JPH0526092B2 - - Google Patents
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- Publication number
- JPH0526092B2 JPH0526092B2 JP59020480A JP2048084A JPH0526092B2 JP H0526092 B2 JPH0526092 B2 JP H0526092B2 JP 59020480 A JP59020480 A JP 59020480A JP 2048084 A JP2048084 A JP 2048084A JP H0526092 B2 JPH0526092 B2 JP H0526092B2
- Authority
- JP
- Japan
- Prior art keywords
- residue
- heating furnace
- incineration residue
- molten
- heat
- 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
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- Discharge Heating (AREA)
- Gasification And Melting Of Waste (AREA)
- Processing Of Solid Wastes (AREA)
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は焼却残渣を加熱溶融する際の起動方法
に関するものである。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a starting method for heating and melting incineration residue.
一般に、家庭や事業所から捨てられるゴミはゴ
ミ焼却炉にて焼却され、焼却炉に残つた焼却残渣
は埋立用に使用されている。
Generally, garbage thrown away from homes and businesses is incinerated in a garbage incinerator, and the incineration residue left in the incinerator is used for landfill.
しかしながら都市化が進むにつれて都市ゴミの
量が増えており、また埋立についても無限に行え
るものでないことから、焼却残渣の減容化が望ま
れている。 However, as urbanization progresses, the amount of municipal waste is increasing, and landfilling cannot be done indefinitely, so it is desired to reduce the volume of incineration residue.
焼却残渣を減容化する方法として、電気炉を用
いて焼却残渣を加熱溶融した後固形化する方法が
従来より提案されている。 As a method for reducing the volume of incineration residue, a method has conventionally been proposed in which the incineration residue is heated and melted using an electric furnace and then solidified.
この方法によれば、焼却残渣は溶融状態(溶融
残渣)では導体であるので、溶融残渣が一旦生成
されれば、電極を溶融残渣に接触させて通電して
抵抗発熱することにより、その後投入される焼却
残渣を溶融残渣で加熱溶融することができ、連続
的に溶融処理できる。 According to this method, since the incineration residue is a conductor in the molten state (molten residue), once the molten residue is generated, the electrode is brought into contact with the molten residue and energized to generate resistance heat, so that it can be thrown in. The incineration residue can be heated and melted with the molten residue, and the melting process can be carried out continuously.
ところが、焼却残渣は固体の状態では不導体で
あるので、溶融残渣が今だ生成されていない起動
時には、何らかの別の方法で焼却残渣を加熱溶融
して、溶融残渣を生成する必要がある。 However, since the incineration residue is a nonconductor in a solid state, at startup when the molten residue has not yet been generated, it is necessary to heat and melt the incineration residue by some other method to generate the molten residue.
その起動方法として、従来は次のような各種の
方法があつた。 Conventionally, various methods have been used to start the system, including the following.
(a) 加熱炉に焼却残渣を投入し、電極を焼却残渣
から浮かした状態に配置する。この状態で電極
間にアーク放電を起こして、そのアーク熱で付
近の焼却残渣を溶融する。(a) Put the incineration residue into the heating furnace and place the electrodes so that they are floating above the incineration residue. In this state, an arc discharge is generated between the electrodes, and the incineration residue in the vicinity is melted by the arc heat.
(b) 加熱炉内に焼却残渣を溶融起動用の導電性材
料を添加して投入し、電極を焼却残渣に接触さ
せて導電性材料を介して通電し、抵抗発熱によ
つて焼却残渣を溶融する。(b) Add a conductive material to start melting the incineration residue and put it into the heating furnace, bring the electrode into contact with the incineration residue, and apply electricity through the conductive material to melt the incineration residue by resistance heat generation. do.
(c) 電極間隔を可変にし、起動時は加熱炉内に焼
却残渣を投入し、電極間隔を狭くして(つまり
アーク放電を起こしやすくして)、電極間にア
ーク放電を起こして、そのアーク熱で付近の焼
却残渣を溶融する。起動後は電極間隔を所定の
距離に引き離す。(c) The electrode spacing is made variable, and at startup, incineration residue is put into the heating furnace, and the electrode spacing is narrowed (in other words, making it easier to cause arc discharge), causing arc discharge between the electrodes, and the arc The heat will melt nearby incineration residue. After activation, the electrodes are separated to a predetermined distance.
