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JP3641393B2 - Exhaust gas treatment method and apparatus using pulse dust removal type bag filter - Google Patents
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JP3641393B2 - Exhaust gas treatment method and apparatus using pulse dust removal type bag filter - Google Patents

Exhaust gas treatment method and apparatus using pulse dust removal type bag filter Download PDF

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Publication number
JP3641393B2
JP3641393B2 JP18270099A JP18270099A JP3641393B2 JP 3641393 B2 JP3641393 B2 JP 3641393B2 JP 18270099 A JP18270099 A JP 18270099A JP 18270099 A JP18270099 A JP 18270099A JP 3641393 B2 JP3641393 B2 JP 3641393B2
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Japan
Prior art keywords
reaction
exhaust gas
bag filter
filter
reaction aid
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JP18270099A
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JP2001009234A (en
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正和 澤井
修一郎 畠山
宇逸 浅井
浩司 林
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Amano Corp
Kawasaki Motors Ltd
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Amano Corp
Kawasaki Jukogyo KK
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  • Treating Waste Gases (AREA)
  • Filtering Of Dispersed Particles In Gases (AREA)

Description

【0001】
【発明の属する技術分野】
本発明は、燃焼有害ガスや悪臭ガスと言った各種の排ガスを、パルス除塵式バグフイルタの濾布面に付着させた反応助剤に接触させることにより、脱臭や脱硫等の各種処理を行えるように工夫したパルス除塵式バグフイルタを用いた排ガス処理方法とその装置に関するものである。
【0002】
【従来の技術】
パルス除塵式バグフイルタの濾布面に付着させた反応助剤を用いて、排ガスを反応処理することができる排ガス処理装置に関しては、従来より例えば実開平7−13422号公報(実願平5−45988号)に記載の如きバグフイルタ式脱臭装置が存在する。
【0003】
この脱臭装置は、脱臭剤を飽和状態に成る迄繰返し使用できるようにしたものであって、フイルタ室のバグフイルタの濾布面に付着させて脱臭に用いた使用済みの脱臭剤を、パルスジェットエアーで下側のホッパーに払い落した後、これを脱臭剤供給タンクに回収して再度利用するように構成されている。
【0004】
【発明が解決しようとする課題】
しかし、上記従来のバグフイルタ式脱臭装置によれば、新しい脱臭剤が供給された当初の時点では、脱臭剤のガス吸着機能(脱臭機能)は高いが、これを繰返し使用することで吸着性能が次第に低下し、全体のランニングの中では排ガスの吸着性能に変動(劣化)が発生して、充分な脱臭効果を発揮できなくなる問題があった。
【0005】
更に、上記従来のバグフイルタ式脱臭装置は、パルスジェットエアーによって払い落した使用済みの脱臭剤を、再び同じ脱臭剤を収容した供給タンクに回収して再利用するものであって、常に1種類の脱臭剤を使用する構成になっているため、例えば、性質の異なる酸性ガスやアルカリ性ガス等の混合ガスを除去したり脱臭したりする場合には、上記のバグフイルタ式脱臭装置(除去装置)を複数台連ねて、処理するガスに合せて除去装置を選んで使い分ける必要があり、使用操作が非常に煩雑であると共に、装置全体が複雑化、大型化して、高コスト化を招く問題もあった。
【0006】
従って本発明の技術的課題は、排ガスに対する吸着処理機能を低下させることなく、バグフイルタから払い落した使用済みの反応助剤(脱臭剤等)を再利用することができると共に、1台の処理装置によって複数種の排ガスの処理を可能にしたパルス除塵式バグフイルタを用いた排ガス処理方法とその装置を提供することである。
【0007】
【課題を解決するための手段】
上記の技術的課題を解決するために本発明で講じた手段は以下の如くである。
【0008】
粉末状の反応助剤をパルス除塵式バグフイルタの濾布面に付着させ、ブロアーの吸引作用を受けてこのバグフイルタを通過する燃焼有害ガスや悪臭ガス等の排ガスを上記の反応助剤に接触させて反応処理する一方、上記バグフイルタの濾布面に付着している使用済みの反応助剤を、逆洗用のパルスジェットエアーで下側のホッパーに払い落すようにしたパルス除塵式バグフイルタを用いた排ガス処理方法であって、
【0009】
(1) 上記使用済み反応助剤をパルスジェットエアーで払い落した後、1種類又は複数種類の新たな反応助剤を上記バグフイルタの濾布面に付着し、次いで、ホッパー内に払い落した上記使用済みの反応助剤をバグフイルタの濾布面に付着している上記新たな反応助剤の外側面に多重に付着させ、これ等多重に付着した新旧の反応助剤によって上記の排ガスを反応処理すること。(請求項1)
【0010】
(2) 使用済み反応助剤をパルスジェットエアーで下側のホッパーに払い落した後、複数種の新たな反応助剤の中から必要とする反応助剤を1種類又は複数種類選んでこれをバグフイルタの濾布面に付着し、次いで、この新たな反応助剤の外側面に上記ホッパー内に払い落した使用済みの反応助剤を多重に付着すること。(請求項2)
【0011】
(3) ホッパーに払い落した使用済み反応助剤をエアーで舞い上げ、これをブロアーの吸引作用を利用して新たな反応助剤の外側面に多重に付着すること。 (請求項3)
【0012】
