JP2004255329A - Apparatus for treating exhaust gas - Google Patents

Apparatus for treating exhaust gas Download PDF

Info

Publication number
JP2004255329A
JP2004255329A JP2003050657A JP2003050657A JP2004255329A JP 2004255329 A JP2004255329 A JP 2004255329A JP 2003050657 A JP2003050657 A JP 2003050657A JP 2003050657 A JP2003050657 A JP 2003050657A JP 2004255329 A JP2004255329 A JP 2004255329A
Authority
JP
Japan
Prior art keywords
ash
exhaust gas
dust collector
melting furnace
incinerator
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.)
Granted
Application number
JP2003050657A
Other languages
Japanese (ja)
Other versions
JP4361296B2 (en
Inventor
Mitsuo Imamura
三夫 今村
Shuhei Ishii
修平 石井
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.)
Mitsubishi Power Ltd
Original Assignee
Babcock Hitachi 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 Babcock Hitachi KK filed Critical Babcock Hitachi KK
Priority to JP2003050657A priority Critical patent/JP4361296B2/en
Publication of JP2004255329A publication Critical patent/JP2004255329A/en
Application granted granted Critical
Publication of JP4361296B2 publication Critical patent/JP4361296B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Abstract

<P>PROBLEM TO BE SOLVED: To provide an apparatus for treating exhaust gas which can reduce the amount of chemicals for removing harmful components in the exhaust gas, the amount of cement and chemicals for solidifying collected ashes and the amount of final materials of solidified ashes. <P>SOLUTION: The apparatus for treating the exhaust gas is provided with a dust filtering collector for an incinerator removing dust in the exhaust gas in an incinerator, an ash melting furnace melting the ash incinerated in the incinerator and the ash collected by the dust filtering collector for the incinerator, and a dust filtering collector for the ash melting furnace removing dust in the exhaust gas in the ash melting furnace. The apparatus for treating the exhaust gas is installed with a dust filtering collector for removing dust and a dust filtering collector for removing harmful gases in this order as the dust filtering collectors for the incinerator, and installed with a means for supplying, to the ash melting furnace, the ash collected in the dust filtering collector for removing dust and a means for making a melting furnace treated gas from the dust filtering collector for the ash melting furnace join the incinerator exhaust gas of upstream of the dust filtering collector for removing the harmful gases, and a means for supplying chemicals to the joined exhaust gases for removing the harmful gases. <P>COPYRIGHT: (C)2004,JPO&NCIPI