(d) 加熱炉に導体成分を投入し、電極をこれに接
触させて通電して抵抗発熱し、その上に焼却残
渣を投入して導体成分の熱で焼却残渣を溶融す
る。(d) A conductor component is placed in a heating furnace, an electrode is brought into contact with the conductor component, and electricity is applied to generate resistance heat, and incineration residue is placed on top of the conductor component, and the incineration residue is melted by the heat of the conductor component.
前記(a)の方法によれば、間隔が離れている電極
間にアーク放電を起こすために高電圧が必要とな
る欠点があつた。
According to the method (a) above, there was a drawback that a high voltage was required to cause arc discharge between electrodes that were spaced apart.
前記(b)の方法によれば、焼却残渣に導電性材料
を添加しただけでは抵抗発熱のための電流路が確
実に形成されるとは限らず、確実に起動すること
はできなかつた。しかも、導体成分を抵抗発熱で
加熱するので高温が得にくく、起動に時間を要し
ていた。 According to method (b) above, simply adding a conductive material to the incineration residue does not necessarily ensure the formation of a current path for resistive heat generation, and it is not possible to start up the device reliably. Moreover, since the conductor components are heated by resistance heat generation, it is difficult to obtain high temperatures and it takes time to start up.
前記(c)の方法によれば、電極間隔を可変するた
めの駆動機構が必要となるので、構成が複雑にな
る欠点があつた。 According to the method (c), a drive mechanism is required to vary the electrode spacing, which has the disadvantage of complicating the configuration.
前記(d)の方法によれば、導体成分を抵抗発熱で
加熱するので高温が得にくく、起動に時間を要し
ていた。 According to method (d) above, since the conductor component is heated by resistance heat generation, it is difficult to obtain a high temperature and it takes time to start up.
この発明は、前記従来の技術における問題を解
決して、アーク放電を起こすために高電圧が不要
で、確実に起動でき、しかも構成が複雑になるこ
とがなく、かつ短時間で起動することができる焼
却残渣の加熱溶融の起動方法を提供しようとする
ものである。 The present invention solves the problems in the conventional technology, does not require high voltage to cause arc discharge, can be started reliably, does not have a complicated configuration, and can be started in a short time. The present invention aims to provide a method for starting the heating and melting of incineration residue.
この発明は、加熱炉に導体成分を投入し、電極
を前記導体成分に非接触の状態に配置して当該電
極と当該導体成分との間にアーク放電を起こして
そのアーク熱により前記加熱炉内を加熱し、その
後前記加熱炉内に焼却残渣を投入して前記加熱炉
内の熱でこれを加熱溶融して導電性の溶融残渣を
生成し、この溶融残渣に前記電極を接触させて通
電することによりこの溶融残渣を抵抗発熱し、こ
の抵抗発熱された溶融残渣でその後前記加熱炉内
に投入される焼却残渣を加熱溶融することを特徴
とするものである。
In the present invention, a conductor component is put into a heating furnace, an electrode is placed in a non-contact state with the conductor component, an arc discharge is caused between the electrode and the conductor component, and the arc heat causes the inside of the heating furnace. After that, the incineration residue is put into the heating furnace, and the heat in the heating furnace is used to heat and melt it to generate a conductive molten residue, and the electrode is brought into contact with the molten residue and energized. This method is characterized in that the molten residue is subjected to resistance heating, and the incineration residue that is subsequently charged into the heating furnace is heated and melted by the molten residue that has been subjected to resistance heating.
〔作用〕
この発明によれば、加熱炉に導体成分を投入
し、電極と導体成分との間にアーク放電を生じさ
せて加熱炉内を加熱して起動するので、前記(a)の
ように電極間にアーク放電を生じさせて起動する
方法に比べてアーク長を短くすることができ、こ
れによりアーク放電が起こりやすくなるので高電
圧が不要になる。[Operation] According to the present invention, a conductor component is put into the heating furnace, and an arc discharge is generated between the electrode and the conductor component to heat the inside of the heating furnace and start up. The arc length can be shortened compared to the method of starting by causing an arc discharge between electrodes, which makes arc discharge more likely to occur and eliminates the need for high voltage.
また、導体成分を焼却残渣に添加するのでなく
そのまま加熱炉に投入して電極との間でアーク放
電を生じさせて加熱するので、前記(b)のように焼
却残渣に導電性材料を添加して導電性材料を介し
て通電して抵抗発熱する方法に比べて起動を確実
に行なうことができる。 In addition, instead of adding a conductive component to the incineration residue, the incineration residue is directly put into the heating furnace and heated by generating an arc discharge between the incineration residue and the electrodes. Compared to a method that generates resistance heat by passing current through a conductive material, startup can be performed more reliably.