(4) ホッパーに払い落した使用済み反応助剤をホッパーの外部に回収し、この回収した使用済み反応助剤をブロアーの送風作用又は吸引作用によってバグフイルタ側に再供給して、新たな反応助剤の外側面に多重に付着すること。(請求項4)
【0013】
ブロアーの送風作用又は吸引作用を受けて排ガスの導入ダクトを通してフイルタ室内に供給又は吸引した粉末状の反応助剤を、パルス除塵式バグフイルタの濾布面に付着し、上記導入ダクトを通って吸引されて来る燃焼有害ガスや悪臭ガス等の排ガスを上記反応助剤に接触させて反応処理する一方、上記バグフイルタの濾布面に付着している使用済みの反応助剤を、逆洗用のパルスジェットエアーで逆洗して下側のホッパーに払い落すように構成したパルス除塵式バグフイルタを用いた排ガス処理装置であって、
【0014】
(5) 上記排ガス導入ダクトの途中に新たな反応助剤を供給するための助剤供給手段を1台又は複数台接続し、上記のホッパーにはパルスジェットエアーによって払い落された使用済み助剤をエアーを噴射して舞い上げる助剤舞い上げ手段を設けて、上記助剤供給手段による新しい反応助剤の供給を終えた後、上記助剤舞い上げ手段による使用済み反応助剤の舞い上げを行って、上記バグフイルタの濾布面に新旧の反応助剤を順番に、且つ、多重に付着させるように構成すること。(請求項5)
【0015】
(6) 上記排ガス導入ダクトの途中に、新たな反応助剤を供給するための1台又は複数台の新規助剤供給手段と、上記ホッパーから回収した使用済み反応助剤を供給するための使用済み助剤供給手段を接続し、上記新規助剤供給手段による新しい反応助剤の供給を終えた後、上記使用済み助剤供給手段による使用済み反応助剤の供給を行って、上記バグフイルタの濾布面に新旧の反応助剤を順番に、且つ、多重に付着させるように構成すること。(請求項6)
【0016】
尚、ここに於いて反応助剤とは、例えば、粉末状に形成した脱臭剤、脱硝剤、或は、脱硫剤等を意味する。
【0017】
▲1▼ 上記(1)で述べた請求項1に係る手段(排ガス処理方法)によれば、使用済みの反応助剤をパルスジェットエアーで払い落した後、1種類又は複数種類の未使用の新たな反応助剤をバグフイルタの濾布面に付着し、その後、払い落した使用済みの反応助剤を上記新しい反応助剤の外側面に多重に付着するため、外層に付着した古い反応助剤が先ず荒取りの反応処理(交流接触)を行い、次いで、内層の新しい反応助剤によって仕上げの処理を行うことができるものであって、使用済み反応助剤の再利用によって除去能率を低下させることなく、複数層に重ねて付着させた新旧の反応助剤によって安定した吸着作用を発揮して、排ガスに対する脱臭や脱硫等の処理効果を向上させることを可能にする。
【0018】
▲2▼ 上記(2)で述べた請求項2に係る手段(排ガス処理方法)によれば、複数種の新たな反応助剤の中から必要とする反応助剤を選んでこれをバグフイルタの濾布面に付着でき、更に、この新たな反応助剤の外側面に使用済みの反応助剤を多重に付着させるため、これ等複数層に重ねて付着させた新旧の反応助剤によって、排ガスの処理効果を向上させることができると共に、複数種の反応助剤を使用可能にしたので、処理する排ガスの種類に合せて使用する反応助剤を選択することにより、例えば酸性ガスやアルカリ性と言った性状が異なる排ガスに応じた反応処理を行うことを可能にする。
【0019】
▲3▼ 上記(3)で述べた請求項3に係る手段(排ガス処理方法)によれば、パルスジェットエアーによって払い落された使用済みの反応助剤を、エアーで舞い上げ、且つ、ブロアーの吸引作用で新たな反応助剤の外側面に多重に付着できるため、バグフイルタの濾布面に多重に付着形成したこれ等新旧の反応助剤の層が、排ガスを安定した状態で効率良く反応処理することを可能にする。
【0020】
▲4▼ 上記(4)で述べた請求項4に係る手段(排ガス処理方法)によれば、パルスジェットエアーによって払い落された使用済みの反応助剤をホッパーの外部に回収し、これをブロアーの送風又は吸引作用によって新たな反応助剤の外側面に多重に付着できるため、バグフイルタの濾布面に多重に付着形成したこれ等新旧の反応助剤の層が、排ガスを安定した状態で効率良く反応処理することを可能にする。
【0021】
▲5▼ 上記(5)で述べた請求項5に係る手段(排ガス処理装置)によれば、排ガス導入ダクトの途中に接続した1台又は複数台の助剤供給手段から、除塵を済ませたバグフイルタの面に必要とする1種類又は複数種類の新しい反応助剤が順番に供給されて多重に付着され、また、パルスジェットエアーによってホッパーに払い落された使用済みの反応助剤は、助剤舞い上げ手段によって舞い上げられて上記新しい反応助剤の外側面に重ねて付着されるため、これ等多重層に付着形成された新旧の反応助剤の層によって安定した吸着作用を発揮して、排ガスを効率良く反応処理することを可能にする。
【0022】
▲6▼ 上記(6)で述べた請求項6に係る手段(排ガス処理装置)によれば、必要とする1種類又は複数種類の新たな反応助剤を、処理する排ガスの種類に応じてバグフイルタの濾布面に供給して付着でき、更に、ホッパーから使用済み助剤供給手段に回収した使用済み反応助剤を、上記新たな反応助剤の外側面に重ねて付着できるため、バグフイルタの濾布面に多重に付着形成したこれら新旧の反応助剤の層が、各種の排ガスを安定した状態で効率良く反応処理することを可能にする。
【0023】
以上の如くであるから、上記(1)〜(6)の手段によって上述した技術的課題を解決して、前記従来の技術の問題点を解消することができる。
【0024】
【発明の実施の形態】
以下に、本発明に係るパルス除塵式バグフイルタを用いた排ガス処理方法とその装置の実施の形態を図面と共に説明すると、図1は本発明の排ガス処理装置の外観を説明した正面図、図2はその拡大側面図、図3は本発明の全体を明示した構成図であって、これ等の図面に於いて、夫々符号1で全体的に示したのはバグフイルタ式の集塵機で、1Aと1Bは仕切板1Xによって上下に区画形成された集塵機1の清浄室とフイルタ室、1Cはフイルタ室1Bの下側に連設したホッパー、2…はフイルタ室1B内に吊下げたバグフイルタを示す。
【0025】
また、3は上記清浄室1Aの内部に設けたパルスジェット用のブローチューブ、3Tはヘッダパイプ、3A…はブローチューブ3に設けたエアー噴射用のノズルであって、上記のヘッダパイプ3Tからブローチューブ3に送られて来るパルスジェットエアー(圧縮エアー)を、各ノズル3A…から上記各バグフイルタ2…の内部に吹き込むことにより、各バグフイルタ2…の濾布面に付着している使用済みの反応助剤を下側のホッパー1Cに払い落すことができる仕組に成っている。
【0026】
4は上記集塵機1の清浄室1Aに接続した吸引ダクト、4Aはこの吸引ダクト4の先端側に接続した吸引ブロアー(吸引ファン)、4Mはブロアー駆動用モータ、4Tは風量調節弁、4Bは排気筒であって、上記吸引ブロアー4Aの吸引作用は、上記の吸引ダクト4を経て集塵機1の清浄室1Aからバグフイルタ2…、及び、フイルタ室1Bを通して排ガス導入ダクト7に及んで、排ガスを集塵機1のフイルタ室1B内に吸引する仕組に成っている。
【0027】
