JP3498523B2 - Exhaust gas treatment equipment - Google Patents

Exhaust gas treatment equipment

Info

Publication number
JP3498523B2
JP3498523B2 JP06283997A JP6283997A JP3498523B2 JP 3498523 B2 JP3498523 B2 JP 3498523B2 JP 06283997 A JP06283997 A JP 06283997A JP 6283997 A JP6283997 A JP 6283997A JP 3498523 B2 JP3498523 B2 JP 3498523B2
Authority
JP
Japan
Prior art keywords
exhaust gas
dust collector
switching damper
combustion oxidizer
gas
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
JP06283997A
Other languages
Japanese (ja)
Other versions
JPH10249162A (en
Inventor
光一 後夷
伸介 飯島
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.)
Sintokogio Ltd
Original Assignee
Sintokogio Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Sintokogio Ltd filed Critical Sintokogio Ltd
Priority to JP06283997A priority Critical patent/JP3498523B2/en
Publication of JPH10249162A publication Critical patent/JPH10249162A/en
Application granted granted Critical
Publication of JP3498523B2 publication Critical patent/JP3498523B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Filtering Of Dispersed Particles In Gases (AREA)
  • Exhaust Gas Treatment By Means Of Catalyst (AREA)

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明はガス中に粉塵、水
分、有害な揮発性有機化合物や悪臭成分などが混在して
いる排ガスを浄化処理する装置であって、粒状触媒固定
層式の燃焼酸化装置の粒状触媒固定層の再生処理を簡単
に行うことができる排ガスの処理装置に関するものであ
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for purifying an exhaust gas in which dust, water, harmful volatile organic compounds, malodorous components, etc. are mixed in a gas, and a granular catalyst fixed bed type combustion oxidation is used. The present invention relates to an exhaust gas treatment device capable of easily performing a regeneration treatment of a granular catalyst fixed bed of the device.

【0002】[0002]

【従来の技術】例えば、鋳造工程のような種々の製造プ
ロセスにおいて発生する排ガス中には、各種の粉塵や水
分あるいは有害な揮発性有機化合物や悪臭成分などが混
在している場合が多く、前記の粉塵を浄化処理するため
の集塵機に併用して、揮発性有機化合物や悪臭成分など
の浄化処理用に粒状触媒固定層式の燃焼酸化装置を用い
るのが普通である。
2. Description of the Related Art For example, exhaust gas generated in various manufacturing processes such as a casting process often contains various kinds of dust, water, harmful volatile organic compounds, malodorous components, etc. It is common to use a granular catalyst fixed bed type combustion oxidizer for purification treatment of volatile organic compounds and malodorous components in combination with a dust collector for purification treatment of the above dust.

【0003】ところが、前記粒状触媒固定層式の燃焼酸
化装置を長時間継続して運転していると、粒状触媒の表
面にガス中のシリカ化合物等の触媒毒が堆積して触媒性
能が劣化するため定期的に触媒交換作業を行う必要があ
り、長時間の継続運転ができないとともに処理効率が低
下するという問題点があった。一方、上記のような触媒
毒の堆積を防止する方法として燃焼酸化装置の燃焼温度
を通常の300℃程度から500℃程度まで上げること
により触媒性能の劣化を遅らせることも考えられるが、
この場合には設備費およびランニングコストが高くなり
実用的でないものであった。
However, if the particulate catalyst fixed bed type combustion oxidizer is continuously operated for a long time, catalyst poisons such as silica compounds in the gas are deposited on the surface of the particulate catalyst to deteriorate the catalytic performance. Therefore, there is a problem that it is necessary to perform the catalyst replacement work regularly, and continuous operation for a long time cannot be performed and the processing efficiency is lowered. On the other hand, as a method of preventing the accumulation of the catalyst poison as described above, it is considered that the deterioration of the catalyst performance is delayed by raising the combustion temperature of the combustion oxidation device from the normal temperature of about 300 ° C to about 500 ° C.
In this case, the equipment cost and running cost are high, which is not practical.