また、電極と導体成分との間にアーク放電を生
じさせて加熱炉内を加熱するので、前記(b)や(d)の
ように抵抗発熱で導体成分を加熱して加熱炉内を
加熱する方法に比べて高温が得られ、これにより
焼却残渣を短時間で溶融することができ、起動時
間を短縮化することができる。 Also, since arc discharge is generated between the electrode and the conductor component to heat the inside of the heating furnace, the inside of the heating furnace is heated by heating the conductor component with resistance heat generation as in (b) and (d) above. Compared to the conventional method, a high temperature can be obtained, which allows the incineration residue to be melted in a short time, and the start-up time can be shortened.
また、前記(c)の方法のようにアーク放電を生じ
やすくするために電極間隔を可変にする必要もな
いので、構成が簡単ですむ。 Furthermore, unlike the method (c) above, there is no need to vary the electrode spacing in order to facilitate arc discharge, so the configuration is simple.
以下図面により本発明の実施例について説明す
る。第1図は本発明方法の実施例を示すフローシ
ート図、第2図は具体的な工程を段階的に示す説
明図である。先ず炭素系固形物や、溶融残渣の比
重よりも小さい金属成分等の導体成分1を加熱炉
2の中に投入する。そして第2図aに示すように
導体成分1に近接するように加熱炉2に付設され
た3本の電極3A〜3Cに夫々三相の高電圧を印
加し、電極3A〜3Cと導体成分1との間にアー
ク放電を起こし、温度約4000℃のアーク熱により
加熱炉2内を加熱する。
Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 is a flow sheet diagram showing an example of the method of the present invention, and FIG. 2 is an explanatory diagram showing the specific steps step by step. First, a conductor component 1 such as a carbon-based solid material or a metal component whose specific gravity is smaller than that of the melted residue is placed in a heating furnace 2 . Then, as shown in FIG. 2a, a three-phase high voltage is applied to each of the three electrodes 3A to 3C attached to the heating furnace 2 so as to be close to the conductor component 1. An arc discharge is generated between the two, and the inside of the heating furnace 2 is heated by the arc heat at a temperature of about 4000°C.
加熱炉2内が高温状態(例えば1350℃以上)と
なつてから、第2図Bに示すようにゴミの焼却残
渣4を適当量加熱炉2内に投入し、加熱炉2内の
熱により焼却残渣4を加熱して溶融する。ここに
焼却残渣4は不導体であるが、溶融し溶融残渣と
することにより導体となる。次に第2図Cに示す
ように溶融残渣5と電極3A〜3Cとを接触させ
て電極3A〜3C間、即ち溶融残渣5を通電し、
これにより抵抗発熱させて加熱する。 After the inside of the heating furnace 2 reaches a high temperature state (for example, 1350° C. or higher), an appropriate amount of garbage incineration residue 4 is put into the heating furnace 2 as shown in FIG. Residue 4 is heated and melted. Although the incineration residue 4 is a nonconductor, it becomes a conductor by melting it to form a molten residue. Next, as shown in FIG. 2C, the molten residue 5 and the electrodes 3A to 3C are brought into contact and electricity is applied between the electrodes 3A to 3C, that is, the molten residue 5,
This causes resistance to heat up.
そして、第2図Dに示すように前記焼却残渣4
に続いて加熱炉2内に投入される焼却残渣4を、
前記抵抗発熱による熱により加熱して溶融する。
以後溶融残渣5を同様に通電して抵抗発熱させ、
その熱を利用して焼却残渣4を加熱し、このよう
にして焼却残渣4の連続投入及び連続溶融を行
う。一方溶融残渣5は、加熱炉2の取り出し口か
ら連続的に取り出されて次の工程に送られ、例え
ば水砕、空砕、空冷などの方法により冷却され固
形化される。焼却残渣4の投入については、焼却
残渣4を一旦貯蔵ピツトに貯蔵しておき、ここか
らコンベア、ホツパ、シユートを介して加熱炉2
内に投入することができる。 Then, as shown in FIG. 2D, the incineration residue 4
The incineration residue 4 that is subsequently put into the heating furnace 2 is
It is heated and melted by the heat generated by the resistance.
Thereafter, the molten residue 5 is similarly energized to generate resistance heat.