更に図中、5は上記ホッパー1Cの底部に設けた使用済み反応助剤の排出装置、5Sはこの排出装置5を構成する排出用スクリューで、このスクリュー5Sによって排出される使用済み反応助剤は、排出弁5A及び排出ダクト5Bを経てフレキシブルコンテナ6に送り込まれて回収され、次いで、ガイドレール14に取付けたホイスト15等の輸送手段を用いて後述する使用済み反応助剤供給手段 (供給タンク)に搬送されて送り込まれる仕組に成っているが、これは実施の一例であって、例えばホッパー1Cに回収した使用済み反応助剤を、輸送用エアーパイプ等を用いて上記の供給タンクに直接送り込んでもよく、その選択は任意とする。
【0028】
更に図中、8は上記ホッパー1C内に設けたエアー噴射パイプ8Aに圧縮エアーを送って、ホッパー1C内に落下して溜った使用済み反応助剤を舞い上げることができるエアーレーション用パイプ、9は先端を上記排ガス導入ダクト7に接続した助剤供給ダクト、10,11はこの供給ダクト9の途中に接続した助剤供給タンク、10A,11Aは各タンク10,11に設けた助剤供給バルブ、12は上記供給ダクト9に設けた助剤供給用ブロアー、12Mはその駆動用モータであって、これ等ブロアー12と供給バルブ10A,11Aの働きによって、各供給タンク10,11に収容した反応助剤を順番に供給ダクト9を通して集塵機1のフイルタ室1B内に送り込むことができる仕組に成っている。
【0029】
尚、図1には各助剤供給タンク10,11毎に助剤供給用ブロアー12,12と供給ダクト9,9を設けて、排ガス導入ダクト7に対して反応助剤を別々に供給する構成が示されているが、これは実施の一例であって、図3の構成図に示すように1本の供給ダクト9に2台の助剤供給タンク10,11を接続し、且つ、1台の助剤供給用ブロアー12で各助剤供給タンク10,11内の反応助剤を順番に供給するようにすることによって、装置全体の簡略化を図るようにしてもよく、その選択は任意とする。
【0030】
更に図3に示した構成図には、スクリュー5Sを用いてフレキシブルコンテナ6に回収した使用済み反応助剤を、2番目の助剤供給タンク10に送り込んで再利用する構成が示されているが、これも実施の一例であって、1台目の助剤供給タンク11と、2台目の助剤供給タンク10、或は、3台目以上の複数台の助剤供給タンクの夫々に、排ガスの性質に合せて選んだ異なる種類の新しい反応助剤を収容する一方、フレキシブルコンテナ6を用いて回収した使用済み反応助剤を別に設けた3台目或はその他の供給タンク(図示省略)に送り込んで再利用したり、或は、フレキシブルコンテナ6を使用せずに、上記エアー噴射パイプ8Aからのエアー噴射(エアーレーション)による舞い上げだけで、使用済み反応助剤の再利用を図るようにしてもよく、その選択も任意とする。
【0031】
而して、図1乃至図3に於いて、1H…は集塵機1を支持する支持脚、1Rは支持台、1Eと1Fは保護柵、7Aは集塵機1に接続した排ガス導入ダクト7の先端部、7Xは逆止弁で、13は反応助剤の供給時に各助剤供給タンク10,11から立ち昇るダスト(反応助剤)を、各フード13A,13Bを用いて上記のダクト7側に吸引させる集塵ダクトである。
【0032】
本発明は以上述べた如き構成であるから、助剤供給用ブロアー12の送風作用を及ぼしながら、更にまた、吸引ブロアー4Aの吸引作用を集塵機1の内部を通して排ガス導入ダクト7側に及ぼしながら、1番目の助剤供給タンク11の供給バルブ11Aを作動して未使用の新しい反応助剤を供給ダクト9に送り出すと、この反応助剤が排ガス導入ダクト7を通って集塵機1のフイルタ室1Bに送り込まれるため、この新しい反応助剤を各バグフイルタ12…の濾布面に付着させることができる。
【0033】
次いで、2番目の助剤供給タンク10の供給バルブ10Aを作動して異なる新しい反応助剤を供給ダクト9に送り出せば、気流に乗ってこの反応助剤が上記各バグフイルタ2…に付着した反応助剤層の外側面に付着して、これにて各バグフイルタ2…の濾布面に異なる未使用の反応助剤の層を二重に形成することができるが、処理する排ガスによっては必ずしもこの2番目の助剤供給タンク10の反応助剤を付着させなくてもよい場合があることは勿論である。
【0034】
その後、エアー噴射パイプ8Aからエアーを噴射してホッパー1C内に溜っている使用済み反応助剤をフイルタ室1Bに舞い上げるか、又は、図示していない3台目或はその他の助剤供給タンクに回収されている使用済み反応助剤を気流に乗せてフイルタ室1Bに送り込むことにより、上記2層目の反応助剤の外側面に使用済み反応助剤の層(3層目)を多重に付着形成することができる。
【0035】
図4はバグフイルタ2の濾布面に上記計3層の反応助剤を多重に付着形成した状態を説明した断面図であって、図中、2Aは例えばゼオライトを用いた1層目の反応助剤層、2Bは例えば活性コークスを用いた2層目の反応助剤層、2Cは前回使用した3層目の使用済み反応助剤層(例えばゼオライト+活性コークス)であって、図示矢印方向に通過する排ガスは、先ず3層目の使用済み反応助剤層2Cによって粗取り(交流接触)が行われ、次いで、2層目の新しい反応助剤層2B及び1層目の新しい反応助剤層2Aの順に接触が繰り返されて、脱臭や脱硫等の反応処理が行われ、反応処理後の浄化ガスがバグフイルタ2…を通って清浄室1A側に排出され、更に、吸引ダクト4を通って集塵機1の外部に排出される仕組に成っている。
【0036】
以上の反応処理を繰り返した各反応助剤層2A,2B,2Cは、ある時期が来るとブローチューブ3のノズル3A…から各バグフイルタ2…内に吹き込まれるパルスジェットエアーによって下側のホッパー2Cに払い落され、次いで、上述した各反応助剤の付着処理を再び繰り返して、各バグフイルタ2…の濾布面に各反応助剤層2A,2B,2Cを多重に付着形成することによって、排ガスの処理運転を再開する。
【0037】
尚、図3に示した構成図では、フレキシブルコンテナ6を用いて回収した使用済み反応助剤2Cを2台目の助剤供給タンク10に送り込んで再利用する構成になっているため、1台目の助剤供給タンク11から供給される新しい反応助剤によって形成される1層目の反応助剤層2Aの外側面に、この使用済み反応助剤の層2Cが重ねて付着形成されることになるが、これは実施の一例であることは勿論である。
【0038】
【発明の効果】
以上述べた如く、本発明に係るパルス除塵式バグフイルタを用いた排ガス処理方法とその装置によれば、バグフイルタの濾布面に先ず未使用の新しい反応助剤の層を付着形成し、次いで、この層の外側にパルスジェットエアーによって払い落された使用済み反応助剤の層を多重に重ねて付着形成するため、反応助剤の吸着処理能力を低下させることなく、これ等新旧の反応助剤層によって排ガスを効率良く反応処理することができると共に、複数の異なる種類の反応助剤をバグフイルタの濾布面に付着させることができるため、1台にて各種排ガスの処理を行える利点を発揮できるものであって、使用済みの反応助剤を有効的に再利用できる点、並びに、既存の集塵機をそのまま使用できる点と相俟って、各種排ガスの脱臭や脱硫等に用いて洵に好適なものである。
【図面の簡単な説明】
【図1】本発明を実施した集塵装置の正面図である。
【図2】本発明を実施した集塵装置の側面図である。
【図3】本発明の全体を明示した構成図である。
【図4】バグフイルタの濾布面に多重に付着形成した反応助剤の層を拡大して示した断面図である。
【符号の説明】
1 集塵機
