JPH0914633A - Gas treating device - Google Patents

Gas treating device

Info

Publication number
JPH0914633A
JPH0914633A JP7157351A JP15735195A JPH0914633A JP H0914633 A JPH0914633 A JP H0914633A JP 7157351 A JP7157351 A JP 7157351A JP 15735195 A JP15735195 A JP 15735195A JP H0914633 A JPH0914633 A JP H0914633A
Authority
JP
Japan
Prior art keywords
activated carbon
gas
regenerated
deteriorated
layer
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP7157351A
Other languages
Japanese (ja)
Inventor
Masayuki Yuguchi
昌幸 湯口
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.)
Kubota Corp
Original Assignee
Kubota Corp
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 Kubota Corp filed Critical Kubota Corp
Priority to JP7157351A priority Critical patent/JPH0914633A/en
Publication of JPH0914633A publication Critical patent/JPH0914633A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE: To obtain a gas treating device, capable of effecting physical filtering treatment of soot, dust and the like from exhaust gas and capable of effecting adsorption treatment through active carbon efficiently, and capable of minimizing the amount of consumption of active carbon as far as possible. CONSTITUTION: A gas treating device is provided with filtrating fabric layers 9 and active carbon layers 10, arranged along the flow direction of objective gas for treating, an extracting mechanism 3 for extracting active carbon, whose adsorbing capacity is deteriorated, from the active carbon layers 10, an active carbon regenerating mechanism 4, regenerating deteriorated active carbon through mechanical treatment for exposing new adsorbing areas on the extracted deteriorated active carbon, and a mixing mechanism 7, mixing the powder of active carbon, which is generated by the mechanical treatment in the active carbon regenerating mechanism 4 into the objective gas of treatment in the upstream side of filtrating fabric layers 9.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は、例えば都市ガス焼却炉
から発生する排ガスより、これに含まれるばいじん、低
沸点金属、酸性ガス中和用の中和剤、さらには、微量重
金属等を除去して浄化するガス処理装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention removes soot and dust, low boiling point metals, neutralizing agents for neutralizing acidic gases, and trace amounts of heavy metals contained in exhaust gas generated from, for example, city gas incinerators. The present invention relates to a gas treatment device for purifying.

【0002】[0002]

【従来の技術】上記のような目的で使用されるガス処理
装置としては、バグフィルタさらには、活性炭吸着装置
が知られている。バグフィルタは、バグと呼ばれる濾布
を備えた濾過具を備えたものであり、この濾布の表裏面
間に渡って処理対象ガスを流通することにより、濾布表
面に固形物を捕らえて、ガスの浄化を行う。一方、活性
炭吸着装置は、活性炭により所定の除去物を吸着させて
ガスの浄化をおこなう。従来、これらの装置は互いに独
立な装置として構成されていた。
2. Description of the Related Art Bag filters and activated carbon adsorption devices are known as gas treatment devices used for the above purposes. The bag filter is provided with a filter tool having a filter cloth called a bag, and by passing the gas to be treated across the front and back surfaces of the filter cloth, a solid matter is captured on the surface of the filter cloth, Purify gas. On the other hand, the activated carbon adsorption device adsorbs a predetermined removed substance by activated carbon to purify the gas. Conventionally, these devices have been configured as devices independent of each other.

【0003】[0003]

【発明が解決しようとする課題】しかしながら、これら
の装置を互いに独立に設置すると、それらの専有空間が
大きく、さらに、各々の装置に対する、設備系、制御系
等が複雑になるという問題があった。従って、これらの
問題を解決するために、処理対象ガスの流れ方向に沿っ
て、濾布層と活性炭層とを設けて、単一のガス処理装置
内でガスを処理しようとする試みが成されている。ここ
で、活性炭層に配される活性炭は、その吸着部位に被吸
着物を経時的に吸着するため、劣化し、その吸着能が劣
ることとなる。従って、従来は、劣化した活性炭を取り
出して、新たな活性炭を補給していた。しかしながら、
このような装置の運転形態を採用すると、活性炭の消費
率が比較的高いとともに、微量重金属の除去が充分でな
く、装置の安定的な運転上、改良の余地がある。さら
に、酸性ガスの処理を目的として、バグフィルタの上流
側に中和剤混入装置が備えられるが、この中和剤混入装
置とバグフィルタさらには、活性炭吸着装置の組み合わ
せにおいても、その中和剤の消費量が多く、この点から
も改良の余地があった。従って、本発明の目的は上記の
問題を解決することにある。
However, if these devices are installed independently of each other, there is a problem that the space occupied by them is large and the equipment system, control system, etc. for each device are complicated. . Therefore, in order to solve these problems, an attempt has been made to treat the gas in a single gas treatment device by providing a filter cloth layer and an activated carbon layer along the flow direction of the gas to be treated. ing. Here, the activated carbon arranged in the activated carbon layer is deteriorated because it adsorbs the adsorbed substance to its adsorption site over time, and its adsorption ability is deteriorated. Therefore, conventionally, the deteriorated activated carbon has been taken out and replenished with new activated carbon. However,
If such an operating mode of the apparatus is adopted, the consumption rate of activated carbon is relatively high and the removal of a trace amount of heavy metals is not sufficient, and there is room for improvement in terms of stable operation of the apparatus. Further, a neutralizing agent mixing device is provided on the upstream side of the bag filter for the purpose of treating the acidic gas. Even in the combination of the neutralizing agent mixing device, the bag filter, and the activated carbon adsorbing device, the neutralizing agent mixing device is used. There was room for improvement from this point as well. Therefore, an object of the present invention is to solve the above problems.