The heat is used to heat the incineration residue 4, and in this way, the incineration residue 4 is continuously charged and continuously melted. On the other hand, the molten residue 5 is continuously taken out from the outlet of the heating furnace 2 and sent to the next step, where it is cooled and solidified by methods such as water pulverization, air pulverization, and air cooling. Regarding the input of the incineration residue 4, the incineration residue 4 is temporarily stored in a storage pit, and from there it is transferred to the heating furnace 2 via a conveyor, hopper, and chute.
It can be inserted inside.
ここで導体成分1は、はじめに加熱炉2内に投
入された焼却残渣4を溶融するためのものであ
り、一旦溶融残渣5ができて抵抗発熱が行われれ
ば以後不要となる。そして導体成分1としては溶
融残渣5よりも比重の小さいものを用いることが
好ましい。 Here, the conductor component 1 is for melting the incineration residue 4 initially put into the heating furnace 2, and once the molten residue 5 is formed and resistance heating is performed, it becomes unnecessary thereafter. As the conductor component 1, it is preferable to use a material having a specific gravity smaller than that of the molten residue 5.
その理由について述べると、溶融残渣(比重約
2〜3)よりも比重の大きい金属例えば鉄屑(比
重約6.5〜6.8)を導体成分1として用いると、溶
融金属は溶融残渣5の下方に沈み炉底に溜まる。
炉底に溜まつた溶融金属は停電時に固化するが、
このとき収縮するので炉床や炉底を損うおそれが
あつて電源復帰時に運転を再開できない場合があ
り、連続運転を妨げるおそれがある。また炉底に
おける固化を避けるため溶融金属を加熱炉2から
引き抜くことも考えられるが、この場合には、レ
ードル、鋳銑機或いはインゴツト処理機等の溶融
金属処理設備が必要となり、そのための設備費が
必要になる。これに対して導体成分1として溶融
残渣5の比重よりも小さいもの、例えばブリーズ
(炭の粉)、コークス若しくは炭素電極屑等の炭素
系固形物、或いはアルミニウム等の非鉄金属を利
用すれば、導体成分1は溶融残渣5内に溶けてこ
れと共に外部に取り出される。また炭素系固形物
の場合にはその一部が大気中に飛散する。このた
め上述のような問題点がなく、格別に溶融金属処
理設備を設けなくとも連続運転を妨げられるおそ
れがない。尚、溶融残渣5は停電時に固化しても
収縮しないため炉床や炉壁を損うおそれがない。 The reason for this is that when a metal with a higher specific gravity than the molten residue (specific gravity of about 2 to 3), such as iron scrap (specific gravity of about 6.5 to 6.8), is used as the conductor component 1, the molten metal sinks below the molten residue 5. Collects at the bottom.
Molten metal that accumulates at the bottom of the furnace solidifies during a power outage, but
Since it contracts at this time, there is a risk of damaging the hearth or hearth bottom, and it may not be possible to restart operation when the power is restored, which may impede continuous operation. It is also possible to withdraw the molten metal from the heating furnace 2 in order to avoid solidification at the bottom of the furnace, but in this case, molten metal processing equipment such as a ladle, pig iron casting machine, or ingot processing machine is required, which increases the equipment cost. is required. On the other hand, if a material with a specific gravity smaller than that of the molten residue 5 is used as the conductor component 1, for example, carbon-based solids such as breeze (charcoal powder), coke or carbon electrode scraps, or non-ferrous metals such as aluminum, the conductor can be formed. Component 1 is dissolved in the melted residue 5 and taken out together with it. Furthermore, in the case of carbon-based solids, a portion of them is scattered into the atmosphere. Therefore, there are no problems such as those mentioned above, and there is no fear that continuous operation will be hindered even if no special molten metal processing equipment is provided. Incidentally, even if the melted residue 5 solidifies during a power outage, it will not shrink, so there is no risk of damaging the hearth or furnace wall.
以上のようにこの発明によれば、加熱炉に導体
成分を投入し、電極と導体成分との間にアーク放
電を生じさせて加熱炉内を加熱して起動するの
で、電極間にアーク放電を生じさせて起動する方
法に比べてアーク長を短くすることができ、これ
によりアーク放電が起こりやすくなるので高電圧
が不要になる。
As described above, according to the present invention, a conductor component is put into the heating furnace, and an arc discharge is generated between the electrode and the conductor component to heat the inside of the heating furnace and start. The arc length can be shortened compared to the method of generating and starting, which makes arc discharge more likely to occur and eliminates the need for high voltage.