1C ホッパー
2 バグフイルタ
2A,2B 新しい反応助剤の層
2C 使用済み反応助剤の層
3 パルスジェットエアー用のブローチューブ
4A 吸引用ブロアー
5 使用済み反応助剤の排出装置
7 排ガス導入ダクト
8A 舞い上げ用のエアー噴射パイプ
10,11 反応助剤供給タンク
12 助剤供給用ブロアー
[0001]
BACKGROUND OF THE INVENTION
The present invention enables various treatments such as deodorization and desulfurization by bringing various exhaust gases such as combustion harmful gas and malodorous gas into contact with the reaction aid adhered to the filter cloth surface of the pulse dust removal type bag filter. The present invention relates to an exhaust gas treatment method using a devised pulse dust removal type bag filter and an apparatus therefor.
[0002]
[Prior art]
Regarding an exhaust gas treatment apparatus capable of reacting exhaust gas using a reaction aid adhered to a filter cloth surface of a pulse dust removal type bag filter, for example, Japanese Utility Model Laid-Open No. 7-13422 (Japanese Utility Model Application No. 5-44988) has been known. There is a bag filter type deodorizing apparatus as described in No.).
[0003]
This deodorizer is designed so that the deodorizer can be used repeatedly until it reaches saturation, and the used deodorizer attached to the filter cloth surface of the bag filter in the filter chamber is used for the deodorization. Then, after the hopper is wiped down to the lower hopper, it is collected in the deodorant supply tank and reused.
[0004]
[Problems to be solved by the invention]
However, according to the conventional bag filter type deodorization apparatus, the gas adsorption function (deodorization function) of the deodorant is high at the initial time when the new deodorant is supplied, but the adsorption performance is gradually increased by repeatedly using this. There is a problem that the exhaust gas adsorption performance fluctuates (deteriorates) during the entire running, and a sufficient deodorizing effect cannot be exhibited.
[0005]
Further, the conventional bag filter type deodorizing apparatus is for recovering and reusing the used deodorant, which has been wiped off by pulse jet air, in a supply tank containing the same deodorant. Since it is configured to use a deodorizer, for example, when removing or deodorizing mixed gases such as acid gas or alkaline gas having different properties, a plurality of the above-mentioned bag filter type deodorization devices (removal devices) are used. It is necessary to select and use a removal device according to the gas to be processed, and the use operation is very complicated, and the entire device becomes complicated and large, resulting in high costs.
[0006]
Therefore, the technical problem of the present invention is that it is possible to reuse the used reaction aid (deodorant, etc.) that has been removed from the bag filter without deteriorating the adsorption treatment function for exhaust gas, and a single treatment device. It is an object to provide an exhaust gas treatment method using a pulse dust removal type bag filter and an apparatus thereof capable of treating multiple types of exhaust gas.
[0007]
[Means for Solving the Problems]
Means taken in the present invention to solve the above technical problems are as follows.
