JPH1182983A - Fly ash treating system - Google Patents

Fly ash treating system

Info

Publication number
JPH1182983A
JPH1182983A JP26518297A JP26518297A JPH1182983A JP H1182983 A JPH1182983 A JP H1182983A JP 26518297 A JP26518297 A JP 26518297A JP 26518297 A JP26518297 A JP 26518297A JP H1182983 A JPH1182983 A JP H1182983A
Authority
JP
Japan
Prior art keywords
fly ash
molten metal
melting furnace
holding tank
heat holding
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
JP26518297A
Other languages
Japanese (ja)
Inventor
Hatsuo Uehara
初男 上原
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.)
JFE Engineering Corp
Original Assignee
NKK Corp
Nippon Kokan Ltd
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 NKK Corp, Nippon Kokan Ltd filed Critical NKK Corp
Priority to JP26518297A priority Critical patent/JPH1182983A/en
Publication of JPH1182983A publication Critical patent/JPH1182983A/en
Pending legal-status Critical Current

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  • Gasification And Melting Of Waste (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a fly ash treating system in which treatment of fly ash is simplified by utilizing the retaining heat of a molten metal effectively and short circuit of electrode through a fused salt is prevented when an electric resistor type incineration ash melting furnace is employed. SOLUTION: A heat retaining tank 11 coupled with an incineration ash melting furnace 20 comprises a section 12 for receiving molten metal being discharged from the incineration ash melting furnace 20 into the heat retaining tank 11, and a section 15 for discharging the molten metal to the outside of the heat retaining tank 11. The heat retaining tank 11 is coupled with a pipe 13 for introducing fly ash externally and provided with a heater 16 for heating the molten metal in the heat retaining tank 11.

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】本発明は産業廃棄物を焼却し
た際に発生する飛灰を処理するための装置に関するもの
である。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for treating fly ash generated when incinerating industrial waste.

【0002】[0002]

【従来の技術】産業廃棄物を焼却炉にて焼却して排出さ
れる焼却灰には、主灰と飛灰(焼却炉で発生した排ガス
に含有されたダスト)とが含まれている。この焼却灰は
次に焼却灰溶融炉で溶融され、主灰は溶融スラグと溶融
メタルとになる。一方、飛灰はNaCl,CaCl2
どの塩を主体とした溶融塩となる。これら主灰と飛灰の
溶融物は、比重が重い順に、溶融メタル、溶融スラグ、
溶融塩となっているため、炉槽内にあってはこの順に下
から層をなす。
2. Description of the Related Art Incinerated ash discharged from incineration of industrial waste in an incinerator contains main ash and fly ash (dust contained in exhaust gas generated in the incinerator). This incineration ash is then melted in an incineration ash melting furnace, and the main ash becomes molten slag and molten metal. On the other hand, fly ash is a molten salt mainly composed of salts such as NaCl and CaCl 2 . The melts of these main ash and fly ash are in the order of specific gravity, molten metal, molten slag,
Since it is a molten salt, layers are formed from the bottom in this order in the furnace tank.

【0003】上記焼却灰の溶融には、例えば電気抵抗式
溶融炉が用いられる。電気抵抗式の溶融炉は、複数本の
電極を炉槽内に装入して溶融スラグの中に浸漬させ、溶
融スラグを介して電極間に通電させ、溶融スラグにジュ
ール熱を発生させるようになっている。
For melting the above incinerated ash, for example, an electric resistance melting furnace is used. In an electric resistance type melting furnace, a plurality of electrodes are charged into a furnace tank, immersed in the molten slag, and electricity is supplied between the electrodes through the molten slag so that Joule heat is generated in the molten slag. Has become.

【0004】[0004]

【発明が解決しようとする課題】ところが、上記溶融炉
に主灰と共に飛灰をも投入すると、飛灰が多くの溶融塩
を発生するので、炉槽内で溶融塩が溶融スラグの上に位
置して層をなすようになり、電極は、溶融スラグに浸漬
すると同時に溶融塩を貫通していることになる。溶融塩
は、溶融スラグに比べて、導電性がはるかに高い。その
ため、焼却灰溶融炉が電気抵抗式の場合には、複数本の
電極の間には、溶融スラグではなくて、溶融塩層を介し
て電気が短絡して流れてしまうことになる(溶融塩への
電力集中)。したがって、溶融スラグが所定温度まで加
熱されずに、粘性が高いものとなる結果、円滑な排出に
支障を生じることになる。これでは、円滑な溶融炉の操
業はできない。
However, if fly ash is also introduced into the above-mentioned melting furnace together with the main ash, the fly ash generates a large amount of molten salt, so that the molten salt is located above the molten slag in the furnace tank. As a result, the electrode is immersed in the molten slag and at the same time penetrates the molten salt. Molten salt has much higher conductivity than molten slag. Therefore, when the incineration ash melting furnace is of the electric resistance type, electricity is short-circuited and flows through the molten salt layer between the plurality of electrodes instead of the molten slag (molten salt). Power concentration to). Therefore, the molten slag is not heated to the predetermined temperature, but becomes high in viscosity, and as a result, smooth discharge is hindered. This does not allow smooth operation of the melting furnace.

