JP2003286822A - Device and method for removing floating fine particulate in exhaust gas - Google Patents

Device and method for removing floating fine particulate in exhaust gas

Info

Publication number
JP2003286822A
JP2003286822A JP2002087723A JP2002087723A JP2003286822A JP 2003286822 A JP2003286822 A JP 2003286822A JP 2002087723 A JP2002087723 A JP 2002087723A JP 2002087723 A JP2002087723 A JP 2002087723A JP 2003286822 A JP2003286822 A JP 2003286822A
Authority
JP
Japan
Prior art keywords
exhaust gas
catalyst solution
suspended
catalyst
particulates
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP2002087723A
Other languages
Japanese (ja)
Other versions
JP4215994B2 (en
Inventor
Toshihiko Setoguchi
稔彦 瀬戸口
Taro Ichihara
太郎 市原
Yuichi Fujioka
祐一 藤岡
Yukihiro Abe
幸浩 阿部
Yuji Oda
裕司 小田
Hiroyuki Endo
浩之 遠藤
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries 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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP2002087723A priority Critical patent/JP4215994B2/en
Publication of JP2003286822A publication Critical patent/JP2003286822A/en
Application granted granted Critical
Publication of JP4215994B2 publication Critical patent/JP4215994B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Processes For Solid Components From Exhaust (AREA)
  • Separating Particles In Gases By Inertia (AREA)
  • Separation Of Particles Using Liquids (AREA)
  • Exhaust Gas Treatment By Means Of Catalyst (AREA)
  • Exhaust Gas After Treatment (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide a removal device for fine particulates floating in exhaust gas which removes the floating fine particulates contained in the exhaust gas from an internal combustion engine such as a diesel engine or the like. <P>SOLUTION: The device is provided with a fine particulate removal device body 16 having a capture portion 13 mounted thereon which captures the floating fine particulates 12 by making the exhaust gas 11 (containing the floating fine particulates 12) pass therethrough, a front chamber 14 and a rear chamber 15, a discharge line 18 which discharges the cleaned-up exhaust gas 17 having passed through the capture portion 13, and a catalyst solution spray means 20 which sprays and adheres a catalyst solution 19 onto surfaces of the fine particulates 12 in the exhaust gas captured by the capture portion 13. The device is also provided with a bypass line 21 which lets the exhaust gas flow into the exhaust gas line 18 from the front chamber 14 of the capture portion 13 without making the exhaust gas pass through the capture portion 13 within the fine particulate removal device main body 16. <P>COPYRIGHT: (C)2004,JPO

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、例えば船舶用、陸
上走行用,陸上定置用の例えばディーゼルエンジン等の
内燃機関等からの排ガス中に含まれる浮遊微粒子(SP
M)を除去する排ガス中の浮遊微粒子除去装置及び方法
に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to suspended particulates (SP) contained in exhaust gas from an internal combustion engine such as a diesel engine for ships, land running, or stationary on land.
The present invention relates to an apparatus and method for removing suspended particles in exhaust gas for removing M).

【0002】[0002]

【背景技術】従来、船舶用、陸上走行用、陸上定置用デ
ィーゼルエンジン等からの排ガス中に含まれる浮遊微粒
子(SPM、以下単に「微粒子」ともいう。)を除去す
るには、セラミックス製のハニカムフィルタ等によるD
PF(Diesel Particulate Filter)が提案されており、
該DPFに微粒子を捕集し、堆積量が増えると排気抵抗
が増大するので、これを燃焼除去し再生している。
BACKGROUND ART Conventionally, in order to remove suspended fine particles (SPM, hereinafter also simply referred to as “fine particles”) contained in exhaust gas from a marine engine, a land traveling vehicle, a stationary stationary diesel engine or the like, a ceramic honeycomb is used. D by filter etc.
PF (Diesel Particulate Filter) has been proposed,
When particulates are collected in the DPF and the amount of deposition increases, the exhaust resistance increases, so this is burned and removed for regeneration.

【0003】この再生方法としては、スロットリングに
より排気温度を向上させる方法やヒータ加熱方法、或い
は追い焚き方法等によって排気ガス温度を上昇させて、
捕集微粒子中の未燃焼分を燃焼させていた。
As this regeneration method, the exhaust gas temperature is raised by a method of improving the exhaust temperature by throttling, a heater heating method, a reheating method, or the like,
The unburned portion of the collected fine particles was burned.