[0008]
A powdery reaction aid is attached to the filter cloth surface of the pulse dust-removing bag filter, and the exhaust gas such as combustion harmful gas and malodorous gas that passes through the bag filter under the suction action of the blower is brought into contact with the reaction aid. Exhaust gas using a pulse dust removal type bag filter in which the spent reaction aid adhering to the filter cloth surface of the bag filter is removed to the lower hopper with pulse jet air for backwashing while the reaction treatment is performed. A processing method,
[0009]
(1) After the above-mentioned used reaction assistant is wiped off with pulse jet air, one or more kinds of new reaction assistants are attached to the filter cloth surface of the bag filter, and then are wiped off into the hopper. The spent reaction aid is attached to the outer surface of the new reaction aid, which is attached to the filter surface of the bag filter, and the exhaust gas is reacted with the old and new reaction aids. To do. (Claim 1)
[0010]
(2) After removing the used reaction aid to the lower hopper with pulse jet air, select one or more required reaction aids from multiple new reaction aids. Adhering to the filter cloth surface of the bag filter, and then adhering the used reaction aids, which have been scraped into the hopper, to the outer surface of the new reaction aid. (Claim 2)
[0011]
(3) Spent the spent reaction aid that has been scraped off to the hopper with air, and apply it to the outer surface of the new reaction aid by using the suction action of the blower. (Claim 3)
[0012]
(4) The spent reaction aid that has been scraped off to the hopper is collected outside the hopper, and the collected spent reaction aid is re-supplied to the bag filter side by the blower blowing action or suction action. Multiple adhesion to the outer surface of the agent. (Claim 4)
[0013]
The powdery reaction aid supplied or sucked into the filter chamber through the exhaust gas introduction duct under the blower's blowing action or suction action adheres to the filter cloth surface of the pulse dust removal type bag filter and is sucked through the introduction duct. The exhaust gas such as flammable toxic gas and bad odor gas is brought into contact with the above reaction aid for reaction treatment, while the used reaction aid adhering to the filter cloth surface of the bag filter is treated with a pulse jet for backwashing. An exhaust gas treatment apparatus using a pulse dust removal type bag filter configured to be backwashed with air and wiped off to the lower hopper,
[0014]
(5) One or more auxiliary agent supplying means for supplying a new reaction auxiliary agent are connected in the middle of the exhaust gas introduction duct, and the used auxiliary agent is removed by pulse jet air to the hopper. An auxiliary agent raising means for raising the air by blowing air is provided, and after the supply of the new reaction auxiliary by the auxiliary agent supply means is finished, the used auxiliary reaction agent is raised by the auxiliary agent raising means. Then, the old and new reaction aids are sequentially and multiply attached to the filter surface of the bag filter. (Claim 5)
[0015]
(6) One or more new auxiliary agent supplying means for supplying a new reaction auxiliary agent in the middle of the exhaust gas introduction duct, and use for supplying a used reaction auxiliary agent recovered from the hopper After the spent auxiliary agent supply means is connected and the supply of the new reaction auxiliary agent by the new auxiliary agent supply means is completed, the spent auxiliary reaction agent is supplied by the used auxiliary agent supply means, and the bag filter is filtered. Construct so that old and new reaction aids are attached to the cloth surface in sequence and in multiple layers. (Claim 6)
[0016]
Here, the reaction aid means, for example, a deodorizing agent, a denitrating agent, or a desulfurizing agent formed in a powder form.
[0017]
(1) According to the means (exhaust gas treatment method) according to claim 1 described in (1) above, one or more kinds of unused ones are used after the spent reaction aid is removed with pulse jet air. A new reaction aid is attached to the filter cloth surface of the bag filter, and then the spent reaction aid removed from the bag filter is attached to the outer surface of the new reaction aid in multiple layers. First, roughing reaction treatment (AC contact) can be performed, and then finishing treatment can be performed with a new reaction aid in the inner layer, and the removal efficiency is reduced by reusing the used reaction aid. Therefore, it is possible to improve the treatment effect such as deodorization and desulfurization for exhaust gas by exhibiting a stable adsorption action by the old and new reaction aids deposited in multiple layers.
[0018]
(2) According to the means (exhaust gas treatment method) according to claim 2 described in (2) above, a necessary reaction assistant is selected from a plurality of kinds of new reaction assistants, and this is filtered by a bag filter. In order to adhere multiple used reaction aids to the outer surface of the new reaction aid, the old and new reaction aids, which are deposited in multiple layers, are used for the exhaust gas. Since the treatment effect can be improved and a plurality of types of reaction aids can be used, by selecting the reaction aid to be used according to the type of exhaust gas to be treated, for example, acid gas or alkaline It makes it possible to perform a reaction process according to exhaust gas having different properties.
[0019]
(3) According to the means (exhaust gas treatment method) according to claim 3 described in the above (3), the spent reaction aid removed by the pulse jet air is swollen with air, and the blower Multiple layers can be attached to the outer surface of the new reaction aid by the suction action, so these new and old layers of reaction aid formed on the filter cloth surface of the bag filter efficiently react with the exhaust gas in a stable state. Make it possible to do.
[0020]
(4) According to the means (exhaust gas treatment method) according to claim 4 described in (4) above, the used reaction aid that has been scraped off by the pulse jet air is recovered outside the hopper, and this is collected into the blower. The new and old layers of reaction aids that are formed on the filter cloth surface of the bag filter can be attached to the outer surface of the new reaction aid by air blowing or suction. It makes it possible to react well.
[0021]
(5) According to the means (exhaust gas treatment device) according to claim 5 described in the above (5), the bag filter in which dust is removed from one or a plurality of auxiliary agent supply means connected in the middle of the exhaust gas introduction duct. One or more kinds of new reaction aids required for the surface of the reactor are sequentially supplied and adhered in multiple layers, and used reaction aids that have been scraped off to the hopper by pulse jet air Since it is lifted up by the lifting means and is deposited on the outer surface of the new reaction aid, it exhibits a stable adsorption action by the old and new layers of the reaction aid formed on the multiple layers, and the exhaust gas Can be efficiently reacted.
[0022]
(6) According to the means (exhaust gas treatment device) according to claim 6 described in (6) above, one or more kinds of required new reaction aids are added to the bag filter according to the type of exhaust gas to be treated. In addition, the used reaction aid recovered from the hopper to the used auxiliary agent supply means can be deposited on the outer surface of the new reaction aid, so that the filter of the bag filter can be filtered. These new and old layers of reaction aids formed in multiple layers on the fabric surface enable various types of exhaust gases to be efficiently reacted in a stable state.