Description

【0001】
【発明の属する技術分野】
本発明は排ガス処理装置に係り、特に灰溶融炉を併設した廃棄物焼却設備に好適な排ガス処理装置に関する。
【0002】
【従来の技術】
近年、廃棄物処理に関し、生活環境を守るための再利用(リサイクル)が社会的な要求として高まっている。また再利用できない廃棄物については、埋立処分場の逼迫から、焼却できるものはできるだけ焼却処理することにより埋立処分場の延命化が図られている。さらに焼却施設においては、煙突から排出される有害物質の軽減および焼却灰の無害化再利用の要求が高まっている。
焼却灰の無害化再利用としては、焼却灰を溶融処理して有害物質の溶出を抑え、溶融スラグとして取出し、路盤材などに再利用する方法が採用されている(例えば、特許文献1等)。
【0003】
図5は、従来技術の排ガス処理装置の系統図である。
この排ガス処理装置は、焼却炉1からの焼却炉排ガス中のばい塵を除去する焼却炉用ろ過集塵器21と、前記焼却炉1の焼却灰14および該焼却炉用ろ過集塵器21で捕集した捕集灰22を溶融する灰溶融炉8と、該灰溶融炉8からの溶融炉排ガス中のばい塵を除去する灰溶融炉用ろ過集塵器10と、前記焼却炉用ろ過集塵器21および灰溶融炉用ろ過集塵器10のそれぞれの前流の排ガスに該排ガス中の有害成分を除去するための薬剤を供給する薬剤供給管7とを主として備える。
【0004】
このような構成において、廃棄物が焼却炉1に供給されて焼却され、このときに生じる焼却炉排ガスは、ガス冷却装置2を経て焼却炉用ろ過集塵器21に供給される。焼却炉用ろ過集塵器21では、焼却炉排ガス中のばい塵と固体化した有害成分が捕集されて除去される。また焼却炉排ガスには硫黄酸化物や塩化水素などの有害ガスが含まれるため、通常、消石灰などの薬剤が薬剤供給管7から焼却炉用ろ過集塵器21の前流の焼却炉排ガスに供給され、焼却炉排ガス中の有害成分を薬剤と反応させて固体化し、上記ばい塵とともに集塵灰22として捕集される。ばい塵および反応物が除去された処理ガスは誘引通風機5を介して煙突6から系外に排出される。
【0005】
一方、焼却炉用ろ過集塵器21で捕集された捕集灰22は、前記焼却炉1の焼却灰14とともに灰溶融炉8に供給されて溶融され、溶融物は溶融スラグ20として系外に排出される。上記焼却灰14および捕集灰22は、その成分にもよるが、ほぼ1300〜1400℃の高温で灰溶融炉8で溶融されるため、焼却灰等に吸着した前記有害成分は、溶融スラグ20中に含有される形態ではなく、灰溶融炉8から排出する溶融炉排ガス中に同伴される。そのため、ガス冷却装置9を経てた後の溶融炉排ガスには、上記焼却炉排ガスと同様に、灰溶融炉用ろ過集塵器10に導入する前に薬剤供給管7から薬剤が投入されて有害ガスの固体化が行われ、溶融炉処理ガス13がファン11により焼却炉用ろ過集塵器21後流の焼却炉処理ガスと合流されて系外に排出される。灰溶融炉用ろ過集塵器10で捕集された捕集灰は、灰溶融炉8に再度供給すると次第に溶融炉排ガス中の有害ガス濃度が濃くなるため、灰溶融炉8には供給せずに灰固化装置18に供給してセメント・薬剤19により固化し、最終処理物として排出される。
【0006】
上記排ガス処理装置では、焼却炉排ガスおよび溶融炉排ガスに含まれる硫黄酸化物や塩化水素ガスなどの有害ガスは、それぞれ消石灰粉末などの反応薬剤と反応させて有害成分を固体化し、焼却炉用ろ過集塵器21および灰溶融炉用ろ過集塵器10で捕集されて除去される。この固体化反応は、固体状の薬剤とガス状の成分とのいわゆる固気反応であり、当量比の薬剤量を供給しただけでは反応が充分に行われないため、一般には当量比の1.5倍から3倍の薬剤量が投入される。投入された未反応の薬剤は、灰溶融炉用ろ過集塵器10で捕集灰17として捕集されるため、捕集灰17の量が増大し、それに伴い、固化処理に必要なセメント・薬剤量が増大し、最終固化処理費用が嵩むという問題があった。また未反応薬剤を再利用ができずに無駄になるという問題があった。さらに焼却炉排ガスおよび溶融炉排ガスに別々に薬剤が投入されるため、薬剤の投入量の調節が容易でなく、投入する薬剤量の低減を図ることが困難であった。
【0007】
【特許文献1】
特開平9−173742号公報
【0008】
【発明が解決しようとする課題】
本発明の課題は、上記従来技術の問題点を解決し、排ガス中の有害成分の除去に使用する薬剤量、捕集灰を固化処理するためのセメント・薬剤量、および最終灰固化物量を低減させることができる排ガス処理装置を提供するにある。
【0009】
【課題を解決するための手段】
本発明者らは、上記課題について鋭意検討した結果、焼却炉用ろ過式集塵器を2段に設置し、前段のばい塵除去用ろ過集塵器で捕集した捕集灰を灰溶融炉に供給して溶融させ、溶融炉排ガス中のばい塵を除去した処理ガスを、前段と後段のろ過集塵器の間の焼却炉排ガスに合流させ、該合流排ガス中に有害成分を除去するための薬剤を投入するようにすることにより、また後段の有害ガス除去用ろ過集塵器で捕集した捕集灰を灰溶融炉用ろ過集塵器の前流の溶融炉排ガスに混合させるようにすることにより、上記課題を達成できることを見いだし、本発明に到達したものである。
上記課題を達成するために本願で特許請求される発明は以下の通りである。
【0010】
(1)焼却炉の排ガス中のばい塵を除去する焼却炉用ろ過集塵器と、前記焼却炉の焼却灰および該焼却炉用ろ過集塵器で捕集した捕集灰を溶融する灰溶融炉と、該灰溶融炉の排ガス中のばい塵を除去する灰溶融炉用ろ過集塵器とを備えた排ガス処理装置において、前記焼却炉用ろ過集塵器として、ばい塵除去用ろ過集塵器と有害ガス除去用ろ過集塵器を順に設置し、該ばい塵除去用ろ過集塵器で捕集した捕集灰を前記灰溶融炉に供給する手段および該有害ガス除去用ろ過集塵器前流の焼却炉排ガスに前記灰溶融炉用ろ過集塵器からの溶融炉処理ガスを合流させる手段を設けるとともに、該有害ガス除去用ろ過集塵器前流の前記合流排ガスに有害ガスを除去するための薬剤を投入する手段を設けたことを特徴とする排ガス処理装置。
(2)前記有害ガス除去用ろ過集塵器で捕集した捕集灰の全部または一部を、前記灰溶融炉用ろ過集塵器前流の溶融炉排ガスに混合させる手段を設けたことを特徴とする請求項1に記載の排ガス処理装置。
【0011】
(3)焼却炉の排ガス中のばい塵を除去する焼却炉用ろ過集塵器と、前記焼却炉の焼却灰および該焼却炉用ろ過集塵器で捕集した捕集灰を溶融する灰溶融炉と、該灰溶融炉の溶融炉排ガス中のばい塵を除去する灰溶融炉用ろ過集塵器とを備えた排ガス処理装置において、前記焼却炉用ろ過集塵器として、ばい塵除去用ろ過集塵器と有害ガス除去用ろ過集塵器を順に設置し、該ばい塵除去用ろ過集塵器で捕集した捕集灰を前記灰溶融炉に供給する手段および該有害ガス除去用ろ過集塵器で捕集した捕集灰を前記灰溶融炉用ろ過集塵器前流の溶融炉排ガスに混合させる手段とを設けるとともに、該有害ガス除去用ろ過集塵器前流の焼却炉排ガスに有害ガスを除去するための薬剤を投入する手段を設けたことを特徴とする排ガス処理装置。
【0012】
【作用】
本発明において、後述する図1に示すように、焼却炉用ろ過式集塵器として、ばい塵除去用ろ過集塵器3と有害ガス除去用ろ過集塵器4をダクト12を介して順に設置し、ばい塵除去用ろ過集塵器3で捕集した捕集灰15を灰溶融炉8に供給して溶融させ、かつ溶融炉排ガス中のばい塵を灰溶融炉用ろ過集塵器10で除去し、溶融炉処理ガス13を前記ダクト12の焼却炉排ガスに合流させるとともに、該ダクト12に接続する薬剤供給管7から薬剤を投入して該合流排ガス中の有害成分を除去するようにすることにより、薬剤の投入を1か所で行うことができ、薬剤投入量の調節が容易となり、ひいては薬剤量の低減、灰溶融炉用ろ過集塵器10で捕集される捕集灰17の低減、該捕集灰17の固化処理に必要なセメント・薬剤19の低減および最終固化物の低減が可能となる。
【0013】
また後述する図2ないし図4に示すように、有害ガス除去用ろ過集塵器4で捕集した捕集灰16の全部または一部を、灰溶融炉用ろ過集塵器10の前流の溶融炉排ガスに混合させるよにすることにより、捕集灰16に含まれる未反応薬剤を溶融炉排ガス中の有害ガスと反応させることができ、投入薬剤の有効利用が可能となる。すなわち、有害ガスを除去するための反応薬剤が当量比の1.5倍から3倍の量で吹き込まれるため、当量比で0.5倍から1.5倍の未反応薬剤が捕集灰16として捕集されることになるが、このような未反応薬剤を含む捕集灰16を灰溶融炉用ろ過集塵器前流の溶融炉排ガスに吹込むようにすることにより、捕集灰16中の未反応薬剤を溶融炉排ガス中の有害ガスと反応させることができ、投入薬剤の有効利用が可能となる。また有害ガスを除去するための薬剤量が少なくなるため、焼却炉用ろ過集塵器4または灰溶融炉用ろ過集塵器10で捕集される捕集灰16、17の量が少なくなり、捕集灰16、17を固化処理するためのセメント・薬剤19の供給量も少なくてよく、最終的な固化物量も少なくなる。さらに溶融炉排ガス中の硫黄酸化物や塩化水素ガスなどの腐食性ガスが除去された溶融炉処理ガス13を焼却炉用ろ過集塵器4の前流または後流に合流させるため、これらを導くためのダクト等の腐食性ガスによる腐食が防止される。
【0014】
【発明の実施の形態】
以下、本発明を図面により詳しく説明するが、本発明はこれらに限定されるものではない。
図1は、本発明の一実施例を示す排ガス処理装置の系統図である。
図1において、図5と異なる点は、焼却炉用ろ過集塵器21の代わりに、ばい塵除去用ろ過集塵器3と有害ガス除去用ろ過集塵器4を順にダクト12を介して連設し、かつばい塵除去用ろ過集塵器3で捕集した捕集灰15をダクトを介して灰溶融炉8に供給し、また灰溶融炉用ろ過集塵器10からの溶融炉処理ガス13をダクトを介して有害ガス除去用ろ過集塵器4の前流のダクト12の焼却炉排ガスに合流させ、さらに薬剤供給管7から投入する薬剤を、ダクト12の合流排ガスに供給するようにし、さらに該有害ガス除去用ろ過集塵器4で捕集された捕集灰16を灰固化装置8に供給するようにした点である。
このような排ガス処理装置によれば、薬剤の投入を1か所で行うことができ、薬剤投入量の調節が容易となるため、薬剤量の低減、灰溶融炉用ろ過集塵器10で捕集される捕集灰17の低減、該捕集灰17の固化処理に必要なセメント・薬剤19の低減および最終固化物の低減が可能となる。
【0015】
図2は、本発明の他の一実施例を示す排ガス処理装置の系統図である。
図2において、図1と異なる点は、有害ガス除去用ろ過集塵器4からの捕集灰16をダクトを介して灰溶融炉用ろ過集塵器10の前流の溶融炉排ガスに合流させるようにした点である。
このような構成とすることにより、上記効果に加え、捕集灰16に含まれる未反応薬剤を溶融炉排ガスと反応させることができ、投入薬剤の有効利用および投入薬剤量の低減が可能となるため、さらなる捕集灰17の低減、固化処理するためのセメント・薬剤19の供給量の低減、および最終固化物の低減が可能となる。さらに有害ガスが除去された溶融炉処理ガス13を焼却炉用ろ過集塵器4の前流に合流させるため、合流させるためのダクト等の有害ガス(腐食性ガス)による腐食を防ぐことができる。
【0016】
上記装置において、焼却炉排ガス中の有害ガスの挙動を調査したところ、ばい塵除去用ろ過集塵器3の捕集灰15には約10%の有害ガスが吸着し、残りの約90%の有害ガスが、ばい塵除去用ろ過集塵器3を通過して有害ガス除去用ろ過式集塵器4に導入されることが明らかとなった。また有害ガスに反応させる薬剤として高反応消石灰を用い、有害ガスとの当量比で約1.5倍量の薬剤を薬剤供給管7から吹込むことで、有害ガス除去用ろ過集塵器4の出口ガス中の有害ガス濃度が、要求値を満足することが測定の結果明らかとなった。これらの結果から、薬剤供給管7から投入した薬剤のうち約1/3が未反応分として捕集灰16に含まれることになり、該捕集灰16を灰溶融炉用ろ過式集塵器10の前流の溶融炉排ガス(上記の約10%の有害ガスを含む)に吹込むことで該未反応薬剤を有効に活用できることになる。本装置を用いた試験でも、有害ガス除去用ろ過集塵器4の前流の焼却炉排ガス中の有害ガス量が約90%に低下し、これに比例して、有害ガス除去用薬剤の投入量、捕集灰固化用のセメント・薬剤の使用量および最終的な固化物の量を約10%低減することができた。
【0017】
図3は本発明のさらに他の一実施例を示す排ガス処理装置の系統図である。