【0004】[0004]

【発明が解決しようとする課題】しかしながら、従来の
微粒子分解処理方法では、以下のような問題がある。 (1) 再生時における熱衝撃の繰返によりハニカム状のセ
ラミックスフィルタの破損が生じるという問題がある。 (2) 異常燃焼の発生により、フィルタ材の耐熱性、耐熱
衝撃性が不足し、損傷が生じるという問題がある。 (3) ヒータ加熱や追い焚き用の装置及び燃料等のユーテ
ィリティー費用が必要となので、処理コストの低減を図
るという要望がある。 (4) 燃焼が十分でない場合には、圧損が増大し、使用不
能となり、その結果当該フィルタ自身を交換する必要が
ある。
However, the conventional method for decomposing fine particles has the following problems. (1) There is a problem that the honeycomb ceramic filter is damaged due to repeated thermal shocks during regeneration. (2) There is a problem in that the heat resistance and thermal shock resistance of the filter material are insufficient due to the occurrence of abnormal combustion, resulting in damage. (3) Utilities such as heater heating and reheating equipment and utility costs such as fuel are required, and there is a demand to reduce processing costs. (4) If the combustion is not sufficient, the pressure loss increases and it becomes unusable, so that the filter itself must be replaced.

【0005】本発明は、上記問題に鑑み、従来のような
ヒータ等の加熱手段を用いることなくしかも低温で排ガ
ス中の浮遊微粒子を分解することのできる排ガス中の浮
遊微粒子除去装置及び方法を提供することを課題とす
る。
In view of the above problems, the present invention provides an apparatus and method for removing suspended particulates in exhaust gas which can decompose suspended particulates in exhaust gas at low temperature without using conventional heating means such as a heater. The task is to do.

【0006】[0006]

【課題を解決するための手段】前記課題を解決する本発
明の第1の発明は、排ガス中の浮遊微粒子を除去する浮
遊微粒子除去装置であって、上記排ガスを通気させて、
上記浮遊微粒子を捕獲する捕獲部を内装して前室と後室
とを備えた微粒子除去装置本体と、該捕獲部を通気した
排ガスを排出する排出ラインと、上記捕集部で捕集した
排ガス中の微粒子表面に触媒溶液を付着させる触媒付着
手段と備えてなると共に、上記微粒子除去装置本体内の
捕獲部を通過することなく捕獲部の前室側から排ガスラ
インへ排ガスを逃がすバイパスラインを設けたことを特
徴とする排ガス中の浮遊微粒子除去装置にある。
The first invention of the present invention for solving the above-mentioned problems is a suspended particle removing apparatus for removing suspended particles in exhaust gas, wherein the exhaust gas is ventilated,
A main body of a fine particle removing device equipped with a front chamber and a rear chamber that incorporates a capturing unit for capturing the suspended particulates, an exhaust line for exhausting exhaust gas aerated through the capturing unit, and an exhaust gas captured by the capturing unit. In addition to being equipped with a catalyst adhering means for adhering the catalyst solution to the surface of the fine particles inside, a bypass line is provided to allow the exhaust gas to escape from the front chamber side of the trap portion to the exhaust gas line without passing through the trap portion in the main body of the fine particle removing device The present invention resides in a device for removing suspended particulates in exhaust gas.

【0007】第2の発明は、第1の発明において、上記
触媒溶液がアルカリ金属或いはアルカリ土類金属の少な
くとも1種を含む触媒を含有してなり、上記捕獲部の表
面で捕集された微粒子を排ガス通気時に触媒燃焼させ、
除去することを特徴とする浮遊微粒子除去装置にある。
In a second aspect based on the first aspect, the catalyst solution contains a catalyst containing at least one of an alkali metal and an alkaline earth metal, and the fine particles collected on the surface of the capturing section. Is catalytically burned when venting exhaust gas,
It is an apparatus for removing suspended particles characterized by removing the particles.

【0008】第3の発明は、第1又は2の発明におい
て、上記微粒子除去装置本体内の捕獲部の後室側から触
媒溶液を排出する排出ラインと、触媒溶液を貯蔵する触
媒溶液貯蔵手段とを備えたことを特徴とする浮遊微粒子
除去装置にある。
According to a third aspect of the present invention, in the first or second aspect of the invention, a discharge line for discharging the catalyst solution from the rear chamber side of the trap in the main body of the fine particle removing device, and a catalyst solution storage means for storing the catalyst solution. An apparatus for removing suspended particles is provided.

【0009】第4の発明は、第3の発明において、上記
触媒溶液貯蔵手段から触媒溶液を触媒付着手段に送給す
る送給ラインを設けたことを特徴とする浮遊微粒子除去
装置にある。
A fourth aspect of the invention is an apparatus for removing suspended particulates according to the third aspect of the invention, further comprising a feed line for feeding the catalyst solution from the catalyst solution storage means to the catalyst adhering means.