【0004】[0004]

【課題を解決するための手段】この目的を達成するため
の本発明によるガス処理装置の第1の特徴構成は、ガス
処理装置が、処理対象ガスの流れ方向に沿って濾布層と
活性炭層とを備え、前記活性炭層より吸着能が低下した
劣化活性炭を抜き出す抜き出し機構を備え、抜き出され
た前記劣化活性炭に新たな吸着面を露出させる機械的処
理を行って前記劣化活性炭を再生する活性炭再生機構を
備えるとともに、前記活性炭再生機構に於ける機械的処
理により発生する活性炭粉末を、前記濾布層の上流側で
前記処理対象ガス内に混入する混入機構を備えて構成さ
れることにある(請求項1に係わる)。さらに、前述の
本願第1の特徴構成において、前記活性炭再生機構と前
記混入機構との間に、前記活性炭再生機構で再生された
再生活性炭を分粒する分粒機構を備え、細粒側の前記再
生活性炭を前記混入機構に供給し、粗粒側の前記再生活
性炭を前記活性炭層に戻す分配循環機構を備えることが
好ましい。これが、請求項2に係わる本願第2の特徴構
成である。さらに、本願第2の特徴構成において、前記
混入機構に導かれる前記活性炭粉末もしくは前記細粒側
の再生活性炭の粒度を調節する粒度調整機構を備えるこ
とが好ましい。これが、請求項3に係わる本願第3の特
徴構成である。さらに、上記の目的を達成するための本
発明によるガス処理装置の第4の特徴構成は、処理対象
ガスの流れ方向に沿って濾布層と活性炭層とを備え、前
記活性炭層より吸着能が低下した劣化活性炭を抜き出す
抜き出し機構を備え、抜き出された前記劣化活性炭に新
たな吸着面を露出させる機械的処理を行って、粒度調整
された粉末状再生活性炭を得る粉末再生処理機構を備え
るとともに、前記粉末再生処理機構により得られる前記
粉末状再生活性炭を、前記濾布層の上流側で前記処理対
象ガス内に混入する混入機構を備えたことにある。これ
が、請求項4に係わる。そして、それらの作用・効果は
次の通りである。
The first characteristic constitution of the gas treatment apparatus according to the present invention for attaining this object is that the gas treatment apparatus comprises a filter cloth layer and an activated carbon layer along the flow direction of the gas to be treated. And an extraction mechanism for extracting deteriorated activated carbon having a reduced adsorption capacity from the activated carbon layer, and activated carbon that regenerates the deteriorated activated carbon by performing a mechanical treatment to expose a new adsorption surface to the extracted deteriorated activated carbon. It is configured to include a regenerating mechanism and a mixing mechanism that mixes the activated carbon powder generated by the mechanical treatment in the activated carbon regenerating mechanism into the gas to be treated on the upstream side of the filter cloth layer. (According to claim 1). Further, in the above-mentioned first characteristic configuration of the present application, a sizing mechanism for sizing the regenerated activated carbon regenerated by the activated carbon regenerating mechanism is provided between the activated carbon regenerating mechanism and the mixing mechanism, It is preferable to provide a distribution circulation mechanism for supplying regenerated activated carbon to the mixing mechanism and returning the regenerated activated carbon on the coarse grain side to the activated carbon layer. This is the second characteristic configuration of the present application according to claim 2. Further, in the second characteristic configuration of the present application, it is preferable to include a particle size adjusting mechanism for adjusting the particle size of the activated carbon powder or the regenerated activated carbon on the fine particle side, which is guided to the mixing mechanism. This is the third characteristic configuration of the present application according to claim 3. Furthermore, a fourth characteristic configuration of the gas treatment apparatus according to the present invention for achieving the above object is provided with a filter cloth layer and an activated carbon layer along the flow direction of the gas to be treated, and the adsorption capacity of the activated carbon layer is higher than that of the activated carbon layer. With a mechanism for extracting the deteriorated activated carbon that has deteriorated, a mechanical treatment for exposing a new adsorption surface to the extracted deteriorated activated carbon, and a powder regeneration treatment mechanism for obtaining a powdery regenerated activated carbon with a particle size adjusted. A mixing mechanism for mixing the regenerated activated carbon powder obtained by the powder regeneration treatment mechanism into the gas to be treated on the upstream side of the filter cloth layer is provided. This relates to claim 4. The actions and effects thereof are as follows.

【0005】[0005]