図3において、図2と異なる点は、有害ガス除去用ろ過集塵器4からの捕集灰16の一部、例えば、余裕炉排ガス中の有害ガス成分を除去するために必要な量の捕集灰16を灰溶融炉用ろ過集塵器10の前流の溶融炉排ガスに合流させ、残りの捕集灰16は灰固化装置18に供給するようにした点である。
このような構成とすることにより、上記効果に加え、溶融炉排ガスに含まれる有害ガス量に応じて捕集灰16の量を調節することができるため、灰溶融炉用ろ過集塵器10の処理効率を向上させることができる。
【0018】
図4は本発明のさらに他の実施例を示す排ガス処理装置の系統図である。
図4において、図2と異なる点は、灰溶融炉用ろ過集塵器10で処理された溶融炉処理ガス13を有害ガス除去用ろ過集塵器4の後流の処理ガスに合流させるようにした点である。このような構成とすることにより、有害ガス除去用ろ過集塵器4の処理効率を向上させることができる。
【0019】
【発明の効果】
請求項1に係る発明によれば、焼却炉用ろ過集塵器を2段に設置し、溶融炉排ガスの処理ガスをばい塵が除去された焼却炉排ガスに合流させ、この合流排ガスに有害ガス除去薬剤の投入することにより、該薬剤の投入量の調節が容易となり、該薬剤量の低減、捕集灰の低減、捕集灰を固化するためのセメント・薬剤量の低減、最終固化物量の低減が可能であり、従って、埋立処分場などの延命化が可能となる。
請求項2または3に係る発明によれば、上記効果に加え、有害ガスを除去するための未反応薬剤の有効利用が可能となり、さらなる有害ガス除去用薬剤等の低減が可能となる。
【図面の簡単な説明】
【図1】本発明の一実施例を示す排ガス処理装置の系統図。
【図2】本発明の他の実施例を示す排ガス処理装置の系統図。
【図3】本発明のさらに他の実施例を示す排ガス処理装置の系統図。
【図4】本発明のさらに他の実施例を示す排ガス処理装置の系統図。
【図5】従来技術の排ガス処理装置の系統図。
【符号の説明】
1…焼却炉、2…ガス冷却装置、3…ばい塵除去用ろ過集塵器、4…有害ガス除去用ろ過集塵器、5…誘引通風機、6…煙突、7…薬剤供給管、8…灰溶融炉、9…ガス冷却装置、10…灰溶融炉用ろ過集塵器、11…ファン、12…ダクト、13…溶融炉排ガス、14…焼却灰、15、16、17…捕集灰、18…灰固化装置、19…セメント・薬剤、20…溶融スラグ、21…焼却路用ろ過集塵器、22…捕集灰。
[0001]
TECHNICAL FIELD OF THE INVENTION
The present invention relates to an exhaust gas treatment device, and more particularly to an exhaust gas treatment device suitable for a waste incineration facility provided with an ash melting furnace.
[0002]
[Prior art]
2. Description of the Related Art In recent years, regarding waste disposal, reuse (recycling) for protecting a living environment has been increasing as a social demand. Due to the tightness of landfill sites, waste that cannot be reused is incinerated as much as possible to extend the life of the landfill site. Furthermore, in incineration facilities, there is an increasing demand for reducing harmful substances emitted from chimneys and detoxifying and recycling incinerated ash.
As a method for detoxifying and recycling incinerated ash, a method is employed in which incinerated ash is melted to suppress elution of harmful substances, taken out as molten slag, and reused as roadbed material (for example, Patent Document 1). .
[0003]
FIG. 5 is a system diagram of a conventional exhaust gas treatment apparatus.
This exhaust gas treatment device comprises an incinerator filter dust collector 21 for removing dust in incinerator exhaust gas from the incinerator 1, an incinerator ash 14 of the incinerator 1, and a filter dust collector 21 for the incinerator. An ash melting furnace 8 for melting the collected ash 22 collected, a ash melting furnace filter / dust collector 10 for removing dust in the smelting furnace exhaust gas from the ash melting furnace 8, and an incinerator filter / collector. It mainly comprises a chemical supply pipe 7 for supplying a chemical for removing harmful components in the exhaust gas to the exhaust gas upstream of each of the dust collector 21 and the filter dust collector 10 for the ash melting furnace.
[0004]
In such a configuration, the waste is supplied to the incinerator 1 and incinerated, and the incinerator exhaust gas generated at this time is supplied to the incinerator filter / dust collector 21 via the gas cooling device 2. In the incinerator filter dust collector 21, dust and solidified harmful components in the incinerator exhaust gas are collected and removed. Since the incinerator exhaust gas contains harmful gases such as sulfur oxides and hydrogen chloride, chemicals such as slaked lime are usually supplied from the chemical supply pipe 7 to the incinerator exhaust gas upstream of the incinerator filter / dust collector 21. Then, the harmful components in the exhaust gas from the incinerator are reacted with a chemical to solidify, and collected as dust ash 22 together with the dust. The processing gas from which the dust and reactants have been removed is discharged from the chimney 6 to the outside of the system via the induction ventilator 5.
[0005]
On the other hand, the collected ash 22 collected by the incinerator filter dust collector 21 is supplied to the ash melting furnace 8 together with the incinerated ash 14 of the incinerator 1, and is melted. Is discharged. The incinerated ash 14 and the collected ash 22 are melted in the ash melting furnace 8 at a high temperature of about 1300 to 1400 ° C., though depending on their components. Instead of being contained therein, it is entrained in the melting furnace exhaust gas discharged from the ash melting furnace 8. Therefore, as in the case of the incinerator exhaust gas, a chemical is introduced from the chemical supply pipe 7 into the melting furnace exhaust gas after passing through the gas cooling device 9 before being introduced into the ash melting furnace filter dust collector 10. The gas is solidified, and the melting furnace processing gas 13 is combined with the incinerator processing gas downstream of the incinerator filter dust collector 21 by the fan 11 and discharged out of the system. The collected ash collected by the ash melting furnace filter dust collector 10 is not supplied to the ash melting furnace 8 because the harmful gas concentration in the melting furnace exhaust gas gradually increases when the ash is again supplied to the ash melting furnace 8. The ash is supplied to an ash solidification device 18 and solidified by a cement / chemical 19 and discharged as a final product.
[0006]
