JP3025149B2 - Method and device for detoxifying harmful substances in refuse incineration plant - Google Patents

Method and device for detoxifying harmful substances in refuse incineration plant

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Publication number
JP3025149B2
JP3025149B2 JP6117729A JP11772994A JP3025149B2 JP 3025149 B2 JP3025149 B2 JP 3025149B2 JP 6117729 A JP6117729 A JP 6117729A JP 11772994 A JP11772994 A JP 11772994A JP 3025149 B2 JP3025149 B2 JP 3025149B2
Authority
JP
Japan
Prior art keywords
fly ash
refuse
exhaust gas
harmful substances
pyrolysis
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 - Fee Related
Application number
JP6117729A
Other languages
Japanese (ja)
Other versions
JPH07323213A (en
Inventor
美智男 石田
良三 志治
澎 聶
紀之 中村
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.)
Hitachi Zosen Corp
Original Assignee
Hitachi Zosen Corp
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Filing date
Publication date
Application filed by Hitachi Zosen Corp filed Critical Hitachi Zosen Corp
Priority to JP6117729A priority Critical patent/JP3025149B2/en
Publication of JPH07323213A publication Critical patent/JPH07323213A/en
Application granted granted Critical
Publication of JP3025149B2 publication Critical patent/JP3025149B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Processing Of Solid Wastes (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は、ごみ焼却設備における
有害物の無害化方法および無害化装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method and a device for detoxifying harmful substances in a refuse incineration plant.

【0002】[0002]

【従来の技術】一般に、ごみ焼却炉から排出される燃焼
排ガスは、ボイラ、調温塔、バグフィルタおよび湿式洗
煙装置を経て、煙突から大気に放出されている。
2. Description of the Related Art In general, combustion exhaust gas discharged from a refuse incinerator is discharged to the atmosphere from a chimney via a boiler, a temperature control tower, a bag filter, and a wet smoke washing device.

【0003】そして、上記バグフィルタで捕集された飛
灰には、有害成分例えばダイオキシン類が含まれてお
り、このダイオキシン類は、熱分解装置で熱分解された
後、飛灰無害化装置を経て排出されている。
[0003] The fly ash collected by the bag filter contains harmful components such as dioxins. The dioxins are thermally decomposed by a pyrolysis device and then passed through a fly ash detoxification device. Has been discharged.

【0004】ところで、この熱分解装置は、本発明者等
が、既に提案しているものである。すなわち、この熱分
解装置は、内部にスクリュウコンベヤを有して、飛灰を
酸素不足下でかつ300℃以上の温度で30分以上保持
して、飛灰中の有害物質であるダイオキシン類を分解す
る灰加熱装置と、この灰加熱装置から排出された飛灰を
冷却する灰冷却装置と、この灰冷却装置で所定温度以下
に冷却された飛灰を蓄える灰バンカと、上記灰加熱装置
で蒸発、揮散した水銀などの低沸点重金属や未分解のダ
イオキシン類などを含む排ガスを冷却する調温塔と、こ
の調温塔で凝縮された凝縮物を溜めるドレンタンクと、
上記調温塔で凝縮しなかった排ガス中に含まれる有害物
質を吸着する活性炭フィルタとから構成したものであ
る。
By the way, this thermal decomposition apparatus has already been proposed by the present inventors. That is, this pyrolysis apparatus has a screw conveyor inside, holds fly ash under oxygen deficiency and at a temperature of 300 ° C or more for 30 minutes or more, and decomposes dioxins, which are harmful substances in fly ash. Ash heating device, an ash cooling device for cooling fly ash discharged from the ash heating device, an ash bunker for storing fly ash cooled to a predetermined temperature or less by the ash cooling device, and an ash heating device for evaporating A temperature control tower for cooling exhaust gas containing low-boiling heavy metals such as volatilized mercury and undecomposed dioxins, and a drain tank for storing condensate condensed in the temperature control tower.
An activated carbon filter for adsorbing harmful substances contained in exhaust gas not condensed in the temperature control tower.

【0005】[0005]

【発明が解決しようとする課題】ところで、上述したよ
うに、灰加熱装置でダイオキシン類を熱分解した後、調
温塔で凝縮した際に、ドレンタンク内に溜められる凝縮
物内に、ダイオキシン類が含まれていることが分かり、
したがってこのドレン水についても、無害化の処理を施
す必要が生じ、別途、高価な無害化装置を設けなければ
ならないという問題がある。
As described above, when dioxins are thermally decomposed by an ash heating device and condensed in a temperature control tower, dioxins are condensed in a drain tank. Is included,
Therefore, this drain water also needs to be subjected to detoxification treatment, and there is a problem that an expensive detoxification device must be separately provided.