【0004】[0004]

【発明が解決しようとする課題】本発明は上記のような
従来の問題点を解決して、粉塵、水分、有害な揮発性有
機化合物や悪臭成分などが混在した排ガスを長時間にわ
たり効率的に浄化処理することができ、また粒状触媒固
定層式の燃焼酸化装置の粒状触媒固定層の再生処理も簡
単に行うことができる排ガスの処理装置を提供すること
を目的として完成されたものである。
DISCLOSURE OF THE INVENTION The present invention solves the above-mentioned conventional problems and efficiently discharges exhaust gas containing dust, water, harmful volatile organic compounds, malodorous components, etc. for a long time. The present invention has been completed with the object of providing an exhaust gas treatment apparatus that can be purified and can easily perform a regeneration treatment of a granular catalyst fixed bed of a granular catalyst fixed bed type combustion oxidation device.

【0005】[0005]

【課題を解決するための手段】上記の課題を解決するた
めになされた本発明の排ガスの処理装置は、排ガス中の
粉塵を集塵除去する集塵機と、排ガス中の有害揮発成分
や悪臭成分を燃焼除去する粒状触媒固定層式の燃焼酸化
装置とを連結した排ガスの処理装置において、燃焼酸化
装置と集塵機との間に送風機や風量調節ダンパからなる
風量調整手段を設け、また前記燃焼酸化装置の出口と集
塵機の入口を結ぶフィードバック用のガス循環路を設け
るとともに、該ガス循環路には前記の粒状触媒固定層を
流動化して再生処理する閉ループ構成用の切替ダンパ手
段を設けたことを特徴とするものである。
The exhaust gas treating apparatus of the present invention made to solve the above-mentioned problems includes a dust collector for collecting and removing dust in the exhaust gas, and a harmful volatile component and an offensive odor component in the exhaust gas. In the exhaust gas treatment system that is connected to a granular catalyst fixed bed combustion oxidation system that removes by combustion,
It consists of a blower and an air volume adjustment damper between the device and the dust collector.
A closed loop structure is provided in which an air flow rate adjusting means is provided, and a feedback gas circulation path connecting the outlet of the combustion oxidizer and the dust collector is provided, and the particulate catalyst fixed bed is fluidized and regenerated in the gas circulation path. It is characterized in that a switching damper means for use is provided.

【0006】[0006]

【発明の実施の形態】以下に、図面を参照しつつ本発明
の好ましい実施の形態を示す。図面は、鋳造工場におけ
る鋳込み後の鋳物と生砂の分離時に発生する湿潤排ガス
を浄化する場合を示すものであって、図中1は粉塵、水
分、有害な揮発性有機化合物や悪臭成分などが混在して
いる排ガスの発生源10を覆う吸引フード、2は排ガス
中の粉塵を集塵除去するためのバグフィルタ式の集塵
機、3は送風機、4は排ガス中の有害揮発成分や悪臭成
分を燃焼除去するための粒状触媒固定層式の燃焼酸化装
置であり、以上の構成は従来のこの種の排ガスの処理装
置と基本的に同じである。
BEST MODE FOR CARRYING OUT THE INVENTION Preferred embodiments of the present invention will be described below with reference to the drawings. The drawing shows the case of purifying the moist exhaust gas generated at the time of separating the casting and the raw sand after the casting in the foundry, and 1 in the figure shows dust, water, harmful volatile organic compounds and malodorous components. A suction hood covering the mixed exhaust gas generation source 10, 2 is a bag filter type dust collector for collecting and removing dust in the exhaust gas, 3 is a blower, and 4 is a burner for harmful volatile components and malodorous components in the exhaust gas. This is a granular catalyst fixed bed combustion oxidizer for removal, and the above configuration is basically the same as a conventional exhaust gas treating apparatus of this type.