【作用】本願第1の特徴構成を備えたガス処理装置にお
いては、活性炭層から抜き出し機構により吸着能が低下
した劣化活性炭が抜き出される。そして、抜き出された
劣化活性炭は活性炭再生機構により、機械的処理を受け
新たな吸着面を露出されて再生される。例えば、劣化活
性炭は粉砕処理されたり、被吸着物が多く吸着されてい
る表面層が取り除かれて、活性炭に新たな吸着活性面が
露出されるのである。このような機械的な再生操作をお
こなうと、その操作に伴って活性炭粉末が発生する。そ
こで、本願の装置にあっては、発生した活性炭粉末が混
入機構により、濾布層の上流側で処理対象ガス内に送り
込まれる。これは、装置に備えられる濾布層の表面に活
性炭のコーティング層を形成する。従来構成のように、
濾布層の上流側に中和剤の混入装置を備える場合は、こ
のコーティング層は、活性炭と中和剤とが混ざったもの
となる。ここで、混入される活性炭粉末は、新たな吸着
能を発揮するため、これを有効利用でき、活性炭の消費
量を全体として低減化できるとともに、微量重金属等の
除去効率を上昇することができ、結果的に、ガス浄化を
安定しておこなうことができる。さらに、このような濾
布層を備えたガス処理装置にあっては、濾布表面に所定
量の被濾過物が体積した状態で、例えば逆洗操作によ
り、体積物が濾布表面から除去され、再生状態での作動
をすることとなる。従って、濾布の再生を容易に行える
とともに、溶融等の後処理に回される被濾過物内に燃焼
源である炭素が比較的多く含有されるため、被濾過物で
あるばいじんの溶融時の熱源として利用することができ
る。
In the gas treatment apparatus having the first characteristic configuration of the present application, the deteriorated activated carbon having a reduced adsorption capacity is extracted from the activated carbon layer by the extraction mechanism. Then, the deteriorated activated carbon extracted is subjected to a mechanical treatment by the activated carbon regenerating mechanism so that a new adsorption surface is exposed and regenerated. For example, the deteriorated activated carbon is pulverized, or the surface layer on which a large amount of the substance to be adsorbed is adsorbed is removed to expose a new adsorption active surface to the activated carbon. When such a mechanical regeneration operation is performed, activated carbon powder is generated along with the operation. Therefore, in the apparatus of the present application, the generated activated carbon powder is fed into the gas to be treated on the upstream side of the filter cloth layer by the mixing mechanism. This forms a coating layer of activated carbon on the surface of the filter cloth layer provided in the device. Like the conventional configuration,
When the neutralizing agent mixing device is provided on the upstream side of the filter cloth layer, the coating layer is a mixture of activated carbon and the neutralizing agent. Here, since the activated carbon powder to be mixed exhibits a new adsorption ability, it can be effectively used, the consumption of activated carbon can be reduced as a whole, and the removal efficiency of a trace amount of heavy metals can be increased, As a result, gas purification can be performed stably. Further, in the gas treatment device provided with such a filter cloth layer, the volume is removed from the filter cloth surface by, for example, backwashing operation with a predetermined amount of the object to be filtered on the filter cloth surface. , It will operate in the regenerated state. Therefore, the filter cloth can be easily regenerated, and a relatively large amount of carbon, which is a combustion source, is contained in the substance to be filtered which is passed to the post-treatment such as melting. It can be used as a heat source.

【0006】本願第2の特徴構成を備えたガス処理装置
においては、活性炭再生機構から再生されて出てくる再
生活性炭が分粒機構により、分粒される。そして、分粒
された再生再生炭のうち、細粒側のものが混入機構に、
粗粒側のものが再度活性炭層内に送り帰される。この働
きを、分配循環機構が受け持つ。従って、この構成にあ
っては、濾布表面には、活性炭粉末と細粒側の活性炭が
濾布表面上においてコーティング層を形成して、上記と
同様な働きをおこなう。さらに、粗粒側の再生活性炭
は、再度、活性炭層に戻されて、活性炭本来の主要な吸
着作用を発揮することができる。従って、活性炭にあっ
て、これを良好に再生しながら無駄なく利用することが
できる。
In the gas treatment device having the second characteristic configuration of the present application, the regenerated activated carbon regenerated from the activated carbon regenerating mechanism is sized by the sizing mechanism. Then, of the regenerated regenerated carbon that has been sized, the one on the fine grain side is added to the mixing mechanism.
The coarser particles are sent back into the activated carbon bed. The distribution and circulation mechanism is responsible for this function. Therefore, in this structure, the activated carbon powder and the activated carbon on the fine grain side form a coating layer on the surface of the filter cloth, and the same function as described above is performed. Further, the regenerated activated carbon on the coarse grain side can be returned to the activated carbon layer again to exhibit the main adsorption function of the activated carbon. Therefore, the activated carbon can be used without waste while properly reproducing it.

【0007】本願第3の特徴構成を備えたガス処理装置
においては、混入機構に導かれる活性炭粉末もしくは細
粒側の再生活性炭の粒度が粒度調整機構により整えられ
る。このように粒度を調整する場合は、濾布の表面にあ
ってコーティング層を形成できる粒度のものでありなが
ら、層状態となっても、なおその通気抵抗が低い通気抵
抗とできるコーティング層を形成するように、粒度を調
節できる。従って、ガスの浄化の点、さらには、ガスの
圧損の点で好ましいガス処理装置の運転が可能となる。
In the gas treatment apparatus having the third characteristic configuration of the present application, the particle size of the activated carbon powder introduced to the mixing mechanism or the regenerated activated carbon on the fine particle side is adjusted by the particle size adjusting mechanism. When adjusting the particle size in this way, a coating layer is formed on the surface of the filter cloth that can form a coating layer, but even if it is in a layered state, it still has a low ventilation resistance. The particle size can be adjusted as desired. Therefore, it is possible to operate the gas treatment apparatus preferably in terms of gas purification and gas pressure loss.

【0008】本願第4の特徴構成を備えたガス処理装置
においては、活性炭層から抜き出し機構により抜き出さ
れた劣化活性炭の全てが、粉末再生処理機構により機械
的処理を受け、再生されるとともに、粒度調整される。
そして、再生状態にあり粒度調整された状態にある粉末
状再生活性炭が、濾布層の上流側から混入機構により、
処理対象ガス内に混入される。従って、この粉末状再生
活性炭が濾布層の表面にコーティング層を形成し、本願
第1の特徴構成で説明した作用を発揮することができ
る。さらに、従来利用されることが少なかった劣化活性
炭を有効に利用して、活性炭消費の低い運転を行えるよ
うになった。
In the gas treatment apparatus having the fourth characteristic constitution of the present application, all of the deteriorated activated carbon extracted from the activated carbon layer by the extraction mechanism is mechanically treated by the powder regeneration treatment mechanism to be regenerated, and The particle size is adjusted.
Then, the powdery regenerated activated carbon in the regenerated state and in the state where the particle size is adjusted, by the mixing mechanism from the upstream side of the filter cloth layer,
It is mixed in the gas to be treated. Therefore, this powdered regenerated activated carbon forms a coating layer on the surface of the filter cloth layer, and can exhibit the action described in the first characteristic configuration of the present application. Furthermore, it has become possible to operate with low activated carbon consumption by effectively utilizing the deteriorated activated carbon which has been rarely used.