【0006】そこで、本発明は上記問題を解消し得るご
み焼却設備における有害物質の無害化方法および無害化
装置を提供することを目的とする。
Accordingly, an object of the present invention is to provide a method and a device for detoxifying harmful substances in a refuse incineration plant which can solve the above-mentioned problems.

【0007】[0007]

【課題を解決するための手段】上記課題を解決するた
め、本発明のごみ焼却設備における有害物質の無害化方
法は、ごみ焼却炉から排出される排ガスに、反応助剤を
添加して有害成分と反応させ、この反応物質を飛灰とと
もに捕集装置で捕集し、この捕集された反応物質を含む
飛灰を熱分解装置により熱分解し、この熱分解により発
生する水分を、上記ごみ焼却炉の燃焼室内に供給する方
法である。
Means for Solving the Problems To solve the above problems, a method for detoxifying harmful substances in a refuse incineration plant according to the present invention comprises adding a reaction aid to exhaust gas discharged from a refuse incinerator to remove harmful components. And the reaction material is collected together with the fly ash by a collection device, the fly ash containing the collected reaction material is thermally decomposed by a pyrolysis device, and the moisture generated by the pyrolysis is removed from the refuse. This is a method of supplying into the combustion chamber of an incinerator.

【0008】また、本発明のごみ焼却設備における有害
物質の無害化装置は、ごみ焼却炉から排出される排ガス
中に反応助剤を添加する反応助剤添加装置と、反応助剤
が添加された排ガス中の反応物質を飛灰とともに捕集す
る捕集装置と、この捕集装置により捕集された反応物質
を飛灰とともに熱分解する熱分解装置と、この熱分解装
置で発生した水分を貯溜する貯溜タンクと、この貯溜タ
ンク内の水分を、ごみ焼却設備における汚水槽を介し
て、または直接に、ごみ焼却炉の燃焼室内に供給する供
給配管とから構成したごみ焼却設備における有害物質の
無害化装置である。
Further, the detoxifying apparatus for harmful substances in the refuse incineration plant of the present invention includes a reaction aid adding apparatus for adding a reaction aid to exhaust gas discharged from a refuse incinerator, and a reaction aid. A collector that collects the reactants in the exhaust gas with fly ash, a pyrolyzer that thermally decomposes the reactants collected by this collector together with fly ash, and stores the water generated by this pyrolyzer Hazardous substances in refuse incineration facilities consisting of a storage tank to be used and a supply pipe for supplying water in this storage tank to the combustion chamber of the refuse incinerator through a wastewater tank in the refuse incinerator or directly Device.

【0009】[0009]

【作用】上記有害物質の無害化方法および無害化装置に
よると、熱分解装置から発生する有害成分を含んだ水分
を、ごみ焼却炉内に再度戻すようにしているため、水分
に含まれる有害成分が熱分解により無害化される。
According to the method and apparatus for detoxifying harmful substances described above, the water containing harmful components generated from the pyrolysis device is returned to the refuse incinerator again. Is rendered harmless by thermal decomposition.

【0010】したがって、水分に含まれた有害成分を除
去するための、特別な無害化装置を設ける必要がない。
Therefore, there is no need to provide a special detoxifying device for removing harmful components contained in water.

【0011】[0011]

【実施例】以下、本発明の一実施例における有害物質の
無害化方法および無害化装置を、図1に基づき説明す
る。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS A method and a device for detoxifying harmful substances according to one embodiment of the present invention will be described below with reference to FIG.