【0005】さらには、焼却灰溶融炉で主灰と飛灰とを
混合処理するときには、炉槽への投入前に主灰と飛灰を
混合する予混合ホッパを追設したり、炉の運転の際に
は、安定化剤を投入する必要があり、装置が複雑化する
のみならずその運転も面倒である。
Further, when mixing the main ash and the fly ash in the incineration ash melting furnace, a premixing hopper for mixing the main ash and the fly ash is added before the furnace ash is introduced into the furnace tub, or the furnace is operated. In such a case, it is necessary to add a stabilizer, which not only complicates the apparatus but also complicates the operation thereof.

【0006】一方、溶融メタルは焼却灰溶融炉の炉槽底
部から抽出され、自然冷却もしくは強制冷却を受けて凝
固し、金属資源として再利用される。しかし、溶融メタ
ルの有している熱エネルギーは、何ら利用されることな
く、冷却中に放出されてしまい、エネルギーの活用とい
う点で好ましいとは言えない。
On the other hand, the molten metal is extracted from the bottom of the furnace tank of the incineration ash melting furnace, solidified by natural cooling or forced cooling, and reused as metal resources. However, the thermal energy of the molten metal is released during cooling without being used at all, which is not preferable in terms of energy utilization.

【0007】本発明は、上述の従来装置がかかえていた
問題を解決し、溶融炉の運転操作が簡単で、溶融メタル
のエネルギーを有効利用でき、溶融炉が電気抵抗式の場
合には焼却灰の溶融時の電気抵抗式溶融炉内での電極間
の短絡という事態を回避できる飛灰処理装置を提供する
ことを目的とする。
SUMMARY OF THE INVENTION The present invention solves the above-mentioned problems of the conventional apparatus, in which the operation of the melting furnace is simple, the energy of the molten metal can be effectively used, and when the melting furnace is an electric resistance type, incineration ash is used. It is an object of the present invention to provide a fly ash treatment apparatus which can avoid a short circuit between electrodes in an electric resistance type melting furnace at the time of melting.

【0008】[0008]

【課題を解決するための手段】本発明では、上記目的の
ために、焼却灰溶融炉に接続された熱保持槽を備えてい
る。該熱保持槽は上記焼却灰溶融炉から排出される溶融
メタルを該熱保持槽内へ受け入れる受入部と、該熱保持
槽外へ溶融メタルを排出する取出部とを有している。さ
らに、上記熱保持槽には、外部から該熱保持槽内へ飛灰
を導入する飛灰導入管が接続されていると共に該熱保持
槽内の溶融メタルを加熱する加熱装置が設けられてい
る。
According to the present invention, a heat holding tank connected to an incineration ash melting furnace is provided for the above purpose. The heat holding tank has a receiving part for receiving the molten metal discharged from the incineration ash melting furnace into the heat holding tank, and a discharge part for discharging the molten metal out of the heat holding tank. Furthermore, a fly ash introduction pipe for introducing fly ash from the outside into the heat holding tank is connected to the heat holding tank, and a heating device for heating the molten metal in the heat holding tank is provided. .

【0009】かかる本発明において、上記飛灰導入管は
先端が熱保持槽内の溶融メタル上面よりも下方に位置す
るように設けられており、飛灰が該飛灰導入管内で溶融
メタル内に強制的に送入されるように圧送装置に接続さ
れていることが望ましい。
In the present invention, the fly ash introduction pipe is provided such that the tip is located below the upper surface of the molten metal in the heat holding tank, and fly ash is introduced into the molten metal in the fly ash introduction pipe. It is desirable to be connected to the pumping device so as to be forcibly fed.

【0010】上述の構成に成る本発明装置においては、
焼却灰のうち主灰のみが焼却灰溶融炉に投入され、飛灰
は本発明の熱保持槽へ投入される。
In the apparatus of the present invention having the above-described configuration,
Of the incinerated ash, only the main ash is charged into the incineration ash melting furnace, and the fly ash is charged into the heat holding tank of the present invention.