【0010】第5の発明は、第3の発明において、上記
触媒溶液貯蔵手段内の触媒溶液を冷却する冷却手段を設
けたことを特徴とする浮遊微粒子除去装置にある。
A fifth aspect of the present invention is the suspended particulate removing apparatus according to the third aspect of the present invention, characterized in that cooling means for cooling the catalyst solution in the catalyst solution storage means is provided.

【0011】第6の発明は、第4の発明において、上記
送給ラインに冷却フィンを設け、触媒溶液を冷却するこ
とを特徴とする浮遊微粒子除去装置にある。
A sixth aspect of the present invention is the suspended particulate removal apparatus according to the fourth aspect of the present invention, wherein a cooling fin is provided in the feed line to cool the catalyst solution.

【0012】第7の発明は、第1の発明において、上記
微粒子除去装置本体内の捕獲部の後室内にフィルタを設
けてなり、触媒溶液を濾過することを特徴とする浮遊微
粒子除去装置にある。
A seventh aspect of the present invention is the suspended particulate removing apparatus according to the first aspect of the present invention, characterized in that a filter is provided in the rear chamber of the capturing section in the main body of the particulate removing apparatus to filter the catalyst solution. .

【0013】第8の発明は、第1の発明において、上記
微粒子除去装置本体から排ガスを排出する排出ラインに
ドレン手段を設けたことを特徴とする浮遊微粒子除去装
置にある。
An eighth aspect of the present invention is the floating particulate matter removing apparatus according to the first aspect of the present invention, characterized in that a drain means is provided in the discharge line for discharging the exhaust gas from the main body of the particulate removing apparatus.

【0014】第9の発明は、第8の発明において、上記
ドレン手段で捕集した触媒溶液貯蔵手段で回収する回収
ラインを設けたことを特徴とする浮遊微粒子除去装置に
ある。
A ninth aspect of the present invention is the suspended particulate removing device according to the eighth aspect, further comprising a recovery line for recovering the catalyst solution storage means collected by the drain means.

【0015】第10の発明は、第1乃至9のいずれか一
の排ガス中の浮遊微粒子除去装置を用い、排ガスを通気
する際にバイパスラインを開放することを特徴とする排
ガス中の浮遊微粒子除去方法にある。
According to a tenth aspect of the present invention, the apparatus for removing suspended particulates in exhaust gas according to any one of the first to ninth aspects is used, wherein a bypass line is opened when the exhaust gas is ventilated. On the way.

【0016】第11の発明は、第1乃至9のいずれか一
の排ガス中の浮遊微粒子除去装置を用い、微粒子除去装
置本体内の捕獲部で仕切られた前室と後室との圧力差を
測定し、所定圧力差以上となった場合に、排ガスを一時
的に通気するバイパスラインを開放することを特徴とす
る排ガス中の浮遊微粒子除去方法にある。
An eleventh aspect of the present invention uses the device for removing suspended particulates in exhaust gas according to any one of the first to ninth aspects, wherein a pressure difference between a front chamber and a rear chamber partitioned by a trap in the main body of the particulate removal device is provided. A method for removing suspended particulates in exhaust gas is characterized in that a bypass line for temporarily ventilating the exhaust gas is opened when the measured pressure exceeds a predetermined pressure difference.

【0017】第12の発明は、 排ガスを浄化する排ガ
ス処理システムであって、排ガスの煙道に介装され、排
ガス中の浮遊微粒子を分解処理する請求項1乃至9の浮
遊微粒子除去装置を有することを特徴とする排ガス処理
システムにある。
A twelfth aspect of the present invention is an exhaust gas treatment system for purifying exhaust gas, which has a suspended particulate removal device according to any one of claims 1 to 9 which is interposed in an exhaust gas flue and decomposes suspended particulates in the exhaust gas. The exhaust gas treatment system is characterized by that.

【0018】第13の発明は、第12の発明において、
上記微粒子除去装置の前流側又は後流側に排ガス中の窒
素酸化物を分解処理する脱硝装置を有することを特徴と
する排ガス処理システムにある。
A thirteenth invention is the twelfth invention, wherein
The exhaust gas treatment system is characterized in that it has a denitration device for decomposing nitrogen oxides in the exhaust gas on the upstream side or the downstream side of the fine particle removing device.

【0019】[0019]

【発明の実施の形態】以下、本発明の実施形態を説明す
るが、本発明はこれに限定されるものではない。
BEST MODE FOR CARRYING OUT THE INVENTION Embodiments of the present invention will be described below, but the present invention is not limited thereto.