また、導体成分を焼却残渣に添加するのでなく
そのまま加熱炉に投入して電極との間でアーク放
電を生じさせて加熱するので、焼却残渣に導電性
材料を添加して導電性材料を介して通電して抵抗
発熱する方法に比べて起動を確実に行なうことが
できる。 In addition, instead of adding a conductive component to the incineration residue, the incineration residue is directly placed in the heating furnace and heated by generating arc discharge between the incineration residue and the incineration residue. Startup can be performed more reliably than a method that generates heat through resistance by applying electricity.
また、電極と導体成分との間にアーク放電を生
じさせて加熱炉内を加熱するので、抵抗発熱で導
体成分を加熱して加熱炉内を加熱する方法に比べ
て高温が得られ、これにより焼却残渣を短時間で
溶融することができ、起動時間を短縮化すること
ができる。 In addition, since arc discharge is generated between the electrode and the conductor component to heat the inside of the heating furnace, a higher temperature can be obtained compared to the method of heating the inside of the heating furnace by heating the conductor component using resistance heat generation. Incineration residue can be melted in a short time, and startup time can be shortened.
また、アーク放電を生じやすくするために電極
間隔を可変にする必要もないので、構成が簡単で
すむ。 Furthermore, since there is no need to vary the electrode spacing to facilitate arc discharge, the configuration is simple.
第1図は本発明方法の実施例を示すフローシー
ト図、第2図A〜Dは具体的な工程例を段階的に
示す説明図である。
1…導体成分、2…加熱炉、3A〜3D…電
極、4…焼却残渣、5…溶融残渣。
FIG. 1 is a flow sheet diagram showing an embodiment of the method of the present invention, and FIGS. 2A to 2D are explanatory diagrams showing step-by-step concrete process examples. DESCRIPTION OF SYMBOLS 1... Conductor component, 2... Heating furnace, 3A-3D... Electrode, 4... Incineration residue, 5... Melting residue.
Claims (1)
当該電極と当該導体成分との間にアーク放電を起
こしてそのアーク熱により前記加熱炉内を加熱
し、 その後前記加熱炉内に焼却残渣を投入して前記
加熱炉内の熱でこれを加熱溶融して導電性の溶融
残渣を生成し、 この溶融残渣に前記電極を接触させて通電する
ことによりこの溶融残渣を抵抗発熱し、 この抵抗発熱された溶融残渣でその後前記加熱
炉内に投入される焼却残渣を加熱溶融することを
特徴とする焼却残渣の加熱溶融の起動方法。[Claims] 1. A conductive component is placed in a heating furnace, an electrode is placed in a non-contact state with the conductive component, an arc discharge is caused between the electrode and the conductive component, and the arc heat causes the The inside of the heating furnace is heated, and then the incineration residue is put into the heating furnace, and it is heated and melted by the heat in the heating furnace to generate a conductive molten residue, and the electrode is brought into contact with this molten residue. A method for starting heating and melting of incineration residue, characterized in that the molten residue is resistively heated by applying electricity, and the incineration residue that is subsequently charged into the heating furnace is heated and melted with the molten residue that has been generated resistance heat.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59020480A JPS60164114A (en) | 1984-02-06 | 1984-02-06 | Heating and fusing method of incinerated residue |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59020480A JPS60164114A (en) | 1984-02-06 | 1984-02-06 | Heating and fusing method of incinerated residue |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS60164114A JPS60164114A (en) | 1985-08-27 |
| JPH0526092B2 true JPH0526092B2 (en) | 1993-04-15 |
Family
ID=12028282
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP59020480A Granted JPS60164114A (en) | 1984-02-06 | 1984-02-06 | Heating and fusing method of incinerated residue |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS60164114A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4563241B2 (en) * | 2005-04-15 | 2010-10-13 | メタウォーター株式会社 | Incineration ash melting electric furnace |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6056963B2 (en) * | 1978-11-17 | 1985-12-12 | 浩 小林 | Melting treatment method and melting furnace for municipal waste incineration ash, sewage sludge, etc. |
| JPS5680613A (en) * | 1979-12-05 | 1981-07-02 | Daido Steel Co Ltd | Starting up method of waste treating arc furnace |
| JPS56146919A (en) * | 1980-04-17 | 1981-11-14 | Fuji Electric Co Ltd | Ash melting device |
| JPS5865591A (en) * | 1981-10-15 | 1983-04-19 | Power Reactor & Nuclear Fuel Dev Corp | Starting method by melting of slag used in electroslag melting |
-
1984
- 1984-02-06 JP JP59020480A patent/JPS60164114A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS60164114A (en) | 1985-08-27 |
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