【0011】主灰は焼却灰溶融炉で溶融され、炉槽内で
溶融メタル層の上に溶融スラグ層を形成する。飛灰が入
っていないため、溶融スラグ層の上に溶融塩層は形成さ
れない。したがって、この溶融炉が電気抵抗式溶融炉で
あっても、既述した電極間の短絡という不具合は生じな
い。
The main ash is melted in an incineration ash melting furnace to form a molten slag layer on the molten metal layer in the furnace tank. Since no fly ash is contained, no molten salt layer is formed on the molten slag layer. Therefore, even if the melting furnace is an electric resistance melting furnace, the above-described short circuit between the electrodes does not occur.

【0012】焼却灰溶融炉の炉槽底部に形成された溶融
メタル層は排出口から排出され、熱保持槽へもたらされ
る。該溶融メタルは熱保持槽に入ると、若干降温する
が、加熱装置により加熱され飛灰の溶融に十分な温度を
保つ。飛灰導入管から導入された飛灰は上記溶融メタル
と接触して溶融し、溶融塩層を溶融メタル層の上に形成
するようになる。溶融メタルと溶融塩は適宜時期・手法
により排出される。この熱保持槽には電極は存在しない
ので電極の短絡といった問題もないし、飛灰の溶融には
溶融メタルの熱が十分に活用される。
[0012] The molten metal layer formed at the bottom of the furnace tank of the incineration ash melting furnace is discharged from the discharge port and brought to the heat holding tank. When the molten metal enters the heat holding tank, it cools slightly, but is heated by a heating device to maintain a temperature sufficient for melting fly ash. The fly ash introduced from the fly ash introduction pipe comes into contact with the molten metal and melts, and a molten salt layer is formed on the molten metal layer. The molten metal and molten salt are discharged according to the timing and method as appropriate. Since there is no electrode in this heat holding tank, there is no problem such as a short circuit of the electrode, and the heat of the molten metal is sufficiently utilized for melting fly ash.

【0013】飛灰と溶融メタルとの接触は、飛灰が圧送
装置により溶融メタル内に強制的に送入されるときに
は、きわめて効果的なものとなる。
The contact between the fly ash and the molten metal is extremely effective when the fly ash is forcibly fed into the molten metal by a pumping device.

【0014】[0014]

【発明の実施の形態】以下、添付図面にもとづき、本発
明の実施の形態を説明する。
Embodiments of the present invention will be described below with reference to the accompanying drawings.

【0015】図1に示す本実施形態としての飛灰処理装
置10は焼却灰溶融炉20に接続されている。
The fly ash treatment apparatus 10 according to the present embodiment shown in FIG. 1 is connected to an incineration ash melting furnace 20.

【0016】焼却灰を溶融するための溶融炉20は、一
例として電気抵抗式溶融炉が示されており、炉槽21内
に複数の電極22が上方から挿入配設されている。該炉
槽21の底部には溶融メタル排出口をなす排出管23が
設けられている。
As an example of the melting furnace 20 for melting incineration ash, an electric resistance melting furnace is shown, and a plurality of electrodes 22 are inserted into a furnace tank 21 from above. A discharge pipe 23 serving as a molten metal discharge port is provided at the bottom of the furnace tank 21.

【0017】一方、飛灰処理装置10は熱保持槽11を
有している。該熱保持槽11は上記溶融炉20と同様、
耐熱材を用いて作られており、上部には溶融炉20から
排出される溶融メタルを受け入れるための受入部12が
開口の形態をなして設けられている。該受入部12には
上述した溶融炉20の溶融メタル排出口をなす排出管2
3の出口部が臨んでいる。また、熱保持槽11の上部に
は外部から飛灰を導入するための飛灰導入管13が接続
されている。該飛灰導入管13は、好ましくは図示のご
とく、下端が槽内の溶融メタルMの上面よりも下方に位
置し、かつ圧送装置(図示せず)によって飛灰が該溶融
メタルM内に強制的に送入されるようになっているのが
良い。
On the other hand, the fly ash treatment device 10 has a heat holding tank 11. The heat holding tank 11 is similar to the melting furnace 20 described above.
It is made of a heat-resistant material, and a receiving portion 12 for receiving the molten metal discharged from the melting furnace 20 is provided in the upper portion in the form of an opening. The receiving part 12 has a discharge pipe 2 serving as a molten metal discharge port of the melting furnace 20 described above.
Exit 3 is facing. Further, a fly ash introduction pipe 13 for introducing fly ash from outside is connected to an upper portion of the heat holding tank 11. As shown in the figure, the fly ash introduction pipe 13 has a lower end located below the upper surface of the molten metal M in the tank, and the fly ash is forcibly forced into the molten metal M by a pumping device (not shown). It is good that they are sent in a special way.