【0009】[0009]

【発明の効果】従って、ガス処理装置に本願第1の特徴
構成を採用することにより、濾布層の表面側に活性炭の
コーティング層を形成して、活性炭の消費率を低下さ
せ、ばいじん、NOx、微量重金属の除去を充分に行
い、装置の安定的な運転を行えるようになった。さら
に、ガス処理装置に本願第2の特徴構成を採用すること
により、濾布表面に形成されるコーティング層に於ける
浄化性能を確保できるとともに、粗粒側の再生活性炭に
ついては、再度、活性炭層で利用して、有効な活性炭の
利用が行えるようになった。さらに、ガス処理装置に本
願第3の特徴構成を採用することにより、濾布表面に形
成されるコーティング層を形成する活性炭の粒度を適切
に調節することにより、処理対象ガスに対する浄化性能
さらにガスの圧損の点で好ましいコーティング層を形成
して、良好な運転状態を確保できるようになった。従っ
て、ガス処理装置に本願第4の特徴構成を採用すること
により、劣化した活性炭を再度、濾布層の表面側に於け
る活性炭のコーティング層形成に活用して、活性炭の消
費率を低下させ、ばいじん、NOx、微量重金属の除去
を充分に行い、装置の安定的な運転を行えるようになっ
た。
Therefore, by adopting the first characteristic constitution of the present invention in the gas treatment apparatus, a coating layer of activated carbon is formed on the surface side of the filter cloth layer to reduce the consumption rate of activated carbon, soot and NOx. , The trace amount of heavy metals was removed sufficiently, and stable operation of the equipment became possible. Further, by adopting the second characteristic configuration of the present invention in the gas treatment device, it is possible to secure the purification performance in the coating layer formed on the surface of the filter cloth, and the regenerated activated carbon on the coarse grain side is again activated carbon layer. It has become possible to effectively use activated carbon by using it. Furthermore, by adopting the third characteristic configuration of the present invention in the gas treatment device, the particle size of the activated carbon forming the coating layer formed on the surface of the filter cloth is appropriately adjusted, and the purification performance for the gas to be treated and the gas By forming a coating layer that is preferable in terms of pressure loss, it has become possible to ensure good operating conditions. Therefore, by adopting the fourth characteristic configuration of the present invention in the gas treatment device, the deteriorated activated carbon is utilized again for forming the coating layer of the activated carbon on the surface side of the filter cloth layer to reduce the consumption rate of the activated carbon. , Dust, NOx, and trace heavy metals were sufficiently removed, and stable operation of the equipment became possible.

【0010】[0010]

【実施例】以下、本願のガス処理装置1の構成を図面に
基づいて説明する。図1に示すように、このガス処理装
置1は、従来型のバグフィルタと同様な構成の装置本体
2と、この装置本体2に付属して備えられる、抜き出し
機構3、活性炭再生機構4、分粒機構5、粒度調整機構
6、さらには混入機構7を備えて構成されている。ここ
で、装置本体2内に複数備えられるガス処理具8は、後
述するように、処理対象ガスの流れ方向に、濾布層9と
活性炭層10とを順に備えたものであり、濾布層9にお
いて、ばいじん、低沸点重金属の濾過除去処理を、活性
炭層10においてNOx、微量重金属の吸着除去処理を
おこなうものである。そして、吸着能が下がった活性炭
(劣化活性炭)にあっては、これらを再生処理して、再
利用できる構成が採用されている。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The configuration of the gas treatment apparatus 1 of the present application will be described below with reference to the drawings. As shown in FIG. 1, the gas treatment apparatus 1 includes an apparatus main body 2 having a configuration similar to that of a conventional bag filter, an extraction mechanism 3, an activated carbon regenerating mechanism 4, and a separation unit which are provided in association with the apparatus main body 2. A grain mechanism 5, a grain size adjusting mechanism 6, and a mixing mechanism 7 are provided. Here, a plurality of gas treatment tools 8 provided in the apparatus main body 2 are, as described later, provided with a filter cloth layer 9 and an activated carbon layer 10 in this order in the flow direction of the gas to be processed. In Fig. 9, soot and dust and low boiling heavy metals are removed by filtration, and in the activated carbon layer 10, NOx and trace heavy metals are removed by adsorption. Then, in the case of activated carbon (deteriorated activated carbon) having a reduced adsorption capacity, a constitution is adopted in which these can be recycled for reuse.

【0011】以下、さらに詳細に説明する。前記装置本
体2は、処理対象ガスが導入されるガス入口11を備え
た導入部12と、複数のガス処理具8が配設される処理
部13と、この処理部13の上部側に位置され、ガス処
理具8による処理を終えた処理済ガスが導出されるガス
出口14を備えた導出部15とを、ガスの流れ方向に備
えて構成されている。
The details will be described below. The apparatus body 2 is provided with an introduction part 12 having a gas inlet 11 for introducing a gas to be treated, a treatment part 13 in which a plurality of gas treatment tools 8 are disposed, and an upper side of the treatment part 13. And a discharge portion 15 having a gas outlet 14 through which the processed gas that has been processed by the gas processing tool 8 is discharged, in the gas flow direction.

【0012】前記ガス処理具8は、図2に示すように外
観構成が円筒状に形成されているものであり、ガスは、
ガス処理具8の周部部位100から円筒内に流入し、こ
の筒内部を上側に移動して、頂部より前記導出部15に
流れる構成となっている。ガス処理具8は、円筒状に形
成される濾布層9と、同様に円筒状に形成されている処
理材保持具16とを、その両端側周縁部位で連接して構
成されている。
As shown in FIG. 2, the gas treating tool 8 has a cylindrical outer configuration, and the gas is
The gas processing tool 8 is configured to flow into the cylinder from the peripheral portion 100, move upward in the cylinder, and flow from the top to the outlet 15. The gas processing tool 8 is configured by connecting a filter cloth layer 9 formed in a cylindrical shape and a processing material holding tool 16 which is also formed in a cylindrical shape at both end side peripheral edge portions thereof.