【0012】まず、ごみ焼却設備全体の概略構成につい
て説明する。すなわち、このごみ焼却設備は、ごみピッ
ト1と、ごみ焼却炉2と、このごみ焼却炉2内にごみピ
ット1内のごみを投入するクレーン装置3と、上記ごみ
焼却炉2からボイラ部2aを経て排出される燃焼排ガス
の冷却を行う調温塔4と、この調温塔4から出た排ガス
に反応助剤[例えば、Ca(OH)2 ]を添加する反応助剤添
加装置5と、この反応助剤が添加されて生成した反応物
質を飛灰とともに捕集する捕集装置であるバグフィルタ
6と、このバグフィルタ6から出た排ガスを湿式洗浄す
る湿式洗浄装置7と、この湿式洗浄装置7から出た排ガ
スを大気に放出する煙突8と、上記ごみピット1から出
た汚水を貯溜する汚水槽9と、途中に汚水用移送ポンプ
10を有しこの汚水槽9内の汚水をごみ焼却炉2の燃焼
室内の高温域に供給する汚水供給配管11と、上記バグ
フィルタ6で捕集された反応物質を含む飛灰(以下、単
に飛灰という)を導き、この飛灰中における有害成分で
あるダイオキシン類を熱分解するためのハーゲンマイヤ
ー法による熱分解装置(従来例で説明したものと同一の
構成のもの)12と、この熱分解装置12でダイオキシ
ン類が熱分解された後の飛灰を導入してその無害化を図
る飛灰無害化装置13と、上記熱分解装置12で発生し
たドレン水(水分)を貯溜する貯溜タンク14と、途中
にドレン水用移送ポンプ15が介装されてこの貯溜タン
ク14内のドレン水を上記汚水槽9内に供給するドレン
水供給配管16とから構成されている。
First, a schematic configuration of the entire refuse incineration facility will be described. That is, this refuse incineration equipment includes a refuse pit 1, a refuse incinerator 2, a crane device 3 for putting refuse in the refuse pit 1 into the refuse incinerator 2, and a boiler unit 2a from the refuse incinerator 2. A temperature control tower 4 for cooling the combustion exhaust gas discharged through the reaction apparatus, a reaction aid addition device 5 for adding a reaction aid [for example, Ca (OH) 2 ] to the exhaust gas discharged from the temperature control tower 4, A bag filter 6 which is a collecting device for collecting a reaction substance generated by adding a reaction assistant together with fly ash, a wet cleaning device 7 for wet cleaning exhaust gas discharged from the bag filter 6, and a wet cleaning device 7 has a chimney 8 for discharging exhaust gas discharged to the atmosphere, a sewage tank 9 for storing sewage discharged from the refuse pit 1, and a transfer pump 10 for sewage in the middle of the sewage tank 9. Supply of sewage to be supplied to the high temperature area in the combustion chamber of furnace 2 A Hagen-Meier method for guiding a fly ash (hereinafter, simply referred to as fly ash) containing a reactant collected by the tube 11 and the bag filter 6 and thermally decomposing dioxins which are harmful components in the fly ash. Pyrolysis apparatus (having the same configuration as that described in the conventional example) 12 and fly ash which is detoxified by introducing fly ash after dioxins are thermally decomposed by the pyrolysis apparatus 12 , A storage tank 14 for storing drain water (moisture) generated in the pyrolysis device 12, and a drain water transfer pump 15 provided on the way to drain the drain water in the storage tank 14 into the sewage water. And a drain water supply pipe 16 to be supplied into the tank 9.

【0013】また、上記飛灰無害化装置は、飛灰を埋立
地に投棄する際に、有害な重金属(例えば、Pb,H
g,Cdなど)が溶出しないように、例えばセメント固
化法により、固化される。なお、他の無害化方法として
は、溶融法、キレート法、酸抽出法などがある。
Further, the fly ash detoxifying apparatus is capable of removing harmful heavy metals (eg, Pb, H) when dumping fly ash into a landfill.
g, Cd, etc.) are solidified by, for example, a cement solidification method. Other detoxifying methods include a melting method, a chelating method, and an acid extracting method.

【0014】次に、排ガス中における有害成分(有害物
質)であるダイオキシン類の無害化について説明する。
ごみ焼却炉2から出た排ガスは、調温塔4で冷却された
後、反応助剤が添加され、これにより生成した反応物質
が飛灰とともにバグフィルタ6により捕集される。
Next, the detoxification of dioxins, which are harmful components (harmful substances) in exhaust gas, will be described.
After the exhaust gas discharged from the refuse incinerator 2 is cooled in the temperature control tower 4, a reaction aid is added, and the generated reactant is collected by the bag filter 6 together with fly ash.

【0015】この反応物質は飛灰とともに熱分解装置1
2に送られ、ここで所定温度で所定時間保持されて、有
害成分であるダイオキシン類が熱分解される。そして、
この熱分解装置12で発生した水分、すなわち灰加熱装
置から排出された排ガスの冷却による凝縮時に発生した
水分が、ドレン水として貯溜タンク14に貯溜される。
このドレン水には、微量ではあるが、ダイオキシン類が
含まれている。
This reactant is combined with fly ash in the thermal decomposition unit 1
2, where it is held at a predetermined temperature for a predetermined time to thermally decompose harmful dioxins. And
The water generated in the thermal decomposition device 12, that is, the water generated when the exhaust gas discharged from the ash heating device is condensed by cooling is stored in the storage tank 14 as drain water.
This drain water contains a small amount of dioxins.