【0018】さらに、熱保持槽11の上部には、槽内で
の処理により発生するガスを排出する排気管14も接続
されており、また、下部には溶融メタル取出管15も設
けられている。
Further, an exhaust pipe 14 for discharging gas generated by processing in the tank is connected to an upper portion of the heat holding tank 11, and a molten metal extracting pipe 15 is provided at a lower portion. .

【0019】また、熱保持槽11の外周には、加熱装置
として誘導コイル16が巻回されている。この加熱装置
は、誘導コイルに限定されるものではなく、槽内の溶融
メタルMを昇温せしめることができれば他の加熱手段で
あっても良いことは言うまでもない。
An induction coil 16 is wound around the outer periphery of the heat holding tank 11 as a heating device. This heating device is not limited to the induction coil, and it goes without saying that other heating means may be used as long as the temperature of the molten metal M in the tank can be raised.

【0020】かかる本実施形態装置にあっては、飛灰の
溶融処理は以下の要領で行なわれる。
In this embodiment, the fly ash is melted in the following manner.

【0021】 焼却灰のうち主灰が焼却灰溶融炉20
に投入され、電極22間のジュール熱により溶融され、
下層が溶融メタル、上層が溶融スラグとなって分層され
る。その際、溶融炉20には飛灰は投入されないので、
溶融スラグ層の上には溶融塩層は存在しない。したがっ
て、従来生じていたような、溶融塩層による電極22間
の短絡という事態は生じない。
The main ash among the incinerated ash is incinerated ash melting furnace 20
And melted by Joule heat between the electrodes 22,
The lower layer is molten metal, and the upper layer is molten slag. At that time, fly ash is not injected into the melting furnace 20,
There is no molten salt layer on the molten slag layer. Therefore, a short circuit between the electrodes 22 due to the molten salt layer does not occur as conventionally occurred.

【0022】 上記溶融炉20の排出管23から溶融
メタルが排出され、熱保持槽11の受入部12から該熱
保持槽11内へ流入する。また、該熱保持槽11へは飛
灰導入管13を経て飛灰が導入される。その際、飛灰導
入管13の下端が溶融メタル層M内に入り込んでいると
きには、適宜気体により飛灰は強制的に溶融メタル層M
内へ圧送される。該溶融メタル層Mは、加熱装置として
の誘導コイル16によって、飛灰を溶融するに十分な温
度まで昇温されている。
The molten metal is discharged from the discharge pipe 23 of the melting furnace 20 and flows into the heat holding tank 11 from the receiving portion 12 of the heat holding tank 11. Fly ash is introduced into the heat holding tank 11 through a fly ash introduction pipe 13. At this time, when the lower end of the fly ash introduction pipe 13 enters into the molten metal layer M, the fly ash is forcibly forced by the gas as appropriate.
It is pumped inside. The molten metal layer M is heated to a temperature sufficient to melt fly ash by the induction coil 16 as a heating device.

【0023】 かくして、飛灰は上記溶融メタル層M
との接触によって溶融され、該溶融メタル層Mの上に溶
融塩層を形成する。溶融メタルは溶融メタル取出管15
から、そして槽内で発生したガスは排気管14から排出
される。
Thus, the fly ash is mixed with the molten metal layer M
To form a molten salt layer on the molten metal layer M. The molten metal is a molten metal extraction tube 15
And the gas generated in the tank is exhausted from the exhaust pipe 14.

【0024】本発明は、図示の実施形態に限定されるも
のではない。先ず、熱保持槽は溶融炉と別体でなくとも
よい。要は溶融炉からの溶融メタルを受け入れられるよ
うに接続されていれば良い。したがって、その接続も、
図示のごとく溶融炉に設けられた溶融メタルの排出管が
熱保持槽の受入部に臨んでいる形態でも、あるいは直接
排出管が受入部に接続されていても良い。その際、受入
時に溶融メタルの温度があまり降下しないように接続す
ることが好ましい。
The present invention is not limited to the illustrated embodiment. First, the heat holding tank need not be separate from the melting furnace. What is essential is that the connection be made so that molten metal from the melting furnace can be received. Therefore, the connection
As shown in the figure, the discharge pipe of the molten metal provided in the melting furnace may face the receiving part of the heat holding tank, or the discharge pipe may be directly connected to the receiving part. At this time, it is preferable to connect the molten metal so that the temperature of the molten metal does not drop so much at the time of receiving.