【0007】そして、本発明においては前記燃焼酸化装
置4の出口と集塵機2の入口を結ぶフィードバック用の
ガス循環路5を設けるとともに、該ガス循環路5には前
記の粒状触媒固定層4aを流動化して再生処理する閉ル
ープ構成用の切替ダンパ手段を設けた点に特徴的構成を
有する。即ち、通常は排ガスを集塵機2および粒状触媒
固定層式の燃焼酸化装置4により浄化処理して粉塵、有
害な揮発性有機化合物や悪臭成分などを除去している
が、長時間の継続運転により前記粒状触媒固定層4aの
触媒劣化が生じた場合には切替ダンパ手段の操作によっ
て燃焼酸化装置4の出口と集塵機2の入口を結ぶフィー
ドバック用のガス循環路5を形成し、この閉ループ状態
に構成されたガス循環路5内でガスを循環させることに
より粒状触媒固定層4aを流動化し、触媒表面に堆積し
た触媒毒を払落して再生するのである。
In the present invention, a gas circulation path 5 for feedback connecting the outlet of the combustion oxidizer 4 and the inlet of the dust collector 2 is provided, and the particulate catalyst fixed layer 4a flows through the gas circulation path 5. It has a characteristic configuration in that a switching damper means for a closed loop configuration for converting into a reproduction process is provided. That is, normally, the exhaust gas is purified by the dust collector 2 and the granular catalyst fixed bed type combustion oxidizer 4 to remove dust, harmful volatile organic compounds, malodorous components, etc. When the catalyst deterioration of the granular catalyst fixed layer 4a occurs, a feedback gas circulation path 5 connecting the outlet of the combustion oxidizer 4 and the inlet of the dust collector 2 is formed by operating the switching damper means, and this closed loop state is formed. By circulating the gas in the gas circulation path 5, the granular catalyst fixed layer 4a is fluidized, and the catalyst poison accumulated on the catalyst surface is removed and regenerated.

【0008】前記の閉ループ構成用の切替ダンパ手段
は、集塵機2への排ガスの吸引を開閉する切替ダンパ7
aと、ガス循環路5の集塵機2への連通を開閉する切替
ダンパ7bと、燃焼酸化装置4の処理ガスの放出を開閉
する切替ダンパ7cから構成されるものであり、通常の
浄化処理時は切替ダンパ7a、7cを開いて切替ダンパ
7bを閉じた状態とし、一方、粒状触媒固定層4aを流
動化して再生処理する時には切替ダンパ7bを開いて切
替ダンパ7a、7cを閉じた状態とすればよい。
The switching damper means for the closed loop construction is a switching damper 7 for opening and closing the suction of the exhaust gas to the dust collector 2.
a, a switching damper 7b that opens and closes the communication of the gas circulation path 5 to the dust collector 2, and a switching damper 7c that opens and closes the discharge of the processing gas of the combustion oxidizer 4 and are used during normal purification processing. When the switching dampers 7a and 7c are opened and the switching damper 7b is closed, on the other hand, when the granular catalyst fixed layer 4a is fluidized and regenerated, the switching damper 7b is opened and the switching dampers 7a and 7c are closed. Good.

【0009】また、前記の集塵機2と燃焼酸化装置4と
の間に設けられている送風機3には風量調節ダンパ8か
らなる風量調整手段が付加されており、通常の運転時と
粒状触媒固定層4aの再生処理時のガス流量を最適のも
のに調整できるよう構成されている。ちなみに、図示の
装置においては再生処理時のガス流量は、通常の運転時
のガス流量に対し約1.2〜1.5倍程度となるよう設
定して稼働した。なお、前記の風量調整手段としては例
えばインバータ制御による送風機3の回転数を調整する
機構とすることもできる。また、前記粒状触媒固定層式
の燃焼酸化装置4には熱交換器6が内蔵されたものとな
っており、燃焼酸化装置4の効率的な稼働が可能となる
よう構成されている。
Further, the blower 3 provided between the dust collector 2 and the combustion oxidizer 4 is provided with an air volume adjusting means consisting of an air volume adjusting damper 8 for the normal operation and the granular catalyst fixed bed. It is configured so that the gas flow rate during the regeneration treatment of 4a can be adjusted to an optimum value. By the way, in the illustrated apparatus, the gas flow rate during the regeneration process was set to be about 1.2 to 1.5 times the gas flow rate during normal operation and operated. The air volume adjusting means may be, for example, a mechanism for adjusting the rotation speed of the blower 3 under inverter control. A heat exchanger 6 is built in the granular catalyst fixed bed type combustion oxidizer 4 so that the combustion oxidizer 4 can be operated efficiently.