【0013】前記処理材保持具16は多孔体であるパン
チングメタルから構成されている。その円筒内部空間
は、処理対象ガスである排ガスを処理する活性炭を収納
可能な処理材収納空間17として形成されている。さら
に、この処理材収納空間17の下部部位には仕切り板1
8が設けられており、この仕切り板18により、内部に
収納される活性炭を下部に配設される活性炭再生機構4
側に導くことができるようになっている。
The processing material holder 16 is made of punching metal which is a porous body. The inner space of the cylinder is formed as a processing material storage space 17 capable of storing activated carbon for processing exhaust gas which is a processing target gas. Further, the partition plate 1 is provided in the lower portion of the processing material storage space 17.
8 is provided, and the activated carbon regenerating mechanism 4 in which the activated carbon stored inside is disposed at the bottom by the partition plate 18
Can be guided to the side.

【0014】前記処理材保持具16と前記濾布層9との
部材間に、空間が形成されており、これが逆洗ガスを供
給可能な逆洗ガス供給空間19とされている。この空間
19に対しては、逆洗ガスを適宜供給するための、逆洗
ガス供給機構20が備えられている。
A space is formed between the members of the treatment material holder 16 and the filter cloth layer 9 and serves as a backwash gas supply space 19 capable of supplying backwash gas. A backwash gas supply mechanism 20 for appropriately supplying the backwash gas is provided in the space 19.

【0015】本願のガス処理装置1にあっては、排ガス
は、導入部12、濾布層9、逆洗ガス供給空間19、処
理材保持具16、処理材収納空間17の順に流れ、ガス
処理具頂部に備えられた処理済ガス出口21から、導出
部15に排出される。従って、濾布層9により酸性ガス
の除去用中和剤、排ガスダスト、低沸点重金属を捕集・
除去できる。さらに、処理材収納空間17に収納された
活性炭により、NOx、微量重金属等を除去できる。さ
らに、所定の時間が経過し、濾布表面に除去物22が体
積した状態にあっては、前述の逆洗ガス供給機構20が
適宜作動され、衝撃的なガス圧の変化を伴った逆洗がお
こなわれる。そして、装置本体下部に備えられる集塵室
(図外)に、除去物22が集められて、装置外へ取り出
されて、後の処理(例えば、溶融処理)がおこなわれ
る。この場合、本願にあっては、この除去物22内に活
性炭粉末が含まれているため、これを燃焼・溶融時に熱
源とすることができ処理をスムーズに進めることができ
る。
In the gas treatment device 1 of the present application, the exhaust gas flows in the order of the introduction part 12, the filter cloth layer 9, the backwash gas supply space 19, the treatment material holder 16, and the treatment material storage space 17 to perform gas treatment. The treated gas outlet 21 provided at the top of the tool discharges the gas to the outlet 15. Therefore, the filter cloth layer 9 collects the neutralizing agent for removing the acidic gas, the exhaust gas dust, and the low boiling heavy metal.
Can be removed. Further, the activated carbon stored in the processing material storage space 17 can remove NOx, trace heavy metals, and the like. Further, when the predetermined amount of time has passed and the removed material 22 has accumulated on the surface of the filter cloth, the above-described backwash gas supply mechanism 20 is appropriately operated to perform backwash accompanied by a shocking change in gas pressure. Is performed. Then, the removed matter 22 is collected in a dust collection chamber (not shown) provided in the lower portion of the apparatus main body, taken out of the apparatus, and a subsequent process (for example, melting process) is performed. In this case, in the present application, since the activated carbon powder is contained in the removed material 22, the activated carbon powder can be used as a heat source at the time of burning and melting, and the processing can be smoothly performed.

【0016】以上が、本願の装置本体2の構造及びその
働きであるが、本願のガス処理装置1にあっては、上記
のガス処理具8内の活性炭を再生して再利用する構成が
採用されている。即ち、図1に示すように、本願のガス
処理装置1には、前述の処理材収納空間17内に形成さ
れている活性炭層10より吸着能が低下した劣化活性炭
を抜き出す抜き出し機構3と、抜き出された劣化活性炭
に新たな吸着面を露出させる機械的処理を行って前記劣
化活性炭を再生する活性炭再生機構4が備えられてい
る。さらに、この活性炭再生機構4に於ける機械的処理
により発生する活性炭粉末を、濾布層9の上流側で処理
対象ガス内に混入する混入機構7が備えられている。
The above is the structure and function of the apparatus main body 2 of the present application. In the gas processing apparatus 1 of the present application, a configuration is adopted in which the activated carbon in the gas processing tool 8 is regenerated and reused. Has been done. That is, as shown in FIG. 1, in the gas treatment device 1 of the present application, an extraction mechanism 3 for extracting deteriorated activated carbon having a lower adsorption capacity than the activated carbon layer 10 formed in the treatment material storage space 17, and an extraction mechanism. An activated carbon regenerating mechanism 4 is provided for regenerating the deteriorated activated carbon by performing a mechanical treatment on the deteriorated activated carbon to expose a new adsorption surface. Further, a mixing mechanism 7 for mixing the activated carbon powder generated by the mechanical treatment in the activated carbon regeneration mechanism 4 into the gas to be treated on the upstream side of the filter cloth layer 9 is provided.