【0016】このダイオキシン類を含んだドレン水は、
ドレン水供給配管16を介して、汚水槽9に供給され
る。そして、この汚水槽9内に供給されたドレン水は汚
水とともに、汚水供給配管11を介して、ごみ焼却炉2
の燃焼室内の高温域に噴霧されて加熱される。すなわ
ち、ダイオキシン類は、ごみ焼却炉2内で熱分解されて
無害化される。
The drain water containing dioxins is
The water is supplied to the sewage tank 9 via a drain water supply pipe 16. The drain water supplied into the sewage tank 9 together with the sewage is supplied to the refuse incinerator 2 via the sewage supply pipe 11.
Is sprayed and heated in a high temperature region in the combustion chamber. That is, dioxins are decomposed by being thermally decomposed in the refuse incinerator 2.

【0017】このように、ダイオキシン類を熱分解する
熱分解装置12で発生するとともに微量のダイオキシン
類含むドレン水を、汚水槽9に供給して、この汚水と一
緒に、ごみ焼却炉2の燃焼室内に噴霧供給して熱分解す
るようにしたので、別途、ダイオキシン類の無害化装置
を設ける必要がないため、ダイオキシン類を含むドレン
水の無害化を、非常に低コストで行うことができるとと
もに、ランニングコストも殆ど不要にし得る。
As described above, the drainage water generated in the pyrolysis apparatus 12 for pyrolyzing dioxins and containing a small amount of dioxins is supplied to the sewage tank 9 and the wastewater is burned in the refuse incinerator 2 together with the sewage. Since it is made to spray and supply indoors and thermally decompose, there is no need to separately provide a detoxification device for dioxins, so that detoxification of drain water containing dioxins can be performed at very low cost. Also, the running cost can be almost eliminated.

【0018】ところで、上記実施例においては、熱分解
装置12から排出されるドレン水を、一旦、汚水槽9に
供給した後、ごみ焼却炉2に供給するようにしたが、例
えば図1の波線にて示すように、ドレン水供給配管16
を、直接、ごみ焼却炉2に接続して、燃焼室内の高温域
に噴霧させるようにしてもよい。
By the way, in the above embodiment, the drain water discharged from the thermal decomposition unit 12 is once supplied to the sewage tank 9 and then supplied to the refuse incinerator 2. , The drain water supply pipe 16
May be directly connected to the refuse incinerator 2 and sprayed on a high temperature region in the combustion chamber.

【0019】この場合、汚水槽9側の汚水供給系統、す
なわち汚水供給配管11に何らかのトラブル(例えば、
汚水用移送ポンプ10が故障した場合)が発生した場合
に、支障なく、ドレン水の無害化処理を図ることができ
る。
In this case, the sewage supply system on the sewage tank 9 side, that is, the sewage supply pipe 11 has some trouble (for example,
When the sewage transfer pump 10 fails, the drain water can be detoxified without any trouble.

【0020】なお、上述した有害物質の無害化方法は、
熱分解装置12から排出されるドレン水の他に、同じご
み焼却設備内で発生するとともにダイオキシン類を含む
ドレン水の無害化にも適用し得る。
The above harmless substance detoxifying method is as follows.
In addition to the drain water discharged from the thermal decomposition device 12, the present invention can be applied to detoxification of drain water generated in the same refuse incineration equipment and containing dioxins.

【0021】[0021]

【発明の効果】以上のように本発明の有害物質の無害化
方法および無害化装置によると、熱分解装置から発生す
るダイオキシン類などの有害成分を含んだ水分を、ごみ
焼却炉の燃焼室内に供給するようにしたので、水分に含
まれ有害物質が熱分解により無害化され、したがって特
別な無害化装置を設けなくても、有害物質の無害化を図
ることができる。すなわち、有害成分の無害化を、非常
に低コストで、かつランニングコストが殆ど要らずに行
うことができる。
As described above, according to the harmless substance detoxification method and detoxification apparatus of the present invention, water containing harmful components such as dioxins generated from a pyrolysis device is introduced into a combustion chamber of a refuse incinerator. Since the supply is performed, the harmful substances contained in the moisture are detoxified by thermal decomposition. Therefore, the harmful substances can be detoxified without providing a special detoxification device. That is, detoxification of the harmful component can be performed at a very low cost and with almost no running cost.