In the above exhaust gas treatment equipment, harmful gases such as sulfur oxides and hydrogen chloride gas contained in the incinerator exhaust gas and the melting furnace exhaust gas are respectively reacted with reactive agents such as slaked lime powder to solidify harmful components, and filtered for the incinerator. The dust is collected and removed by the dust collector 21 and the filtration dust collector 10 for the ash melting furnace. This solidification reaction is a so-called solid-gas reaction between a solid drug and a gaseous component, and the reaction is not sufficiently performed only by supplying an equivalent amount of the drug. Five to three times the amount of drug is dispensed. The introduced unreacted chemicals are collected by the ash melting furnace filter dust collector 10 as the collected ash 17, so that the amount of the collected ash 17 increases. There is a problem that the amount of the drug increases and the final solidification treatment cost increases. There is also a problem that the unreacted drug cannot be reused and is wasted. Further, since the chemicals are separately injected into the exhaust gas from the incinerator and the exhaust gas from the melting furnace, it is difficult to adjust the amount of the injected chemical, and it is difficult to reduce the amount of the injected chemical.
[0007]
[Patent Document 1]
Japanese Patent Application Laid-Open No. 9-173742
[Problems to be solved by the invention]
The object of the present invention is to solve the above-mentioned problems of the prior art and reduce the amount of chemicals used for removing harmful components in exhaust gas, the amount of cement and chemicals for solidifying collected ash, and the amount of final ash solidified material. It is an object of the present invention to provide an exhaust gas treatment device that can perform the treatment.
[0009]
[Means for Solving the Problems]
The present inventors have conducted intensive studies on the above-mentioned problems, and as a result, installed a filtration dust collector for an incinerator in two stages, and collected ash collected by a filtration dust collector for removing dust in the preceding stage in an ash melting furnace. The processing gas from which the dust is removed from the melting furnace exhaust gas is combined with the incinerator exhaust gas between the pre-stage and post-stage filtration dust collectors to remove harmful components from the combined exhaust gas. So that the collected ash collected by the harmful gas removal filter dust collector at the subsequent stage is mixed with the exhaust gas of the melting furnace upstream of the filter dust collector for the ash melting furnace. By doing so, the inventors have found that the above-mentioned object can be achieved, and have reached the present invention.
The invention claimed in this application to achieve the above object is as follows.
[0010]
(1) Filtration precipitators for incinerators for removing dust in exhaust gas from incinerators, and ash melting for melting incineration ash from the incinerators and collected ash collected by the filtration precipitators for incinerators In an exhaust gas treatment apparatus provided with a furnace and a filter and dust collector for an ash melting furnace for removing dust in exhaust gas from the ash melting furnace, Means for sequentially installing a filter and a harmful gas removal filter dust collector, a means for supplying collected ash collected by the dust removal filter dust collector to the ash melting furnace, and the harmful gas removal filter dust collector. Means are provided for joining the processing gas of the melting furnace from the ash melting furnace filter / dust collector to the upstream incinerator exhaust gas, and harmful gas is removed from the combined exhaust gas upstream of the harmful gas removal filter / dust collector. An exhaust gas treatment device provided with a means for introducing a chemical for performing the treatment.
(2) A means for mixing all or a part of the collected ash collected by the harmful gas removal filter dust collector with the melting furnace exhaust gas upstream of the ash melting furnace filter dust collector is provided. The exhaust gas treatment device according to claim 1, wherein:
[0011]
(3) Filtration precipitator for incinerator for removing dust in exhaust gas from incinerator, and ash melting for melting incineration ash of the incinerator and collected ash collected by the filtration precipitator for incinerator In an exhaust gas treatment apparatus provided with a furnace and a filter dust collector for an ash melting furnace that removes dust in a flue gas of the melting furnace of the ash melting furnace, the filter for dust removal is used as the filter dust collector for the incinerator. A dust collector and a harmful gas removal filtration dust collector are sequentially installed, and a means for supplying collected ash collected by the dust removal filtration dust collector to the ash melting furnace; and a harmful gas removal filtration collector. Means for mixing the collected ash collected by the dust collector with the exhaust gas of the melting furnace upstream of the filter dust collector for the ash melting furnace, and providing the exhaust gas of the incinerator upstream of the filter dust collector for harmful gas removal. An exhaust gas treatment device comprising means for introducing a chemical for removing harmful gas.
[0012]
[Action]