【0020】[第1の実施の形態]図1は本実施の形態
の排ガス中の浮遊微粒子除去装置の概略図である。排ガ
ス11中の浮遊微粒子を除去する浮遊微粒子除去装置で
あって、上記排ガス(浮遊微粒子12を含む)11を通
気させて、上記浮遊微粒子12を捕獲する捕獲部13を
内装して前室14と後室15とを備えた微粒子除去装置
本体16と、該捕獲部13を通気した浄化排ガス17を
排出する排出ライン18と、上記捕集部13で捕集した
排ガス中の微粒子表12面に触媒溶液19を噴霧して付
着させる触媒溶液噴霧手段20と備えてなると共に、上
記微粒子除去装置本体16内の捕獲部13を通過するこ
となく捕獲部13の前室14側から上記排ガスライン1
8へ排ガスを逃がすバイパスライン21を設けたもので
ある。
[First Embodiment] FIG. 1 is a schematic view of a device for removing suspended particles in exhaust gas according to the present embodiment. A suspended particulates removing device for removing suspended particulates in the exhaust gas (11), which is provided with a trap section (13) for ventilating the exhaust gas (including suspended particulates (12)) and capturing the suspended particulates (12). A fine particle removing device main body 16 having a rear chamber 15, an exhaust line 18 for exhausting the purified exhaust gas 17 that has permeated the capturing portion 13, and a catalyst on the surface 12 of the fine particles in the exhaust gas captured by the capturing portion 13. The exhaust gas line 1 is provided with catalyst solution spraying means 20 for spraying and adhering the solution 19 and from the front chamber 14 side of the trap 13 without passing through the trap 13 in the main body 16 of the fine particle removing device.
A bypass line 21 is provided to allow exhaust gas to escape to 8.

【0021】本実施の形態にかかる排ガス中の微粒子除
去装置では、排ガス11中の微粒子12を捕獲部13で
付着させ、その後、所定時間経過した後又は圧力変動が
発生した後、捕獲された上記微粒子表面に触媒溶液19
を噴霧して付着させた後に触媒溶液を乾燥させ、その後
排ガスの排熱により未燃焼微粒子を燃焼するものであ
る。上記触媒に噴霧するために、本実施の形態では、浮
遊微粒子除去装置本体の天井部から触媒溶液19を噴霧
するようにしている。
In the device for removing fine particles from exhaust gas according to the present embodiment, the fine particles 12 in the exhaust gas 11 are adhered by the capturing unit 13 and then captured after a predetermined time has elapsed or a pressure fluctuation has occurred. Catalyst solution 19 on the surface of fine particles
Is sprayed and adhered, the catalyst solution is dried, and then unburned fine particles are burned by exhaust heat of exhaust gas. In order to spray the catalyst, the catalyst solution 19 is sprayed from the ceiling portion of the main body of the suspended particulate removing apparatus in this embodiment.

【0022】本実施の形態では上記触媒液19を噴霧す
る際又は前室14と後室15との間で圧力変動があった
際に、バイパスライン21を開放して、捕獲部13の目
詰まりを防止するようにしている。
In the present embodiment, when the catalyst liquid 19 is sprayed or when there is a pressure fluctuation between the front chamber 14 and the rear chamber 15, the bypass line 21 is opened and the trapping portion 13 is clogged. I try to prevent it.

【0023】また、噴霧した触媒溶液19は触媒回収タ
ンク30で回収して再利用に供されている。また、微粒
子除去装置本体16の後室の内部には、フィルタ22を
設けて触媒溶液19を濾過するようにしている。
Further, the sprayed catalyst solution 19 is recovered in the catalyst recovery tank 30 for reuse. In addition, a filter 22 is provided inside the rear chamber of the main body 16 of the fine particle removing device to filter the catalyst solution 19.

【0024】また、触媒回収タンク30内には水を供給
して触媒溶液19を冷却する冷却手段23が設けられて
いる。これは高温の排気ガスを通過させて微粒子を捕集
した捕獲部と触媒溶液19が接触するので、高温となる
ことがあるからである。また、触媒回収タンク30内に
は供給水24及び新規触媒溶液19を供給して触媒濃度
を調整(例えばpH計等による調整)するようにしてい
る。また、触媒の残渣25は回収タンクの底部から適宜
廃棄するようにしてもよい。
A cooling means 23 for supplying water to cool the catalyst solution 19 is provided in the catalyst recovery tank 30. This is because the catalyst solution 19 comes into contact with the capturing portion that collects the fine particles by passing the high-temperature exhaust gas, so that the temperature may be high. Further, the supply water 24 and the new catalyst solution 19 are supplied into the catalyst recovery tank 30 to adjust the catalyst concentration (for example, adjustment with a pH meter). Further, the catalyst residue 25 may be appropriately discarded from the bottom of the recovery tank.