[0023]
As described above, the technical problems described above can be solved by the means (1) to (6), and the problems of the conventional techniques can be solved.
[0024]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, an embodiment of an exhaust gas treatment method using a pulse dust removal type bag filter according to the present invention and an apparatus thereof will be described with reference to the drawings. FIG. 1 is a front view illustrating the appearance of the exhaust gas treatment apparatus of the present invention, and FIG. FIG. 3 is an enlarged side view showing the whole of the present invention. In these drawings, a reference numeral 1 indicates a bag filter type dust collector, and 1A and 1B are A clean chamber and a filter chamber of the dust collector 1 which are partitioned vertically by the partition plate 1X, 1C is a hopper connected to the lower side of the filter chamber 1B, 2... Are bag filters suspended in the filter chamber 1B.
[0025]
3 is a pulse jet blow tube provided inside the clean chamber 1A, 3T is a header pipe, 3A... Is an air jet nozzle provided in the blow tube 3, and is blown from the header pipe 3T. Pulsed jet air (compressed air) sent to the tube 3 is blown into the bag filters 2 from the nozzles 3A, so that the used reaction adhered to the filter cloth surface of the bag filters 2 ... The structure is such that the auxiliary agent can be removed to the lower hopper 1C.
[0026]
4 is a suction duct connected to the clean chamber 1A of the dust collector 1, 4A is a suction blower (suction fan) connected to the front end side of the suction duct 4, 4M is a blower drive motor, 4T is an air volume control valve, and 4B is a drainage valve. In the cylinder, the suction action of the suction blower 4A extends from the clean chamber 1A of the dust collector 1 through the suction duct 4 to the bag filter 2... And the filter chamber 1B to the exhaust gas introduction duct 7, and the exhaust gas is collected into the dust collector 1. It is structured to suck into the filter chamber 1B.
[0027]
Further, in the figure, 5 is a discharge device for the used reaction aid provided at the bottom of the hopper 1C, 5S is a discharge screw constituting the discharge device 5, and the used reaction aid discharged by the screw 5S is Then, it is sent to the flexible container 6 through the discharge valve 5A and the discharge duct 5B and collected, and then used reaction auxiliary agent supply means (supply tank) which will be described later using a transport means such as a hoist 15 attached to the guide rail 14 This is an example of implementation. For example, the spent reaction aid recovered in the hopper 1C is directly fed into the supply tank using a transport air pipe or the like. However, the selection is arbitrary.
[0028]
Further, in the figure, reference numeral 8 denotes an aeration pipe capable of sending compressed air to an air injection pipe 8A provided in the hopper 1C and soaking up a used reaction aid that has fallen into the hopper 1C and accumulated. Is an auxiliary agent supply duct whose tip is connected to the exhaust gas introduction duct 7, 10 and 11 are auxiliary agent supply tanks connected in the middle of the supply duct 9, and 10A and 11A are auxiliary agent supply valves provided in the tanks 10 and 11, respectively. , 12 is an auxiliary agent supply blower provided in the supply duct 9, and 12M is a drive motor for the reaction contained in the supply tanks 10, 11 by the functions of the blower 12 and supply valves 10A, 11A. The structure is such that the auxiliary agent can be sequentially fed into the filter chamber 1B of the dust collector 1 through the supply duct 9.
[0029]
In FIG. 1, auxiliary supply blowers 12 and 12 and supply ducts 9 and 9 are provided for each auxiliary supply tank 10 and 11, and reaction auxiliary agents are separately supplied to the exhaust gas introduction duct 7. This is an example of implementation, and as shown in the block diagram of FIG. 3, two auxiliary agent supply tanks 10 and 11 are connected to one supply duct 9, and The auxiliary apparatus supply blower 12 may supply the reaction auxiliary agents in the auxiliary agent supply tanks 10 and 11 in order, thereby simplifying the entire apparatus. To do.
[0030]
Further, the configuration diagram shown in FIG. 3 shows a configuration in which the used reaction auxiliary agent recovered in the flexible container 6 using the screw 5S is sent to the second auxiliary agent supply tank 10 and reused. This is also an example of implementation, and each of the first auxiliary agent supply tank 11, the second auxiliary agent supply tank 10, or the third auxiliary agent supply tanks of three or more, A third or other supply tank (not shown) that contains different types of new reaction aids selected according to the nature of the exhaust gas, while separately providing spent reaction aids recovered using the flexible container 6 The used reaction aid can be reused only by raising it up by air injection (aeration) from the air injection pipe 8A without using the flexible container 6 and reusing it. In At best, the selection is also optional.
[0031]
1 to 3, 1H is a support leg for supporting the dust collector 1, 1R is a support base, 1E and 1F are protective fences, and 7A is a tip portion of an exhaust gas introduction duct 7 connected to the dust collector 1. , 7X is a check valve, and 13 is the dust (reaction aid) rising from the auxiliary agent supply tanks 10 and 11 when the reaction auxiliary agent is supplied, and sucking it to the duct 7 side using the hoods 13A and 13B. It is a dust collection duct to be made.
[0032]
Since the present invention is configured as described above, the air blowing action of the auxiliary agent supply blower 12 is exerted, and further, the suction action of the suction blower 4A is applied to the exhaust gas introduction duct 7 side through the inside of the dust collector 1. When the supply valve 11A of the second auxiliary agent supply tank 11 is operated and new unused reaction auxiliary agent is sent out to the supply duct 9, this reaction auxiliary agent is sent into the filter chamber 1B of the dust collector 1 through the exhaust gas introduction duct 7. Therefore, this new reaction aid can be attached to the filter cloth surface of each bag filter 12.
[0033]
Next, when the supply valve 10A of the second auxiliary agent supply tank 10 is actuated to send out a different new reaction auxiliary agent to the supply duct 9, the reaction auxiliary agent is attached to the bag filters 2 in an air stream. It is possible to form a double layer of different unused reaction aids on the filter cloth surface of each bag filter 2... By adhering to the outer surface of the agent layer. Of course, it is not necessary to attach the reaction aid of the second auxiliary agent supply tank 10.