【0010】このように構成したものは、発生源10で
発生したレアガスを吸引フード1で集めて集塵機2に導
入し排ガス中の粉塵を集塵除去した後、燃焼酸化装置4
に導入しここで熱交換器6により昇温した後、有害揮発
成分や悪臭成分を燃焼除去して浄化処理を行うものであ
る点は従来のこの種の排ガスの処理装置と基本的に同じ
である。そして、長時間にわたり継続運転して粒状触媒
の表面にガス中のシリカ化合物等の不活性な触媒毒が堆
積し触媒性能が劣化してきた場合には、切替ダンパ7b
を開くとともに切替ダンパ7a、7cを閉じた状態とし
てガス循環路5を利用した閉ループを構成し、更にガス
流量を約1.2〜1.5倍程度に上げて稼働することに
より粒状触媒固定層4aを流動化して触媒の再生処理を
行うものである。即ち、この再生処理により粒状触媒の
表面を覆っている不活性層は、図2に示されるように、
粒状触媒どうしの衝突・摩耗によって剥離され再び表面
が活性化されることになるのである。またこの時、剥離
した不活性層はガス循環路5を通じて集塵機2に導入さ
れ除去処理されるので大気中に放出されることもなく、
大気汚染の心配も全くないものである。このようにして
粒状触媒の再生処理が終了した後は、再び切替ダンパ7
a、7cを開くとともに切替ダンパ7bを閉じた状態と
して通常の運転を再開すれば、排ガス中の粉塵の集塵除
去処理および有害揮発成分や悪臭成分の燃焼除去処理が
再び再開され、以上の操作の繰り返しにより長時間にわ
たって排ガスの浄化処理を継続運転できることとなる。
With such a structure, the rare gas generated in the generation source 10 is collected by the suction hood 1 and introduced into the dust collector 2 to remove dust in the exhaust gas, and then the combustion oxidizer 4 is used.
It is basically the same as the conventional exhaust gas treating apparatus of this type in that the volatile component and the odorous component are burned and removed to perform the purification treatment after the temperature is introduced into the heat exchanger 6 and the temperature is raised by the heat exchanger 6. is there. If the catalyst performance deteriorates due to inactive catalyst poisons such as silica compounds in the gas accumulated on the surface of the granular catalyst after continuous operation for a long time, the switching damper 7b
And a switching damper 7a, 7c is closed to form a closed loop using the gas circulation path 5, and further the gas flow rate is increased by about 1.2 to 1.5 times to operate the granular catalyst fixed bed. 4a is fluidized and the catalyst is regenerated. That is, the inactive layer covering the surface of the granular catalyst by this regeneration treatment is, as shown in FIG.
Due to the collision and abrasion of the granular catalysts, they are separated and the surface is activated again. Further, at this time, the separated inactive layer is introduced into the dust collector 2 through the gas circulation path 5 and is removed, so that it is not released into the atmosphere.
There is no concern about air pollution. After the regeneration process of the granular catalyst is completed in this way, the switching damper 7 is again activated.
When a and 7c are opened and the switching damper 7b is closed and normal operation is resumed, the dust collection removal processing of dust in the exhaust gas and the combustion removal processing of harmful volatile components and malodorous components are restarted again. By repeating the above, the exhaust gas purification process can be continuously operated for a long time.

【0011】[0011]

【発明の効果】以上の説明からも明らかなように、本発
明は粉塵、水分、有害な揮発性有機化合物や悪臭成分な
どが混在した排ガスを長時間にわたり効率的に浄化処理
することができ、また粒状触媒固定層式の燃焼酸化装置
の粒状触媒固定層の再生処理も簡単に行うことができる
ものであり、この結果、従来のように定期的な触媒交換
作業を行う必要もなく大幅な作業効率の向上を図ること
ができるとともに、大幅な設備費の低廉化とランニング
コストの低下を達成することができるものである。更に
は、従来の装置に対しフィードバック用のガス循環路と
閉ループ構成用の切替ダンパを付加するのみで改良で
き、設備費の少ない低コストのシステムを提供すること
ができるという利点も有する。よって本発明は従来の問
題点を一掃した排ガスの処理装置として、産業の発展に
寄与するところは極めて大である。
As is apparent from the above description, the present invention can efficiently purify exhaust gas containing dust, water, harmful volatile organic compounds, malodorous components, etc. for a long time, In addition, it is possible to easily regenerate the granular catalyst fixed bed of the granular catalyst fixed bed type combustion oxidizer, and as a result, it is not necessary to perform regular catalyst replacement work as in the past, and it is a large work. In addition to being able to improve efficiency, it is possible to significantly reduce equipment costs and running costs. Further, it has an advantage that it can be improved by only adding a gas circulation path for feedback and a switching damper for a closed loop configuration to the conventional apparatus, and a low cost system with low equipment cost can be provided. Therefore, the present invention, as an exhaust gas treatment apparatus that eliminates the conventional problems, is extremely important in contributing to industrial development.