In the present invention, as shown in FIG. 1 described later, a filter dust collector 3 for removing dust and a filter dust collector 4 for removing harmful gas are sequentially installed via a duct 12 as a filter dust collector for an incinerator. Then, the collected ash 15 collected by the filtration dust collector 3 for dust removal is supplied to the ash melting furnace 8 to be melted, and the dust in the exhaust gas of the melting furnace is collected by the filtration dust collector 10 for the ash melting furnace. Removed, the melting furnace processing gas 13 is combined with the exhaust gas from the incinerator of the duct 12, and a chemical is supplied from the chemical supply pipe 7 connected to the duct 12 to remove harmful components in the combined exhaust gas. This makes it possible to carry out the introduction of the medicine in one place, thereby facilitating the adjustment of the introduction amount of the medicine, reducing the amount of the medicine, and reducing the amount of the collected ash 17 collected by the ash melting furnace filter dust collector 10. Reduction of cement and chemicals 19 necessary for solidifying the collected ash 17 Reduction of and the final solidified product becomes possible.
[0013]
Further, as shown in FIGS. 2 to 4 described later, all or a part of the collected ash 16 collected by the harmful gas removing filter dust collector 4 is transferred to the upstream of the ash melting furnace filter dust collector 10. By mixing with the melting furnace exhaust gas, the unreacted chemical contained in the collected ash 16 can be reacted with the harmful gas in the melting furnace exhaust gas, and the input chemical can be effectively used. That is, since the reactant for removing the harmful gas is blown in an amount of 1.5 to 3 times the equivalent ratio, the unreacted agent having an equivalent ratio of 0.5 to 1.5 times is collected. The collected ash 16 containing such unreacted chemicals is blown into the exhaust gas of the melting furnace in front of the filter dust collector for the ash melting furnace, so that the collected ash 16 in the collected ash 16 is collected. The unreacted chemical can be reacted with the harmful gas in the exhaust gas of the melting furnace, and the input chemical can be effectively used. In addition, since the amount of chemicals for removing harmful gas is reduced, the amount of collected ash 16, 17 collected by the filter dust collector 4 for the incinerator or the filter dust collector 10 for the ash melting furnace is reduced, The supply amount of the cement / drug 19 for solidifying the collected ashes 16 and 17 may be small, and the final solidified amount is also small. Further, the melting furnace treatment gas 13 from which corrosive gases such as sulfur oxides and hydrogen chloride gas in the melting furnace exhaust gas have been removed is joined to the upstream or downstream of the incinerator filter / dust collector 4 in order to join them. Due to corrosive gas in ducts and the like is prevented.
[0014]
BEST MODE FOR CARRYING OUT THE INVENTION
Hereinafter, the present invention will be described in detail with reference to the drawings, but the present invention is not limited thereto.
FIG. 1 is a system diagram of an exhaust gas treatment apparatus showing one embodiment of the present invention.
1 is different from FIG. 5 in that a filter dust collector 3 for removing dust and a filter dust collector 4 for removing harmful gas are sequentially connected via a duct 12 instead of the filter dust collector 21 for the incinerator. The collected ash 15 collected by the filter dust collector 3 for removing dust is supplied to the ash melting furnace 8 through a duct, and the processing gas of the melting furnace from the filter dust collector 10 for the ash melting furnace is supplied. 13 is merged with the incinerator exhaust gas from the duct 12 upstream of the harmful gas removing filter / dust collector 4 through the duct, and the chemical supplied from the chemical supply pipe 7 is supplied to the combined exhaust gas from the duct 12. Another point is that the collected ash 16 collected by the harmful gas removing filter dust collector 4 is supplied to the ash solidifying device 8.
According to such an exhaust gas treatment apparatus, the medicine can be injected at one place, and the adjustment of the amount of injected medicine becomes easy. It is possible to reduce the amount of collected ash 17 collected, the amount of cement and chemicals 19 required for the solidification of the collected ash 17, and the amount of final solidified material.
[0015]
FIG. 2 is a system diagram of an exhaust gas treatment apparatus showing another embodiment of the present invention.
2, the difference from FIG. 1 is that the collected ash 16 from the harmful gas removing filter dust collector 4 is combined with the exhaust gas of the melting furnace upstream of the ash melting furnace filter dust collector 10 via a duct. It is the point that it did.
With such a configuration, in addition to the above effects, the unreacted chemical contained in the collected ash 16 can be reacted with the exhaust gas from the melting furnace, and the effective use of the injected chemical and the reduction of the amount of the injected chemical can be achieved. Therefore, it is possible to further reduce the collected ash 17, the supply amount of the cement / chemical 19 for the solidification treatment, and the final solidified material. Further, since the melting furnace processing gas 13 from which the harmful gas has been removed is combined with the upstream of the incinerator filter / dust collector 4, corrosion due to a harmful gas (corrosive gas) such as a duct for merging can be prevented. .