[0034]
Thereafter, air is injected from the air injection pipe 8A and the spent reaction aid accumulated in the hopper 1C is raised to the filter chamber 1B, or a third or other auxiliary supply tank not shown in the figure. The spent reaction aid collected in the air is placed in an air stream and sent to the filter chamber 1B, so that the layer of the spent reaction aid (third layer) is multiplexed on the outer surface of the second reaction aid. Adhesion can be formed.
[0035]
FIG. 4 is a cross-sectional view illustrating a state in which a total of three layers of the reaction assistants are formed on the filter cloth surface of the bag filter 2. In FIG. 4, 2A is the reaction aid for the first layer using, for example, zeolite. The agent layer, 2B is, for example, the second reaction assistant layer using activated coke, and 2C is the third used reaction assistant layer (for example, zeolite + active coke), which was used last time, The exhaust gas that passes through is first roughened (AC contact) by the third spent reaction aid layer 2C, and then the second new reaction aid layer 2B and the first new reaction aid layer. Contact is repeated in the order of 2A, reaction treatment such as deodorization and desulfurization is performed, and the purified gas after the reaction treatment is discharged to the clean chamber 1A side through the bag filter 2 and further through the suction duct 4 to the dust collector. It is structured to be discharged to the outside of 1.
[0036]
Each of the reaction aid layers 2A, 2B, 2C, which has been subjected to the above reaction process, is applied to the lower hopper 2C by pulse jet air blown into the bag filters 2 from the nozzles 3A of the blow tube 3 at a certain time. Then, the above-mentioned adhesion process of each reaction aid is repeated again to form multiple reaction aid layers 2A, 2B, 2C on the filter cloth surface of each bag filter 2. Resume processing operation.
[0037]
In the configuration diagram shown in FIG. 3, the used reaction aid 2C recovered using the flexible container 6 is sent to the second auxiliary agent supply tank 10 and reused. The spent reaction aid layer 2C is deposited and formed on the outer surface of the first reaction aid layer 2A formed by the new reaction aid supplied from the eye aid supply tank 11. Of course, this is an example of implementation.
[0038]
【The invention's effect】
As described above, according to the exhaust gas processing method and apparatus using the pulse dust removal type bag filter according to the present invention, an unused new reaction aid layer is first formed on the filter cloth surface of the bag filter. Since the layers of used reaction aids that have been wiped off by pulse jet air are deposited on the outside of the layers in multiple layers, these new and old reaction aid layers can be used without degrading the adsorption capacity of the reaction aids. It is possible to efficiently treat exhaust gas by using this method and to attach a plurality of different types of reaction aids to the filter cloth surface of the bag filter. Combined with the point that the used reaction aid can be effectively reused and the existing dust collector can be used as it is, it is used for deodorization and desulfurization of various exhaust gases. It is suitable for.
[Brief description of the drawings]
FIG. 1 is a front view of a dust collector embodying the present invention.
FIG. 2 is a side view of a dust collecting apparatus embodying the present invention.
FIG. 3 is a configuration diagram clearly showing the whole of the present invention.
FIG. 4 is an enlarged cross-sectional view showing a layer of reaction aids that are formed in multiple layers on the filter cloth surface of a bag filter.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Dust collector 1C Hopper 2 Bag filter 2A, 2B New reaction aid layer 2C Used reaction aid layer 3 Pulse jet air blow tube 4A Suction blower 5 Used reaction aid discharge device 7 Exhaust gas introduction duct 8A Air injection pipes 10 and 11 for raising the reaction aid supply tank 12 Auxiliary supply blower

Claims (6)

粉末状の反応助剤をパルス除塵式バグフイルタの濾布面に付着させ、ブロアーの吸引作用を受けてこのバグフイルタを通過する燃焼有害ガスや悪臭ガス等の排ガスを上記の反応助剤に接触させて反応処理する一方、上記バグフイルタの濾布面に付着している使用済みの反応助剤を、逆洗用のパルスジェットエアーで下側のホッパーに払い落すようにしたパルス除塵式バグフイルタを用いた排ガス処理方法であって、
上記使用済み反応助剤をパルスジェットエアーで払い落した後、1種類又は複数種類の新たな反応助剤を上記バグフイルタの濾布面に付着し、次いで、ホッパー内に払い落した上記使用済みの反応助剤をバグフイルタの濾布面に付着している上記新たな反応助剤の外側面に多重に付着させ、これ等多重に付着した新旧の反応助剤によって上記の排ガスを反応処理することを特徴とするパルス除塵式バグフイルタを用いた排ガス処理方法。
A powdery reaction aid is attached to the filter cloth surface of the pulse dust-removing bag filter, and the exhaust gas such as combustion harmful gas and malodorous gas that passes through the bag filter under the suction action of the blower is brought into contact with the reaction aid. Exhaust gas using a pulse dust removal type bag filter in which the spent reaction aid adhering to the filter cloth surface of the bag filter is removed to the lower hopper with pulse jet air for backwashing while the reaction treatment is performed. A processing method,
After the used reaction aid is wiped off with pulse jet air, one or more kinds of new reaction aids are attached to the filter cloth surface of the bag filter, and then used in the hopper. The reaction aid is adhered to the outer surface of the new reaction aid attached to the filter surface of the bag filter, and the exhaust gas is reacted with the old and new reaction aids attached in multiple layers. An exhaust gas treatment method using a pulse dust removal type bug filter as a feature.