【0025】また、触媒の冷却方法としては、冷却手段
23の替わりに、触媒溶液を噴霧する触媒溶液噴霧手段
20までの触媒溶液19の供給配管26の周囲には冷却
フィン等の冷却手段を設けるようにしてもよい。
As a method of cooling the catalyst, instead of the cooling means 23, a cooling means such as a cooling fin is provided around the supply pipe 26 for supplying the catalyst solution 19 to the catalyst solution spraying means 20 for spraying the catalyst solution. You may do it.

【0026】ここで、本発明で触媒溶液とは、炭酸カリ
ウム,炭酸ナトリウム等のNa,K等のアルカリ金属,
アルカリ土類金属のうち少なくとも一種を含む水溶液で
ある。また、アルカリ触媒として海水を利用することも
できる。また、上記アルカリ金属或いはアルカリ土類金
属の少なくとも1種を海水中に含有するようにしてもよ
い。
In the present invention, the catalyst solution means Na such as potassium carbonate and sodium carbonate, alkali metal such as K,
It is an aqueous solution containing at least one kind of alkaline earth metal. Further, seawater can be used as the alkali catalyst. Further, at least one kind of the above-mentioned alkali metal or alkaline earth metal may be contained in seawater.

【0027】本発明ではアルカリ触媒溶液をフィルタに
捕集された微粒子の表面を覆うように噴霧することで、
触媒を微粒子表面及び内部に含浸・担持させることによ
り、当該触媒を均一に配置させることができ、この結
果、燃焼場を均一化させることができると共に、従来の
ヒータ等による燃焼温度(400℃以上)よりもより低
温側(300℃以下)において触媒燃焼を可能とするこ
とができる。上記触媒燃焼の熱源は高温の排気ガスを用
いている。
In the present invention, by spraying the alkaline catalyst solution so as to cover the surface of the fine particles collected by the filter,
By impregnating and supporting the catalyst on the surface and inside of the fine particles, the catalyst can be uniformly arranged, and as a result, the combustion field can be made uniform, and the combustion temperature by the conventional heater (400 ° C or higher). It is possible to enable catalytic combustion on a lower temperature side (300 ° C. or lower) than the above. The heat source of the catalytic combustion uses high temperature exhaust gas.

【0028】次に、図2において、上記捕集された微粒
子12の触媒分解の概要を説明する。図2に示すよう
に、捕集された浮遊微粒子12は、脱落水中に含有され
た触媒によりその表面が覆われることになる。その後、
排ガスが通気され、触媒溶液が乾燥すると共に、浮遊微
粒子12の細孔中にも触媒溶液19が浸透する。次いで
内部に侵入した触媒溶液19も乾燥し、触媒活性を示す
成分が微粒子内部に均一に残留する。その後、排ガス1
1を流入させることにより、排ガス11の温度でゆっく
り触媒燃焼が進行することになる。この触媒燃焼により
浮遊微粒子12の表面のみならず内部においても触媒作
用が働き、浮遊微粒子12の完全燃焼が可能となる。な
お、上記乾燥は排ガスを供給する代わりに、空気等を供
給して触媒成分を乾燥させるようにしてもよい。
Next, referring to FIG. 2, an outline of catalytic decomposition of the collected fine particles 12 will be described. As shown in FIG. 2, the surface of the collected suspended fine particles 12 is covered with the catalyst contained in the dropped water. afterwards,
The exhaust gas is aerated, the catalyst solution is dried, and the catalyst solution 19 also permeates the pores of the suspended fine particles 12. Next, the catalyst solution 19 that has penetrated into the inside is also dried, and the component exhibiting catalytic activity remains uniformly inside the fine particles. After that, exhaust gas 1
By causing 1 to flow in, catalytic combustion slowly proceeds at the temperature of the exhaust gas 11. Due to this catalytic combustion, the catalytic action works not only on the surface of the suspended fine particles 12 but also inside thereof, and the suspended fine particles 12 can be completely burned. In the above drying, instead of supplying exhaust gas, air or the like may be supplied to dry the catalyst component.