[0016]
When the behavior of the harmful gas in the exhaust gas from the incinerator was investigated in the above-mentioned apparatus, about 10% of the harmful gas was adsorbed on the collected ash 15 of the filter dust collector 3 for removing dust, and about 90% of the remaining about 90% was collected. It has been clarified that the harmful gas passes through the dust collector 3 and is introduced into the harmful gas filter 4. In addition, a highly reactive slaked lime is used as a chemical that reacts with the harmful gas, and about 1.5 times the amount of the chemical with an equivalent ratio to the harmful gas is blown from the chemical supply pipe 7 so that the filter dust collector 4 for harmful gas removal can be used. The measurement results revealed that the concentration of harmful gas in the outlet gas satisfied the required value. From these results, about one-third of the drug supplied from the drug supply pipe 7 is contained in the collected ash 16 as an unreacted component, and the collected ash 16 is filtered by the filter dust collector for the ash melting furnace. The unreacted chemicals can be effectively used by blowing the gas into the exhaust gas (including the above harmful gas of about 10%) in the upstream of the melting furnace. Even in the test using this apparatus, the amount of harmful gas in the exhaust gas from the incinerator upstream of the harmful gas removal filter and dust collector 4 was reduced to about 90%. The amount, the amount of cement and chemicals used for collecting and solidifying ash, and the amount of final solidified material could be reduced by about 10%.
[0017]
FIG. 3 is a system diagram of an exhaust gas treatment apparatus showing still another embodiment of the present invention.
3 is different from FIG. 2 in that a part of the collected ash 16 from the harmful gas removal filter dust collector 4, for example, an amount of ash trapped in a surplus furnace exhaust gas that is necessary to remove harmful gas components. The ash collector 16 is combined with the melting furnace exhaust gas upstream of the ash melting furnace filter dust collector 10, and the remaining collected ash 16 is supplied to an ash solidifying device 18.
With such a configuration, in addition to the above-described effects, the amount of the collected ash 16 can be adjusted according to the amount of harmful gas contained in the exhaust gas of the melting furnace. Processing efficiency can be improved.
[0018]
FIG. 4 is a system diagram of an exhaust gas treatment apparatus showing still another embodiment of the present invention.
4 is different from FIG. 2 in that the melting furnace processing gas 13 processed by the ash melting furnace filtration dust collector 10 is combined with the processing gas downstream of the harmful gas removal filtration dust collector 4. It is a point that did. With such a configuration, the processing efficiency of the harmful gas removing filtration dust collector 4 can be improved.
[0019]
【The invention's effect】
According to the first aspect of the present invention, the filter dust collector for the incinerator is installed in two stages, and the processing gas of the exhaust gas of the melting furnace is combined with the exhaust gas of the incinerator from which the dust has been removed. By adding the removing agent, it becomes easy to control the amount of the agent, and the amount of the agent is reduced, the amount of collected ash is reduced, the amount of cement and agent for solidifying the collected ash is reduced, and the amount of the final solidified material is reduced. Therefore, the life of a landfill site can be extended.
According to the second or third aspect of the invention, in addition to the above-mentioned effects, it is possible to effectively use the unreacted drug for removing the harmful gas, and it is possible to further reduce the harmful gas removal drug and the like.
[Brief description of the drawings]
FIG. 1 is a system diagram of an exhaust gas treatment apparatus showing one embodiment of the present invention.
FIG. 2 is a system diagram of an exhaust gas treatment apparatus showing another embodiment of the present invention.
FIG. 3 is a system diagram of an exhaust gas treatment apparatus showing still another embodiment of the present invention.
FIG. 4 is a system diagram of an exhaust gas treatment apparatus showing still another embodiment of the present invention.
FIG. 5 is a system diagram of a conventional exhaust gas treatment apparatus.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 ... Incinerator, 2 ... Gas cooling device, 3 ... Filter dust collector for dust removal, 4 ... Filter dust collector for harmful gas removal, 5 ... Induction ventilator, 6 ... Chimney, 7 ... Chemical supply pipe, 8 ... ash melting furnace, 9 ... gas cooling device, 10 ... filter and dust collector for ash melting furnace, 11 ... fan, 12 ... duct, 13 ... melting furnace exhaust gas, 14 ... incineration ash, 15, 16, 17 ... collection ash , 18: Ash solidification device, 19: Cement / drug, 20: Melt slag, 21: Filtration dust collector for incineration path, 22: Ash collected.