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

【図1】本発明の一実施例におけるごみ焼却設備の概略
全体構成を示すブロック図である。
FIG. 1 is a block diagram showing a schematic overall configuration of a refuse incineration plant according to an embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1 ごみ焼却炉 5 反応助剤添加装置 6 バグフィルタ 9 汚水槽 10 汚水用移送ポンプ 11 汚水供給配管 12 熱分解装置 13 飛灰無害化装置 14 貯溜タンク 15 ドレン水用移送ポンプ 16 ドレン水供給配管 Reference Signs List 1 refuse incinerator 5 reaction aid addition device 6 bag filter 9 sewage tank 10 sewage transfer pump 11 sewage supply pipe 12 thermal decomposition device 13 fly ash detoxification device 14 storage tank 15 drain water transfer pump 16 drain water supply pipe

───────────────────────────────────────────────────── フロントページの続き (72)発明者 中村 紀之 大阪府大阪市此花区西九条5丁目3番28 号 日立造船株式会社内 (56)参考文献 特開 平5−146772(JP,A) 特開 平5−33914(JP,A) 特開 平5−23540(JP,A) (58)調査した分野(Int.Cl.7,DB名) B01D 53/34 - 53/88 B09B 3/00 ──────────────────────────────────────────────────続 き Continuation of the front page (72) Inventor Noriyuki Nakamura 5-3-28 Nishikujo, Konohana-ku, Osaka-shi, Hitachi Zosen Corporation (56) Reference JP-A-5-146772 (JP, A) JP-A-5-33914 (JP, A) JP-A-5-23540 (JP, A) (58) Fields investigated (Int. Cl. 7 , DB name) B01D 53/34-53/88 B09B 3/00

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】ごみ焼却炉から排出される排ガスに、反応
助剤を添加して有害成分と反応させ、この反応物質を飛
灰とともに捕集装置で捕集し、この捕集された反応物質
を含む飛灰を熱分解装置により熱分解し、この熱分解に
より発生する水分を、上記ごみ焼却炉の燃焼室内に供給
することを特徴とするごみ焼却設備における有害物質の
無害化方法。
1. An exhaust gas discharged from a refuse incinerator is added with a reaction aid to react with harmful components, and this reactant is collected together with fly ash by a collector, and the collected reactant is collected. A method for detoxifying harmful substances in a refuse incineration plant, comprising thermally decomposing fly ash containing water by a pyrolysis apparatus and supplying water generated by the pyrolysis to the combustion chamber of the refuse incinerator.
【請求項2】ごみ焼却炉から排出される排ガス中に反応
助剤を添加する反応助剤添加装置と、反応助剤が添加さ
れた排ガス中の反応物質を飛灰とともに捕集する捕集装
置と、この捕集装置により捕集された反応物質を飛灰と
ともに熱分解する熱分解装置と、この熱分解装置で発生
した水分を貯溜する貯溜タンクと、この貯溜タンク内の
水分を、ごみ焼却設備における汚水槽を介して、または
直接に、ごみ焼却炉の燃焼室内に供給する供給配管とか
ら構成したことを特徴とするごみ焼却設備における有害
物質の無害化装置。
2. A reaction assistant addition device for adding a reaction assistant to exhaust gas discharged from a refuse incinerator, and a collection device for collecting a reaction substance in the exhaust gas to which the reaction assistant has been added together with fly ash. And a pyrolysis device that pyrolyzes the reactants collected by the collection device together with fly ash, a storage tank that stores the water generated by the pyrolysis device, and incinerates the water in the storage tank. A detoxifying apparatus for harmful substances in refuse incineration facilities, comprising a supply pipe for supplying directly into a combustion chamber of a refuse incinerator through a sewage tank in the facility or directly.
JP6117729A 1994-05-31 1994-05-31 Method and device for detoxifying harmful substances in refuse incineration plant Expired - Fee Related JP3025149B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6117729A JP3025149B2 (en) 1994-05-31 1994-05-31 Method and device for detoxifying harmful substances in refuse incineration plant

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6117729A JP3025149B2 (en) 1994-05-31 1994-05-31 Method and device for detoxifying harmful substances in refuse incineration plant

Publications (2)

Publication Number Publication Date
JPH07323213A JPH07323213A (en) 1995-12-12
JP3025149B2 true JP3025149B2 (en) 2000-03-27

Family

ID=14718845

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6117729A Expired - Fee Related JP3025149B2 (en) 1994-05-31 1994-05-31 Method and device for detoxifying harmful substances in refuse incineration plant

Country Status (1)

Country Link
JP (1) JP3025149B2 (en)

Also Published As

Publication number Publication date
JPH07323213A (en) 1995-12-12

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