【0025】また、焼却灰溶融炉は電気抵抗式のものに
は限定されない。電気抵抗式のものであれば、溶融塩に
よる電極の短絡が回避されるという利点が得られるが、
他の形式の溶融炉であっても、飛灰溶融のための安定化
剤投入とか投入前の予混合とかが不要になり、さらに溶
融メタルの熱エネルギーの利用が図れる。
The incineration ash melting furnace is not limited to the electric resistance type. If it is of the electric resistance type, the advantage that the short circuit of the electrode due to the molten salt is avoided is obtained,
Even with other types of melting furnaces, it is not necessary to add a stabilizing agent for melting fly ash or premixing before the addition, and it is possible to use the thermal energy of the molten metal.

【0026】[0026]

【発明の効果】本発明は以上のごとく焼却灰溶融炉に接
続された熱保持槽へ溶融メタルを移し、ここで飛灰を溶
融することとしたので、溶融メタルの保有する熱を無駄
にすることなく有効に活かし、飛灰を主灰と予混合する
手間もまた安定化剤投入ということも要らず、きわめて
簡単に処理が行なえ、これに加え、焼却灰溶融炉が電気
抵抗式のときには、溶融塩による電極の短絡という不具
合も伴わないという効果をもたらす。
According to the present invention, as described above, the molten metal is transferred to the heat holding tank connected to the incineration ash melting furnace, where the fly ash is melted, so that the heat held by the molten metal is wasted. It can be used very effectively without the need for premixing the fly ash with the main ash, and without the need to add a stabilizer. There is an effect that the short-circuit of the electrode due to the molten salt is not accompanied.

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

【図1】本発明の一実施形態装置を示す概要構成図であ
る。
FIG. 1 is a schematic configuration diagram showing an apparatus according to an embodiment of the present invention.

【符号の説明】[Explanation of symbols]

10 飛灰処理装置 11 熱保持槽 12 受入部 13 飛灰導入管 15 取出部(溶融メタル取出管) 20 焼却灰溶融炉 DESCRIPTION OF SYMBOLS 10 Fly ash processing apparatus 11 Heat holding tank 12 Receiving part 13 Fly ash introduction pipe 15 Extraction part (molten metal extraction pipe) 20 Incineration ash melting furnace

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 焼却灰溶融炉に接続された熱保持槽を備
え、該熱保持槽は上記焼却灰溶融炉から排出される溶融
メタルを該熱保持槽内へ受け入れる受入部と、該熱保持
槽外へ溶融メタルを排出する取出部とを有し、さらに、
上記熱保持槽には、外部から該熱保持槽内へ飛灰を導入
する飛灰導入管が接続されていると共に該熱保持槽内の
溶融メタルを加熱する加熱装置が設けられていることを
特徴とする飛灰処理装置。
1. A heat holding tank connected to an incineration ash melting furnace, the heat holding tank receiving a molten metal discharged from the incineration ash melting furnace into the heat holding tank, and the heat holding tank. With an outlet for discharging the molten metal out of the tank,
The heat holding tank is connected to a fly ash introduction pipe for introducing fly ash from the outside into the heat holding tank, and is provided with a heating device for heating the molten metal in the heat holding tank. Characterized fly ash processing equipment.
【請求項2】 飛灰導入管は先端が熱保持槽内の溶融メ
タル上面よりも下方に位置するように設けられており、
飛灰が該飛灰導入管内で溶融メタル内に強制的に送入さ
れるように圧送装置に接続されていることとする請求項
1に記載の飛灰処理装置。
2. The fly ash introduction pipe is provided such that the tip is located below the upper surface of the molten metal in the heat holding tank,
2. The fly ash processing device according to claim 1, wherein the fly ash is connected to a pressure feeding device so that the fly ash is forcibly fed into the molten metal in the fly ash introduction pipe.
JP26518297A 1997-09-12 1997-09-12 Fly ash treating system Pending JPH1182983A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP26518297A JPH1182983A (en) 1997-09-12 1997-09-12 Fly ash treating system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP26518297A JPH1182983A (en) 1997-09-12 1997-09-12 Fly ash treating system

Publications (1)

Publication Number Publication Date
JPH1182983A true JPH1182983A (en) 1999-03-26

Family

ID=17413714

Family Applications (1)

Application Number Title Priority Date Filing Date
JP26518297A Pending JPH1182983A (en) 1997-09-12 1997-09-12 Fly ash treating system

Country Status (1)

Country Link
JP (1) JPH1182983A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100343577C (en) * 2002-07-26 2007-10-17 日精株式会社 Water outlet device for smelting furnace and fused water heater

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100343577C (en) * 2002-07-26 2007-10-17 日精株式会社 Water outlet device for smelting furnace and fused water heater

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