【0017】前記抜き出し機構3は、前記ガス処理具8
に接続され、処理材収納空間17内より劣化活性炭を落
下排出可能な排出管3aと前述の仕切り板18の開閉機
構(図外)から構成されている。前記活性炭再生機構4
は所謂ミルクラッシャであり、劣化活性炭をミル処理す
ることにより、活性炭において、被吸着物が吸着してい
ない新たな吸着面を露出する操作をするものである。こ
の処理にあっては、処理の程度により、被吸着物が吸着
された表面層を除去したり、活性炭を粉砕して、活性炭
の内側に存する新たな吸着面を露出することができる。
このような機械的処理にあっては、活性炭粉末が発生す
る。前記混入機構7は、上記のようにして発生する活性
炭粉末および、別途説明する分粒機構5及び粒度調整機
構6を経て得られる比較的粒度の揃った細粒側の再生活
性炭を、処理対象ガスが流れるガス流路24に混入させ
るためのものである。従って、これは、ガス流路24に
開口する混入口7aを備えるとともに、この混入口7a
に所定物(活性炭粉末及び細粒側の再生活性炭)を粒度
調整機構6から導く活性炭移送路7b及び気体搬送用の
ブロア7cを備えて構成されている。
The extraction mechanism 3 includes the gas treatment tool 8
And a discharge pipe 3a capable of dropping and discharging the deteriorated activated carbon from the treatment material storage space 17 and an opening / closing mechanism (not shown) for the partition plate 18 described above. The activated carbon regeneration mechanism 4
Is a so-called milk crusher, which is a milled process of deteriorated activated carbon to expose a new adsorption surface of the activated carbon on which the substance to be adsorbed is not adsorbed. In this treatment, depending on the degree of treatment, it is possible to remove the surface layer on which the substance to be adsorbed is adsorbed or crush the activated carbon to expose a new adsorption surface inside the activated carbon.
In such a mechanical treatment, activated carbon powder is generated. The mixing mechanism 7 uses the activated carbon powder generated as described above, and the regenerated activated carbon on the fine grain side having a relatively uniform grain size obtained through the sizing mechanism 5 and the grain size adjusting mechanism 6, which will be described separately, as a gas to be treated. Is for mixing in the gas flow path 24 through which Therefore, this is provided with the mixing port 7a opening to the gas flow path 24, and this mixing port 7a
In addition, an activated carbon transfer path 7b for guiding a predetermined substance (activated carbon powder and regenerated activated carbon on the fine particle side) from the particle size adjusting mechanism 6 and a blower 7c for gas transfer are configured.

【0018】図1に示すように、前記活性炭再生機構4
と前記混入機構7との間には、前記活性炭再生機構4で
再生された再生活性炭を分粒する分粒機構5が備えら
れ、細粒側の再生活性炭を混入機構7側に導き、且つ粗
粒側の再生活性炭を前記ガス処理具8内に設けられてい
る活性炭層10に戻す分配循環機構25が備えられてい
る。さらに、上記の混入機構7に導かれる活性炭粉末も
しくは細粒側の再生活性炭の粒度を調節する粒度調整機
構6が、前記分粒機構5の下手側の混入機構7の活性炭
移送路7bに備えられている。
As shown in FIG. 1, the activated carbon regeneration mechanism 4 is used.
And a mixing mechanism 7 are provided with a sizing mechanism 5 for sizing the regenerated activated carbon regenerated by the activated carbon regenerating mechanism 4, and guides the regenerated activated carbon on the fine grain side to the mixing mechanism 7 side, and A distribution circulation mechanism 25 for returning the regenerated activated carbon on the grain side to the activated carbon layer 10 provided in the gas treatment tool 8 is provided. Further, the particle size adjusting mechanism 6 for adjusting the particle size of the activated carbon powder or the regenerated activated carbon on the fine particle side guided to the mixing mechanism 7 is provided in the activated carbon transfer path 7b of the mixing mechanism 7 on the lower side of the sizing mechanism 5. ing.

【0019】以上が、本願のガス処理装置1の構造であ
るが、本願にあっては、活性炭はガス処理具8内の処理
材収納空間17内から、その吸着能が30〜50%程度
残存している状態で、抜き出される。そして、活性炭再
生機構4を構成するミルクラッシャにより表面脱離、粉
砕処理されて再生処理され、再生活性炭となる。この工
程で、活性炭粉末が発生する。再生処理された再生活性
炭は分粒機構5に送られ、細粒側のものと粗粒側のもの
とに分粒される。そして、細粒側のものが前述の活性炭
粉末とともに、混入機構7側に送られて、処理対象ガス
内に混入される。従って、この部位から混入された活性
炭は、同時に混入される酸性ガス用の中和剤とともに、
濾布層の表面にコーティング層26を形成し、夫々の機
能を発揮する。一方、粗粒側の再生活性炭は、前述のガ
ス処理具8内の処理材収納空間17内に再度充填され、
この部位で、吸着作用を発揮する。従って、本願の構造
においては、活性炭を充分に活用することができ、装置
全体としての活性炭さらには中和剤の消費量を従来より
抑えることができる。
The above is the structure of the gas treatment apparatus 1 of the present application. In the present application, the activated carbon has an adsorption capacity of about 30 to 50% from the treatment material storage space 17 in the gas treatment tool 8. It is taken out in the state of doing. Then, the surface is desorbed and pulverized by a milk crusher constituting the activated carbon regenerating mechanism 4 to be regenerated to be regenerated activated carbon. In this process, activated carbon powder is generated. The regenerated activated carbon that has been regenerated is sent to the sizing mechanism 5, where it is sized into fine particles and coarse particles. Then, the fine particles are sent to the mixing mechanism 7 side together with the above-mentioned activated carbon powder and mixed into the gas to be treated. Therefore, the activated carbon mixed from this part, together with the neutralizing agent for the acidic gas mixed at the same time,
The coating layer 26 is formed on the surface of the filter cloth layer to exert its respective functions. On the other hand, the regenerated activated carbon on the coarse particle side is refilled in the processing material storage space 17 in the gas processing tool 8 described above,
At this site, it exerts an adsorption effect. Therefore, in the structure of the present application, the activated carbon can be fully utilized, and the consumption amount of the activated carbon and the neutralizing agent in the entire device can be suppressed more than before.