Claims (3)

焼却炉の排ガス中のばい塵を除去する焼却炉用ろ過集塵器と、前記焼却炉の焼却灰および該焼却炉用ろ過集塵器で捕集した捕集灰を溶融する灰溶融炉と、該灰溶融炉の排ガス中のばい塵を除去する灰溶融炉用ろ過集塵器とを備えた排ガス処理装置において、前記焼却炉用ろ過集塵器として、ばい塵除去用ろ過集塵器と有害ガス除去用ろ過集塵器を順に設置し、該ばい塵除去用ろ過集塵器で捕集した捕集灰を前記灰溶融炉に供給する手段および該有害ガス除去用ろ過集塵器前流の焼却炉排ガスに前記灰溶融炉用ろ過集塵器からの溶融炉処理ガスを合流させる手段を設けるとともに、該有害ガス除去用ろ過集塵器前流の前記合流排ガスに有害ガスを除去するための薬剤を投入する手段を設けたことを特徴とする排ガス処理装置。An incinerator filter dust collector for removing dust in exhaust gas of an incinerator, and an ash melting furnace for melting the incineration ash of the incinerator and the collected ash collected by the incinerator filter dust collector, In an exhaust gas treatment device provided with a filter dust collector for an ash melting furnace that removes dust in exhaust gas from the ash melting furnace, the filter dust collector for an incinerator is provided with a filter dust collector for removing dust. A gas removing filter dust collector is installed in order, a means for supplying the collected ash collected by the dust removing filter dust collector to the ash melting furnace, and a means upstream of the harmful gas removing filter dust collector. A means for joining the melting furnace processing gas from the ash melting furnace filter dust collector to the incinerator exhaust gas is provided, and a harmful gas is removed from the combined exhaust gas in front of the harmful gas removal filter dust collector. An exhaust gas treatment device comprising a means for introducing a drug. 前記有害ガス除去用ろ過集塵器で捕集した捕集灰の全部または一部を、前記灰溶融炉用ろ過集塵器前流の溶融炉排ガスに混合させる手段を設けたことを特徴とする請求項1に記載の排ガス処理装置。A means for mixing all or a part of the collected ash collected by the harmful gas removal filter dust collector with the melting furnace exhaust gas upstream of the ash melting furnace filter dust collector is provided. The exhaust gas treatment device according to claim 1. 焼却炉の排ガス中のばい塵を除去する焼却炉用ろ過集塵器と、前記焼却炉の焼却灰および該焼却炉用ろ過集塵器で捕集した捕集灰を溶融する灰溶融炉と、該灰溶融炉の排ガス中のばい塵を除去する灰溶融炉用ろ過集塵器とを備えた排ガス処理装置において、前記焼却炉用ろ過集塵器として、ばい塵除去用ろ過集塵器と有害ガス除去用ろ過集塵器を順に設置し、該ばい塵除去用ろ過集塵器で捕集した捕集灰を前記灰溶融炉に供給する手段および該有害ガス除去用ろ過集塵器で捕集した捕集灰を前記灰溶融炉用ろ過集塵器前流の溶融炉排ガスに混合させる手段とを設けるとともに、該有害ガス除去用ろ過集塵器前流の焼却炉排ガスに有害ガスを除去するための薬剤を投入する手段を設けたことを特徴とする排ガス処理装置。An incinerator filter dust collector for removing dust in exhaust gas of an incinerator, and an ash melting furnace for melting the incineration ash of the incinerator and the collected ash collected by the incinerator filter dust collector, In an exhaust gas treatment device provided with a filter dust collector for an ash melting furnace that removes dust in exhaust gas from the ash melting furnace, the filter dust collector for an incinerator is provided with a filter dust collector for removing dust. A gas removing filter dust collector is installed in order, and the collected ash collected by the dust removing filter dust collector is supplied to the ash melting furnace and collected by the harmful gas removing filter dust collector. Means for mixing the collected ash with the exhaust gas of the melting furnace upstream of the filter dust collector for the ash melting furnace, and removing harmful gas from the exhaust gas of the incinerator upstream of the filter dust collector for harmful gas removal. Exhaust gas treatment device provided with means for introducing a chemical for use in the treatment.
JP2003050657A 2003-02-27 2003-02-27 Exhaust gas treatment equipment Expired - Fee Related JP4361296B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2003050657A JP4361296B2 (en) 2003-02-27 2003-02-27 Exhaust gas treatment equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2003050657A JP4361296B2 (en) 2003-02-27 2003-02-27 Exhaust gas treatment equipment

