0010]

【実施例】本発明の運転について説明する。EXAMPLES The operation of the present invention will be described.

【0011】ごみ投入後溶融が始まり溶融物が生成し、
溶融スラグ層、溶融メタル層が形成される。この状態で
炉蓋に設置された通電検出端子14を駆動装置17で下
降し、溶融スラグ内に浸漬して行く。通電端子が溶融ス
ラグの上部、即ち空間にある場合は、通電検出端子14
間の抵抗は無限であり、端子間を流れる電流は0とな
る。しかし、通電端子が溶融スラグに到達すると、図3
に示すように、スラグの表面に析出する溶融塩と溶融ス
ラグで電気抵抗値が異なるため、通電電流量が変化す
る。この電流値の変化と通電端子の降下距離で溶融スラ
グのレベルが検出されると共に、溶融塩層の厚みを検知
することができる。
After throwing in the waste, melting begins and a melt is produced,
A molten slag layer and a molten metal layer are formed. In this state, the energization detection terminal 14 installed on the furnace lid is lowered by the driving device 17 and immersed in the molten slag. If the energization terminal is located above the molten slag, that is, in the space, the energization detection terminal 14
The resistance between them is infinite, and the current flowing between the terminals is zero. However, when the energizing terminal reaches the molten slag,
As shown in, since the electric resistance value differs between the molten salt deposited on the surface of the slag and the molten slag, the energizing current amount changes. It is possible to detect the level of the molten slag and the thickness of the molten salt layer based on the change in the current value and the distance that the energizing terminal descends.

【0012】ちなみに、溶融塩と溶融スラグの電気抵抗
比は、溶融スラグ1に対し溶融塩は1/200〜1/3
00程度と大きく異なるため、その差を検出するには十
分である。
Incidentally, the electric resistance ratio between the molten salt and the molten slag is 1/200 to 1/3 of the molten salt with respect to the molten slag 1.
Since it is significantly different from about 00, it is sufficient to detect the difference.

【0013】本発明は、検出器により溶融スラグレベル
を把握すると共に、スラグレベルを常に一定になるよう
に灰供給量を制御する。また、灰供給量に応じた出力電
力を制御することで、最適な溶融処理が図れる。例え
ば、溶融スラグ出湯口を開閉機構とし、溶融スラグレベ
ルを検知し、出湯口を開閉動作させて溶融スラグレベル
を調整することで、安定した溶融スラグの連続排出が可
能になると共に、また、溶融スラグレベルを一定に保つ
ため灰供給量を制御すると共に、灰供給量に応じた必要
電力量を制御することも可能である。
The present invention grasps the molten slag level by the detector and controls the ash supply amount so that the slag level is always constant. Further, by controlling the output power according to the ash supply amount, optimum melting processing can be achieved. For example, the molten slag tap opening is used as an opening / closing mechanism, the molten slag level is detected, and the molten slag level is adjusted by opening / closing the tap opening to enable stable continuous discharge of molten slag, and It is possible to control the ash supply amount in order to keep the slag level constant, and it is also possible to control the required electric power amount according to the ash supply amount.

【0014】また、電極の損耗や荷電不安定の要因とな
る溶融塩が大量に溶融スラグの上に溜まった場合は、例
えば、系外から灰の供給を行なうことにより、溶融スラ
グ及び溶融塩のレベルを上昇し、炉壁に設けた専用の溶
融塩出湯口の位置に溶融塩を移動させ、溶融塩のみを強
制的に連続的に排出することが可能となる。
When a large amount of molten salt that causes wear of the electrodes and unstable charging is accumulated on the molten slag, for example, by supplying ash from outside the system, the molten slag and the molten salt are separated. It is possible to raise the level, move the molten salt to the position of the dedicated molten salt tap hole provided on the furnace wall, and forcibly and continuously discharge only the molten salt.

【0015】[0015]

【発明の効果】本発明によれば、溶融スラグレベル及び
溶融塩層の厚みを検知・把握することで灰供給量及び出
力電力量の自動制御が実現でき、最適な溶融処理運転が
可能となり、また、電極を著しく損耗する溶融塩を強制
的に排出できるため、電極の寿命を大幅に向上すること
も可能になった。
According to the present invention, the ash supply amount and the output power amount can be automatically controlled by detecting and grasping the molten slag level and the thickness of the molten salt layer, and the optimum melting treatment operation can be performed. Further, since the molten salt that significantly wears the electrode can be forcibly discharged, the life of the electrode can be significantly improved.

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

【図1】本発明による焼却灰用の電気抵抗溶融炉の断面
図。
1 is a sectional view of an electric resistance melting furnace for incineration ash according to the present invention.

【図2】通電検出器の構造を示す断面図。FIG. 2 is a cross-sectional view showing the structure of an energization detector.