【0029】この結果、従来のようにヒータ等を用いる
ことなく、しかも低温領域(例えば300℃程度)にお
いて、当該微粒子中の未燃焼分(スート,タール等)を
分解することができることになる。よって、排ガス中の
浮遊微粒子12は捕集され触媒燃焼がなされるので連続
的に処理することができ、微粒子の除去されたクリーン
排ガスを排出することができる。
As a result, unburned components (soot, tar, etc.) in the fine particles can be decomposed in a low temperature region (eg, about 300 ° C.) without using a heater or the like as in the conventional case. Therefore, the suspended particulates 12 in the exhaust gas are collected and catalytically burned, so that they can be continuously treated, and the clean exhaust gas from which the particulates have been removed can be discharged.

【0030】本発明では、排ガス中の浮遊微粒子を分解
処理することができるので、内燃機関の種類を何ら特定
するものではない。例えば船舶用、陸上走行用、陸上定
置用ディーゼルや発電機等の内燃機関からの排ガス中に
含まれる浮遊微粒子(SPM)の未燃焼分を低温で分解
処理することができる。また、内燃機関から排出される
排ガス中の浮遊微粒子を分解除去するのみならず、例え
ば都市ゴミ焼却炉,産業廃棄物焼却炉,汚泥焼却炉等の
各種焼却炉、熱分解炉、溶融炉等から排ガス中の浮遊微
粒子も除去することができる。
In the present invention, the suspended particulates in the exhaust gas can be decomposed, so that the type of the internal combustion engine is not specified. For example, it is possible to decompose unburned particulate matter (SPM) contained in exhaust gas from internal combustion engines such as ships, land vehicles, stationary diesel engines, and generators at a low temperature. In addition to decomposing and removing suspended particulates in the exhaust gas discharged from an internal combustion engine, for example, from various incinerators such as municipal waste incinerators, industrial waste incinerators, sludge incinerators, pyrolysis furnaces, melting furnaces, etc. It is also possible to remove suspended particles in the exhaust gas.

【0031】[第2の実施の形態]図3は本実施の形態
の排ガス中の浮遊微粒子除去装置の概略図である。排ガ
ス中の浮遊微粒子を除去する浮遊微粒子除去装置であっ
て、上記排ガス(浮遊微粒子12を含む)を通気させ
て、上記浮遊微粒子12を捕獲する捕獲部13を内装し
て前室14と後室15とを備えた微粒子除去装置本体1
6と、該捕獲部13を通気した浄化排ガス17を排出す
る排出ライン18と、上記捕集部13で捕集した排ガス
中の微粒子表12面に触媒溶液19を噴霧して付着させ
る触媒溶液噴霧手段20と備えてなると共に、上記微粒
子除去装置本体16内の捕獲部13を通過することなく
捕獲部13の前室14側から上記排ガスライン18へ排
ガスを逃がすバイパスライン30と、上記微粒子除去装
置本体16内に水31を供給する水供給手段32とを設
けたものである。
[Second Embodiment] FIG. 3 is a schematic view of a device for removing suspended particulates in exhaust gas according to the present embodiment. A suspended particulates removing device for removing suspended particulates in exhaust gas, comprising a front chamber 14 and a rear chamber, which are provided with a trapping portion 13 for ventilating the exhaust gas (including suspended particulates 12) and capturing the suspended particulates 12. A fine particle removing device main body 1 including
6, a discharge line 18 for discharging the purified exhaust gas 17 aerated through the trap 13, and a catalyst solution spray for spraying and adhering the catalyst solution 19 on the surface 12 of the fine particles in the exhaust gas collected by the collector 13. Means 20 and a bypass line 30 for allowing exhaust gas to escape from the front chamber 14 side of the trap 13 to the exhaust gas line 18 without passing through the trap 13 in the main body 16 of the particulate remover; and the particulate remover. A water supply means 32 for supplying water 31 is provided in the main body 16.

【0032】上記バイパスライン21の開放により、捕
獲部13での目詰まりに対応できるが、上記捕獲部13
での触媒の析出があった場合には、水供給手段32から
水31を供給することで、捕獲部13で析出した触媒を
溶解させることができる。
By opening the bypass line 21, it is possible to deal with the clogging in the capturing unit 13, but the capturing unit 13
When the catalyst is deposited in (3), the catalyst deposited in the trap 13 can be dissolved by supplying the water 31 from the water supply means 32.

【0033】特に、捕獲部13の温度が高い場合に、触
媒溶液19を急激に噴霧した場合などに当該触媒が析出
する場合があり、これに迅速に対応することができる。
In particular, when the temperature of the capture unit 13 is high, the catalyst may be deposited when the catalyst solution 19 is rapidly sprayed, and this can be dealt with promptly.