Publications (2)

Publication Number Publication Date
JP2004255329A true JP2004255329A (en) 2004-09-16
JP4361296B2 JP4361296B2 (en) 2009-11-11

Family

ID=33116011

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2003050657A Expired - Fee Related JP4361296B2 (en) 2003-02-27 2003-02-27 Exhaust gas treatment equipment

Country Status (1)

Country Link
JP (1) JP4361296B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010115588A (en) * 2008-11-12 2010-05-27 Kubota Corp Melting treatment method of incineration ash and melting treatment equipment

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010115588A (en) * 2008-11-12 2010-05-27 Kubota Corp Melting treatment method of incineration ash and melting treatment equipment

Also Published As

Publication number Publication date
JP4361296B2 (en) 2009-11-11

Similar Documents

Publication Publication Date Title
US5413621A (en) Process for cooling and purifying hot, dust-laden flue gases containing dioxins and other toxic substances
JP2010075897A (en) Apparatus for fly ash treatment, method for fly ash treatment, waste disposal system, and operation method for waste disposal system
JP3285692B2 (en) Fly ash treatment device in incinerator
JP2009112910A (en) Removal method and apparatus for mercury in incineration ash containing mercury and treatment apparatus for exhaust gas containing mercury
JP2007117890A (en) Exhaust gas treating method and system
JP4361296B2 (en) Exhaust gas treatment equipment
JP2001096134A (en) Treatment method of combustion gas containing heavy metal
JP4084503B2 (en) Processing method of incinerated fly ash containing dioxins
JP3664941B2 (en) Exhaust gas treatment method and system for ash melting furnace
JP3202453B2 (en) Exhaust gas treatment method for melting furnace
JP2001311588A (en) Exhaust gas treatment method and apparatus
JP2003190915A (en) Method of melting treatment and apparatus therefor
JP2000117223A (en) Ash treatment for waste melting treatment device
JP2005195228A (en) Waste material melting treatment system
JP3343328B2 (en) Apparatus and method for melting wet ash
JP2003334511A (en) Fly ash stabilizing apparatus
JP3970065B2 (en) Waste treatment equipment
JP2003212618A (en) Method for treating organic contaminated soil
JPH1157373A (en) Operation of electric melting furnace
JP2002273164A (en) Treatment method for defusing exhaust gas in refuse incinerator and system therefor
JP2004138253A (en) Method for blowing inflammable dust into waste melting furnace
JPH10277335A (en) Dust collecting device for electric furnace
JPH1130406A (en) Combustion method for fluidized bed
JP4015887B2 (en) Method for treating molten exhaust gas
JP2004024982A (en) Treatment method of flue gas from melting furnace

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20060209

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20071101

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20090519

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20090710

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20090804

A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20090812

R150 Certificate of patent or registration of utility model

Free format text: JAPANESE INTERMEDIATE CODE: R150

Ref document number: 4361296

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120821

Year of fee payment: 3

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130821

Year of fee payment: 4

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

S111 Request for change of ownership or part of ownership

Free format text: JAPANESE INTERMEDIATE CODE: R313111

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

S111 Request for change of ownership or part of ownership

Free format text: JAPANESE INTERMEDIATE CODE: R313113

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

LAPS Cancellation because of no payment of annual fees