【図3】炉内の溶融スラグ、溶融塩のレベルと通電検出
器による通電電流量の変化の関係を示すグラフ。
FIG. 3 is a graph showing the relationship between the levels of molten slag and molten salt in the furnace and changes in the amount of current passed by the current detector.

【図4】従来の焼却灰用の3相交流電気抵抗溶融炉の断
面図。
FIG. 4 is a cross-sectional view of a conventional three-phase AC electric resistance melting furnace for incineration ash.

【図5】従来の焼却灰用の直流電気抵抗溶融炉の断面
図。
FIG. 5 is a sectional view of a conventional DC electric resistance melting furnace for incineration ash.

【符号の説明】[Explanation of symbols]

1 灰投入口、 2 排気口、 3 溶融スラグ排出
口、 4 電極、 5 焼却灰層、 6 溶融スラグ
層、 7 溶融メタル、 8 溶融塩層、9 ホッパ
ー、 10 炉壁 11 炉壁、 12 溶融塩排出
口、 13 耐熱絶縁管、14 通電検出端子、 15
ロータリーバルブ、 16 電極昇降装置、17 駆
動装置、 18 通電検出器
1 ash input port, 2 exhaust port, 3 molten slag discharge port, 4 electrode, 5 incinerated ash layer, 6 molten slag layer, 7 molten metal, 8 molten salt layer, 9 hopper, 10 furnace wall 11 furnace wall, 12 molten salt Discharge port, 13 Heat-resistant insulating tube, 14 Energization detection terminal, 15
Rotary valve, 16 electrode lifting device, 17 driving device, 18 energization detector

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 H05B 3/00 330 H05B 3/00 330Z (72)発明者 長谷川 佳史 北九州市戸畑区大字中原46−59 日鐵プラ ント設計株式会社内─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification number Internal reference number FI Technical display location H05B 3/00 330 H05B 3/00 330Z (72) Inventor Yoshifumi Hasegawa 46, Nakahara, Tobata-ku, Kitakyushu 59 Nittetsu Plant Design Co., Ltd.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 灰処理用電気抵抗溶融炉の炉蓋から垂直
方向に設置された溶融面レベル計により、炉内の溶融ス
ラグレベル及び溶融塩の層の厚みを検知し、この溶融ス
ラグレベルに基づいて溶融炉の運転を制御することを特
徴とする灰処理用電気抵抗溶融炉の運転方法。
1. A molten surface level meter installed vertically from the furnace lid of an electric resistance melting furnace for ash treatment detects the molten slag level and the thickness of the molten salt layer in the furnace and determines the molten slag level. A method for operating an electric resistance melting furnace for ash treatment, which comprises controlling the operation of the melting furnace based on the above.
【請求項2】 溶融面レベル計の一対の端子に電圧をか
けるとともに、端子を上下動させて溶融物に浸漬させ、
溶融物の抵抗の違いによる異なる電流値から溶融物のレ
ベルと溶融塩層の厚みを検知することを特徴とする請求
項1記載の灰処理用電気抵抗溶融炉の運転方法。
2. A voltage is applied to a pair of terminals of the melt surface level meter, and the terminals are moved up and down to be immersed in the melt.
2. The method for operating an electric resistance melting furnace for ash treatment according to claim 1, wherein the level of the melt and the thickness of the molten salt layer are detected from different current values depending on the difference in the resistance of the melt.
JP26188495A 1995-10-09 1995-10-09 Operating method for ash treating electric resistance melting furnace Pending JPH09105507A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP26188495A JPH09105507A (en) 1995-10-09 1995-10-09 Operating method for ash treating electric resistance melting furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP26188495A JPH09105507A (en) 1995-10-09 1995-10-09 Operating method for ash treating electric resistance melting furnace

Publications (1)

Publication Number Publication Date
JPH09105507A true JPH09105507A (en) 1997-04-22

Family

ID=17368109

Family Applications (1)

Application Number Title Priority Date Filing Date
JP26188495A Pending JPH09105507A (en) 1995-10-09 1995-10-09 Operating method for ash treating electric resistance melting furnace

Country Status (1)

Country Link
JP (1) JPH09105507A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007292350A (en) * 2006-04-24 2007-11-08 Takuma Co Ltd Operation control method of electric melting furnace
JP2010255890A (en) * 2009-04-22 2010-11-11 Nippon Steel Engineering Co Ltd Waste melting treatment method and waste melting treatment device
WO2019092962A1 (en) * 2017-11-08 2019-05-16 謙三 高橋 Metal product manufacturing device and metal product manufacturing method

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007292350A (en) * 2006-04-24 2007-11-08 Takuma Co Ltd Operation control method of electric melting furnace
JP2010255890A (en) * 2009-04-22 2010-11-11 Nippon Steel Engineering Co Ltd Waste melting treatment method and waste melting treatment device
WO2019092962A1 (en) * 2017-11-08 2019-05-16 謙三 高橋 Metal product manufacturing device and metal product manufacturing method

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