【0020】〔別実施例〕本願の別実施例について、以
下説明する。 (イ) 上記の実施例においては、処理材収納空間内に
収納されるものとしては、通常の活性炭を挙げたが、こ
のようなものとしては、活性コークスをも含めることが
でき、これらを含めて広い意味での活性炭と呼ぶ。 (ロ) 上記の実施例においては、劣化活性炭を再生す
るとともに、再生活性炭を粒度に従って分別し、粗粒側
のものについては、ガス処理具内へ戻す構成としたが、
劣化活性炭の全てを粉末化するとともに再生して、処理
対象ガス内に混入させる構成を採用しても、活性炭の再
利用により、その消費量を低減化させることができる。
このような例を図3に示した。図3に示すものの例と、
図1に示すものの例とを比較すると、図3に示すものに
あっても、抜き出し機構3及び混入機構7が備えられて
いる。しかしながら、この例にあっては、分粒機構は備
えられておらず、再生活性炭を混入に適した状態でおこ
なうために、粉末再生処理機構500により粒度調整さ
れた粉末状再生活性炭を得るように、これが構成されて
いる。即ち、この粉末再生処理機構500は、前述の例
のミルクラッシャ500aを備えるとともに、このクラ
ッシャ500aから排出される再生活性炭の粒度を整え
る粒度調整機構500bを備えて構成されている。結
果、この機構500により、粉末化、粒度調整、さらに
は再生処理を経た粉末状再生活性炭の全てが、処理対象
ガスへ混入され、利用される。この構成の場合は、活性
炭の活性が比較的低くなった状態で活性炭を抜き出し、
濾布層表面に於けるコーティング層26の形成に役立て
るのである。 (ハ) 上記の実施例においては、活性炭のガス処理具
からの抜き取り操作のタイミングについては、処理の進
行に伴う定期バッチ的な操作としたが、これを連続的に
抜き取る構成としても、本願の目的は達成できる。
Another Embodiment Another embodiment of the present application will be described below. (A) In the above-mentioned embodiment, the ordinary activated carbon is used as the material to be stored in the treatment material storage space. However, as such a material, activated coke can be also included. It is called activated carbon in a broad sense. (B) In the above embodiment, the deteriorated activated carbon is regenerated, the regenerated activated carbon is separated according to the particle size, and the coarse particle side is returned to the gas treatment tool.
Even if all of the deteriorated activated carbon is pulverized and regenerated and mixed into the gas to be treated, the consumption of the activated carbon can be reduced by reusing the activated carbon.
Such an example is shown in FIG. An example of what is shown in FIG.
Compared with the example shown in FIG. 1, even the example shown in FIG. 3 is provided with the extracting mechanism 3 and the mixing mechanism 7. However, in this example, a sizing mechanism is not provided, and in order to carry out the regenerated activated carbon in a state suitable for mixing, it is necessary to obtain the powdered regenerated activated carbon whose particle size is adjusted by the powder regeneration processing mechanism 500. , This is configured. That is, the powder regeneration processing mechanism 500 includes the milk crusher 500a of the above-described example and the particle size adjusting mechanism 500b for adjusting the particle size of the regenerated activated carbon discharged from the crusher 500a. As a result, by this mechanism 500, all of the powdery regenerated activated carbon that has been pulverized, adjusted in particle size, and regenerated is mixed into the gas to be treated and used. In the case of this configuration, the activated carbon is extracted with the activity of the activated carbon being relatively low,
It serves to form the coating layer 26 on the surface of the filter cloth layer. (C) In the above-described embodiment, the timing of the operation of extracting the activated carbon from the gas treatment tool was a periodic batch operation with the progress of the treatment, but even if it is configured to be continuously extracted, The purpose can be achieved.

【0021】尚、特許請求の範囲の項に図面との対照を
便利にするために符号を記すが、該記入により本発明は
添付図面の構成に限定されるものではない。
In the claims, reference numerals are provided for convenience of comparison with the drawings, but the present invention is not limited to the configuration shown in the attached drawings.

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

【図1】本願のガス処理装置の構成を示す図FIG. 1 is a diagram showing a configuration of a gas treatment device of the present application.

【図2】本願のガス処理具の詳細構成を示す図FIG. 2 is a diagram showing a detailed configuration of a gas treatment tool of the present application.

【図3】本願のガス処理装置の別構成例を示す図FIG. 3 is a diagram showing another configuration example of the gas treatment device of the present application.

【符号の説明】[Explanation of symbols]

3 抜き出し機構 4 活性炭再生機構 5 分粒機構 6 粒度調整機構 7 混入機構 9 濾布層 10 活性炭層 500 粉末再生処理機構 3 Extraction mechanism 4 Activated carbon regeneration mechanism 5 Grain size mechanism 6 Particle size adjustment mechanism 7 Mixing mechanism 9 Filter cloth layer 10 Activated carbon layer 500 Powder regeneration treatment mechanism