使用済み反応助剤をパルスジェットエアーで下側のホッパーに払い落した後、複数種の新たな反応助剤の中から必要とする反応助剤を1種類又は複数種類選んでこれをバグフイルタの濾布面に付着し、次いで、この新たな反応助剤の外側面に上記ホッパー内に払い落した使用済みの反応助剤を多重に付着することを特徴とする請求項1記載のパルス除塵式バグフイルタを用いた排ガス処理方法。After removing the used reaction aid to the lower hopper with pulse jet air, select one or more required reaction aids from multiple types of new reaction aids and filter them through the bag filter. 2. The pulse dust removing type bag filter according to claim 1, wherein the used reaction aid that has adhered to the cloth surface and then dropped into the hopper is adhered to the outer surface of the new reaction aid. Exhaust gas treatment method using ホッパーに払い落した使用済み反応助剤をエアーで舞い上げ、これをブロアーの吸引作用を利用して新たな反応助剤の外側面に多重に付着することを特徴とする請求項1又は2記載のパルス除塵式バグフイルタを用いた排ガス処理方法。3. The spent reaction aid that has fallen to the hopper is blown up with air, and this is adhered to the outer surface of the new reaction aid in multiple using the suction action of the blower. Exhaust gas treatment method using a pulse dust removal type bag filter. ホッパーに払い落した使用済み反応助剤をホッパーの外部に回収し、この回収した使用済み反応助剤をブロアーの送風作用又は吸引作用によってバグフイルタ側に再供給して、新たな反応助剤の外側面に多重に付着することを特徴とする請求項1又は2記載のパルス除塵式バグフイルタを用いた排ガス処理方法。The spent reaction aid removed to the hopper is collected outside the hopper, and the collected spent reaction aid is re-supplied to the bag filter side by the blower blowing action or suction action to remove the new reaction aid. The exhaust gas treatment method using a pulse dust-removing bag filter according to claim 1 or 2, wherein a plurality of deposits are attached to the side surface. ブロアーの送風作用又は吸引作用を受けて排ガスの導入ダクトを通してフイルタ室内に供給又は吸引した粉末状の反応助剤を、パルス除塵式バグフイルタの濾布面に付着し、上記導入ダクトを通って吸引されて来る燃焼有害ガスや悪臭ガス等の排ガスを上記反応助剤に接触させて反応処理する一方、上記バグフイルタの濾布面に付着している使用済みの反応助剤を、逆洗用のパルスジェットエアーで逆洗して下側のホッパーに払い落すように構成したパルス除塵式バグフイルタを用いた排ガス処理装置であって、
上記排ガス導入ダクトの途中に新たな反応助剤を供給するための助剤供給手段を1台又は複数台接続し、上記のホッパーにはパルスジェットエアーによって払い落された使用済み助剤をエアーを噴射して舞い上げる助剤舞い上げ手段を設けて、上記助剤供給手段による新しい反応助剤の供給を終えた後、上記助剤舞い上げ手段による使用済み反応助剤の舞い上げを行って、上記バグフイルタの濾布面に新旧の反応助剤を順番に、且つ、多重に付着させるように構成したことを特徴とするパルス除塵式バグフイルタを用いた排ガス処理装置。
The powdery reaction aid supplied or sucked into the filter chamber through the exhaust gas introduction duct under the blower's blowing action or suction action adheres to the filter cloth surface of the pulse dust removal type bag filter and is sucked through the introduction duct. The exhaust gas such as flammable toxic gas and bad odor gas is brought into contact with the above reaction aid for reaction treatment, while the used reaction aid adhering to the filter cloth surface of the bag filter is treated with a pulse jet for backwashing. An exhaust gas treatment apparatus using a pulse dust removal type bag filter configured to be backwashed with air and wiped off to the lower hopper,
One or a plurality of auxiliary agent supply means for supplying a new reaction auxiliary agent are connected in the middle of the exhaust gas introduction duct, and the used auxiliary agent removed by pulse jet air is supplied to the hopper with air. Auxiliary uplifting means is provided for jetting up, and after the supply of the new reaction auxiliary by the auxiliary supply means is completed, the spent reaction auxiliary is raised up by the auxiliary uplifting means, An exhaust gas treatment apparatus using a pulse dust removal type bag filter, characterized in that the old and new reaction aids are sequentially and multiply attached to the filter cloth surface of the bag filter.
ブロアーの送風作用又は吸引作用を受けて排ガスの導入ダクトを通してフイルタ室内に供給又は吸引した粉末状の反応助剤を、パルス除塵式バグフイルタの濾布面に付着し、上記導入ダクトを通って吸引されて来る燃焼有害ガスや悪臭ガス等の排ガスを上記反応助剤に接触させて反応処理する一方、上記バグフイルタの濾布面に付着している使用済みの反応助剤を、逆洗用のパルスジェットエアーで逆洗して下側のホッパーに払い落すように構成したパルス除塵式バグフイルタを用いた排ガス処理装置であって、
上記排ガス導入ダクトの途中に、新たな反応助剤を供給するための1台又は複数台の新規助剤供給手段と、上記ホッパーから回収した使用済み反応助剤を供給するための使用済み助剤供給手段を接続し、上記新規助剤供給手段による新しい反応助剤の供給を終えた後、上記使用済み助剤供給手段による使用済み反応助剤の供給を行って、上記バグフイルタの濾布面に新旧の反応助剤を順番に、且つ、多重に付着させるように構成したことを特徴とするパルス除塵式バグフイルタを用いた排ガス処理装置。
The powdery reaction aid supplied or sucked into the filter chamber through the exhaust gas introduction duct under the blower's blowing action or suction action adheres to the filter cloth surface of the pulse dust removal type bag filter and is sucked through the introduction duct. The exhaust gas such as flammable toxic gas and bad odor gas is brought into contact with the above reaction aid for reaction treatment, while the used reaction aid adhering to the filter cloth surface of the bag filter is treated with a pulse jet for backwashing. An exhaust gas treatment apparatus using a pulse dust removal type bag filter configured to be backwashed with air and wiped off to the lower hopper,
One or more new auxiliary agent supplying means for supplying a new reaction auxiliary agent in the middle of the exhaust gas introduction duct, and a used auxiliary agent for supplying the used reaction auxiliary agent recovered from the hopper After the supply means is connected and the supply of the new reaction auxiliary by the new auxiliary agent supply means is completed, the used reaction auxiliary agent is supplied by the used auxiliary agent supply means, and the bag filter is applied to the filter cloth surface. An exhaust gas treatment apparatus using a pulse dust removal type bag filter, characterized in that old and new reaction aids are sequentially and multiply attached.
JP18270099A 1999-06-29 1999-06-29 Exhaust gas treatment method and apparatus using pulse dust removal type bag filter Expired - Fee Related JP3641393B2 (en)

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