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

【図1】本発明の実施の形態を示す全体概略図である。FIG. 1 is an overall schematic diagram showing an embodiment of the present invention.

【図2】粒状触媒固定層に流動化処理を施した場合を示
す説明図である。
FIG. 2 is an explanatory view showing a case where a granular catalyst fixed bed is subjected to a fluidization treatment.

【符号の説明】[Explanation of symbols]

2 集塵機 4 燃焼酸化装置 4a 粒状触媒固定層 5 ガス循環路 6 熱交換器 7a 切替ダンパ 7b 切替ダンパ 7c 切替ダンパ 8 風量調節ダンパ 2 dust collector 4 Combustion oxidizer 4a Granular catalyst fixed bed 5 gas circulation 6 heat exchanger 7a switch damper 7b switching damper 7c switching damper 8 Air volume adjustment damper

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 平8−112515(JP,A) (58)調査した分野(Int.Cl.7,DB名) B01D 53/86 ─────────────────────────────────────────────────── ─── Continuation of the front page (56) Reference JP-A-8-112515 (JP, A) (58) Fields investigated (Int.Cl. 7 , DB name) B01D 53/86

Claims (3)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 排ガス中の粉塵を集塵除去する集塵機
(2)と、排ガス中の有害揮発成分や悪臭成分を燃焼除
去する粒状触媒固定層式の燃焼酸化装置(4)とを連結
した排ガスの処理装置において、燃焼酸化装置(4)と
集塵機(2)との間に送風機(3)や風量調節ダンパ
(8)からなる風量調整手段を設け、また前記燃焼酸化
装置(4)の出口と集塵機(2)の入口を結ぶフィード
バック用のガス循環路(5)を設けるとともに、該ガス
循環路(5)には前記の粒状触媒固定層(4a)を流動
化して再生処理する閉ループ構成用の切替ダンパ手段を
設けたことを特徴とする排ガスの処理装置。
1. Exhaust gas in which a dust collector (2) for collecting and removing dust in exhaust gas and a granular catalyst fixed bed type combustion oxidizer (4) for burning and removing harmful volatile components and malodorous components in exhaust gas are connected. in the processing apparatus, the combustion oxidizer (4)
A blower (3) and an air volume adjustment damper between the dust collector (2)
(8) An air volume adjusting means is provided, and a feedback gas circulation path (5) connecting the outlet of the combustion oxidizer (4) and the inlet of the dust collector (2) is provided, and the gas circulation path (5) is also provided. The exhaust gas treating apparatus is characterized in that it is provided with a switching damper means of a closed loop configuration for fluidizing and regenerating the granular catalyst fixed layer (4a).
【請求項2】 切替ダンパ手段は集塵機(2)への排ガ
スの吸引を開閉する切替ダンパ(7a)と、ガス循環路
(5)の集塵機(2)への連通を開閉する切替ダンパ
(7b)と、燃焼酸化装置(4)の処理ガスの放出を開
閉する切替ダンパ(7c)からなるものである請求項1
に記載の排ガスの処理装置。
2. The switching damper means includes a switching damper (7a) that opens and closes suction of exhaust gas to the dust collector (2) and a switching damper (7b) that opens and closes communication of the gas circulation path (5) to the dust collector (2). And a switching damper (7c) for opening and closing the discharge of the processing gas from the combustion oxidizer (4).
The exhaust gas treatment device according to item 1.
【請求項3】 粒状触媒固定層式の燃焼酸化装置(4)
には熱交換器(6)が内蔵されている請求項1または2
に記載の排ガスの処理装置。
3. A granular bed fixed bed combustion oxidizer (4).
A heat exchanger (6) is built in the said 1 or 2.
The exhaust gas treatment device according to item 1.
JP06283997A 1997-03-17 1997-03-17 Exhaust gas treatment equipment Expired - Fee Related JP3498523B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP06283997A JP3498523B2 (en) 1997-03-17 1997-03-17 Exhaust gas treatment equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP06283997A JP3498523B2 (en) 1997-03-17 1997-03-17 Exhaust gas treatment equipment

Publications (2)

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JPH10249162A JPH10249162A (en) 1998-09-22
JP3498523B2 true JP3498523B2 (en) 2004-02-16

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