【0034】また、本実施の形態において、図3に示す
ように、水タンク33を設け、該水タンク33から供給
ポンプ34で触媒液の供給配管26を介して、装置本体
16内に水31を供給するようにしてもよい。
Further, in the present embodiment, as shown in FIG. 3, a water tank 33 is provided, and water 31 is supplied from the water tank 33 to the inside of the apparatus main body 16 through the catalyst liquid supply pipe 26 by the supply pump 34. May be supplied.

【0035】[第3の実施の形態]図4は本実施の形態
の排ガス中の浮遊微粒子除去装置の概略図である。排ガ
ス中の浮遊微粒子を除去する浮遊微粒子除去装置であっ
て、上記排ガス(浮遊微粒子12を含む)を通気させ
て、上記浮遊微粒子12を捕獲する捕獲部13を内装し
て前室14と後室15とを備えた微粒子除去装置本体1
6と、該捕獲部13を通気した浄化排ガス17を排出す
る排出ライン18と、上記捕集部13で捕集した排ガス
中の微粒子表12面に触媒溶液19を噴霧して付着させ
る触媒溶液噴霧手段20と備えてなると共に、上記微粒
子除去装置本体16内の捕獲部13を通過することなく
捕獲部13の前室14側から上記排ガスライン18へ排
ガスを逃がすバイパスライン21と、上記微粒子除去装
置本体16から排ガスを排出する排出ライン18にドレ
ン手段41を設けたものである。
[Third Embodiment] FIG. 4 is a schematic view of a device for removing suspended particles in exhaust gas according to the present embodiment. A suspended particulates removing device for removing suspended particulates in exhaust gas, comprising a front chamber 14 and a rear chamber, which are provided with a trapping portion 13 for ventilating the exhaust gas (including suspended particulates 12) and capturing the suspended particulates 12. A fine particle removing device main body 1 including
6, a discharge line 18 for discharging the purified exhaust gas 17 aerated through the trap 13, and a catalyst solution spray for spraying and adhering the catalyst solution 19 on the surface 12 of the fine particles in the exhaust gas collected by the collector 13. Means 20 and a bypass line 21 for allowing exhaust gas to escape from the front chamber 14 side of the trap 13 to the exhaust gas line 18 without passing through the trap 13 in the main body 16 of the particulate remover; and the particulate remover. The drain means 41 is provided in the discharge line 18 for discharging the exhaust gas from the main body 16.

【0036】上記ドレン手段41はドレン内部に鉛直方
向に仕切り板42を設けた容器本体43とドレン排出ラ
イン44とからなり、微粒子が除去された浄化排ガス1
7を仕切り板42に衝突させることで、排ガス中に混入
する微量の触媒溶液19を分離させることができる。分
離された触媒溶液19はドレン排出ライン44を介して
触媒回収タンク30へ戻すようにしている。
The drain means 41 comprises a container body 43 having a partition plate 42 provided in the drain in the vertical direction and a drain discharge line 44.
By colliding 7 with the partition plate 42, a small amount of the catalyst solution 19 mixed in the exhaust gas can be separated. The separated catalyst solution 19 is returned to the catalyst recovery tank 30 via the drain discharge line 44.

【0037】なお、触媒除去装置の前流側において、ア
ンモニア脱硝手段を設けた場合に、脱硝で使用するアン
モニアにより硫酸水素アンモニウム(NH4 HSO3
が含まれる場合があるが、この硫酸アンモニウムも上記
ドレン手段41で分離することができる。この硫酸アン
モウニウムが触媒回収タンク内の触媒溶液19を中和す
ることになるが、pH計等により触媒溶液の監視を行
い、必要に応じて新規触媒を補充することでこれを解消
するようにすればよい。
When ammonia denitration means is provided on the upstream side of the catalyst removing device, ammonium hydrogensulfate (NH 4 HSO 3 ) is changed by the ammonia used for denitration.
However, this ammonium sulfate can also be separated by the drain means 41. This ammonium sulfate neutralizes the catalyst solution 19 in the catalyst recovery tank, but this should be eliminated by monitoring the catalyst solution with a pH meter or the like and supplementing with a new catalyst as necessary. Good.

【0038】また、硫酸アンモニウムの配管での析出を
防止するために、微粒子除去装置からドレン手段41ま
での排ガスライン18を高温(200℃以上)で保温し
て析出を防止するようにし、上記ドレン手段41で積極
的に落とすようにすればよい。
In order to prevent ammonium sulfate from depositing in the pipe, the exhaust gas line 18 from the fine particle removing device to the drain means 41 is kept at a high temperature (200 ° C. or higher) to prevent the deposit. It should be positively dropped at 41.