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 処理対象ガスの流れ方向に沿って濾布層
(9)と活性炭層(10)とを備え、前記活性炭層(1
0)より吸着能が低下した劣化活性炭を抜き出す抜き出
し機構(3)を備え、抜き出された前記劣化活性炭に新
たな吸着面を露出させる機械的処理を行って前記劣化活
性炭を再生する活性炭再生機構(4)を備えるととも
に、前記活性炭再生機構(4)に於ける機械的処理によ
り発生する活性炭粉末を、前記濾布層(9)の上流側で
前記処理対象ガス内に混入する混入機構(7)を備えた
ガス処理装置。
1. A filter cloth layer (9) and an activated carbon layer (10) are provided along a flow direction of a gas to be treated, and the activated carbon layer (1).
0), the activated carbon regenerating mechanism is provided with a withdrawing mechanism (3) for withdrawing the deteriorated activated carbon having a lower adsorption capacity, and performing a mechanical treatment to expose a new adsorption surface to the withdrawn deteriorated activated carbon to regenerate the deteriorated activated carbon. A mixing mechanism (7) that includes (4) and that mixes the activated carbon powder generated by the mechanical treatment in the activated carbon regeneration mechanism (4) into the gas to be treated upstream of the filter cloth layer (9). ) Equipped with a gas treatment device.
【請求項2】 前記活性炭再生機構(4)と前記混入機
構(7)との間に、前記活性炭再生機構(4)で再生さ
れた再生活性炭を分粒する分粒機構(5)を備え、細粒
側の前記再生活性炭を前記混入機構(7)に供給し、且
つ粗粒側の前記再生活性炭を前記活性炭層(10)に戻
す分配循環機構(25)を備えた請求項1記載のガス処
理装置。
2. A sizing mechanism (5) for sizing the regenerated activated carbon regenerated by the activated carbon regenerating mechanism (4) is provided between the activated carbon regenerating mechanism (4) and the mixing mechanism (7), The gas according to claim 1, further comprising a distribution circulation mechanism (25) for supplying the regenerated activated carbon on the fine grain side to the mixing mechanism (7) and returning the regenerated activated carbon on the coarse grain side to the activated carbon layer (10). Processing equipment.
【請求項3】 前記混入機構(7)に導かれる前記活性
炭粉末もしくは前記細粒側の再生活性炭の粒度を調節す
る粒度調整機構(6)を備えた請求項2記載のガス処理
装置。
3. The gas treatment apparatus according to claim 2, further comprising a particle size adjusting mechanism (6) for adjusting the particle size of the activated carbon powder or the regenerated activated carbon on the fine particle side, which is guided to the mixing mechanism (7).
【請求項4】 処理対象ガスの流れ方向に沿って濾布層
(9)と活性炭層(10)とを備え、前記活性炭層(1
0)より吸着能が低下した劣化活性炭を抜き出す抜き出
し機構(3)を備え、抜き出された前記劣化活性炭に新
たな吸着面を露出させる機械的処理を行って、粒度調整
された粉末状再生活性炭を得る粉末再生処理機構(50
0)を備えるとともに、前記粉末再生処理機構(50
0)により得られる前記粉末状再生活性炭を、前記濾布
層(9)の上流側で前記処理対象ガス内に混入する混入
機構(7)を備えたガス処理装置。
4. The activated carbon layer (1) is provided with a filter cloth layer (9) and an activated carbon layer (10) along the flow direction of the gas to be treated.
0), which is equipped with a withdrawal mechanism (3) for withdrawing the deteriorated activated carbon having a lower adsorption capacity, and a mechanical treatment for exposing a new adsorption surface to the extracted deteriorated activated carbon to adjust the particle size of powdered regenerated activated carbon. Powder regeneration processing mechanism (50
0), and the powder regeneration treatment mechanism (50
0) The powdered regenerated activated carbon obtained in 0) is equipped with a mixing mechanism (7) for mixing the powdered regenerated activated carbon into the gas to be treated on the upstream side of the filter cloth layer (9).
JP7157351A 1995-06-23 1995-06-23 Gas treating device Pending JPH0914633A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7157351A JPH0914633A (en) 1995-06-23 1995-06-23 Gas treating device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7157351A JPH0914633A (en) 1995-06-23 1995-06-23 Gas treating device

Publications (1)

Publication Number Publication Date
JPH0914633A true JPH0914633A (en) 1997-01-17

Family

ID=15647784

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7157351A Pending JPH0914633A (en) 1995-06-23 1995-06-23 Gas treating device

Country Status (1)

Country Link
JP (1) JPH0914633A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003286020A (en) * 2002-03-27 2003-10-07 Electric Power Dev Co Ltd Highly activated active coke powder and manufacturing method thereof
WO2005030641A1 (en) * 2003-09-26 2005-04-07 Electric Power Development Co., Ltd. Highly activated coke powder and process for producing the same
KR101674328B1 (en) * 2015-12-23 2016-11-08 코오롱환경서비스주식회사 Flue gas treatment system
KR101981169B1 (en) * 2019-02-28 2019-05-22 주식회사 대성그린테크 Continuously regeneration device for activated carbon connecting structure with filtration apparatus and activated carbon recycling method using the same

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JPH0731847A (en) * 1993-07-20 1995-02-03 Kobe Steel Ltd Removal of harmful substance from waste gas
JPH0747228A (en) * 1993-08-06 1995-02-21 Sumitomo Heavy Ind Ltd Treatment of exhaust gas

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0731847A (en) * 1993-07-20 1995-02-03 Kobe Steel Ltd Removal of harmful substance from waste gas
JPH0747228A (en) * 1993-08-06 1995-02-21 Sumitomo Heavy Ind Ltd Treatment of exhaust gas

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003286020A (en) * 2002-03-27 2003-10-07 Electric Power Dev Co Ltd Highly activated active coke powder and manufacturing method thereof
WO2005030641A1 (en) * 2003-09-26 2005-04-07 Electric Power Development Co., Ltd. Highly activated coke powder and process for producing the same
KR101674328B1 (en) * 2015-12-23 2016-11-08 코오롱환경서비스주식회사 Flue gas treatment system
KR101981169B1 (en) * 2019-02-28 2019-05-22 주식회사 대성그린테크 Continuously regeneration device for activated carbon connecting structure with filtration apparatus and activated carbon recycling method using the same
WO2020175743A1 (en) * 2019-02-28 2020-09-03 주식회사 대성그린테크 Continuous activated carbon regeneration apparatus using hydrothermal pressurization, having structure connected with filter, and continuous activated carbon regeneration method using same

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