【0039】また、上記ドレン手段41を冷却する冷却
手段を設け、ドレン捕集効率を向上させるようにしても
よい。
A cooling means for cooling the drain means 41 may be provided to improve the drain collection efficiency.

【0040】また、微粒子が除去された浄化排ガス17
を仕切り板42に衝突させる仕切り板41の代わりに金
網等の積層体を設けるようにしてもよく、さらに、仕切
り板41に複数細孔を設け、この細孔が互い違いとなる
ように仕切り板41を鉛直軸方向と直交するように複数
積層させてガス流路を変化させるようにして、ドレン捕
集効率を向上させるようにしてもよい。
Purified exhaust gas 17 from which fine particles have been removed
A laminated body such as a wire mesh may be provided in place of the partition plate 41 that causes the partition plate 42 to collide with the partition plate 42. Further, the partition plate 41 is provided with a plurality of pores, and the partition plates 41 are arranged so that the pores are staggered. May be laminated so as to be orthogonal to the vertical axis direction and the gas flow path may be changed to improve the drain collection efficiency.

【0041】[0041]

【発明の効果】以上、説明したように本発明によれば、
上記触媒液を噴霧する際又は前室と後室との間で圧力変
動があった際に、バイパスラインを開放して、捕獲部の
目詰まりを防止するようにしている。
As described above, according to the present invention,
When spraying the catalyst liquid or when there is a pressure change between the front chamber and the rear chamber, the bypass line is opened to prevent clogging of the trap portion.

【0042】また、微粒子除去装置内に水を供給するよ
うにしたので、上記捕獲部での触媒の析出があった場合
に触媒を溶解させることができる。
Further, since water is supplied into the fine particle removing device, the catalyst can be dissolved in the case where the catalyst is deposited in the capturing section.

【0043】さらに、微粒子除去装置本体から排ガスを
排出する排出ラインにドレン手段を設けたので、微粒子
が除去された浄化排ガス中に混入する微量の触媒溶液を
分離させることができる。なお、分離された触媒溶液は
再利用することができる。
Further, since the drain means is provided in the discharge line for discharging the exhaust gas from the main body of the fine particle removing apparatus, it is possible to separate a minute amount of the catalyst solution mixed in the purified exhaust gas from which the fine particles have been removed. The separated catalyst solution can be reused.

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

【図1】第1の実施の形態にかかる浮遊微粒子除去装置
の概略図である。
FIG. 1 is a schematic diagram of an apparatus for removing suspended particles according to a first embodiment.

【図2】浮遊微粒子に触媒液が被覆する状態を示す概略
図である。
FIG. 2 is a schematic diagram showing a state in which suspended particulates are coated with a catalyst liquid.

【図3】第2の実施の形態にかかる浮遊微粒子除去装置
の概略図である。
FIG. 3 is a schematic view of a suspended particle removing apparatus according to a second embodiment.

【図4】第3の実施の形態にかかる浮遊微粒子除去装置
の概略図である。
FIG. 4 is a schematic view of a suspended particle removing device according to a third embodiment.

【符号の説明】[Explanation of symbols]

11 排ガス 12 浮遊微粒子 13 捕獲部 14 前室 15 後室 16 微粒子除去装置本体 17 浄化排ガス 18 排出ライン 19 触媒溶液 20 触媒溶液噴霧手段 21 回収タンク 22 フィルタ 23 冷却手段 24 供給水 25 残渣 26 供給配管 30 回収タンク 31 水 32 水供給手段 33 水タンク 34 供給ポンプ 41 ドレン手段 11 exhaust gas 12 suspended particles 13 Capture Department 14 anteroom 15 Rear room 16 Particle removal device body 17 Purified exhaust gas 18 discharge line 19 Catalyst solution 20 catalyst solution spraying means 21 Recovery tank 22 filters 23 Cooling means 24 Supply water 25 residue 26 Supply piping 30 recovery tank 31 water 32 Water supply means 33 water tank 34 Supply pump 41 Drain means

フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) B01D 47/06 F01N 3/04 D 4D064 53/94 3/18 F F01N 3/04 B01D 53/36 104B 3/18 35/14 101 (72)発明者 藤岡 祐一 長崎県長崎市深堀町五丁目717番1号 三 菱重工業株式会社長崎研究所内 (72)発明者 阿部 幸浩 神奈川県相模原市田名3000番地 三菱重工 業株式会社汎用機・特車事業本部内 (72)発明者 小田 裕司 長崎県長崎市深堀町五丁目717番1号 三 菱重工業株式会社長崎研究所内 (72)発明者 遠藤 浩之 長崎県長崎市深堀町五丁目717番1号 三 菱重工業株式会社長崎研究所内 Fターム(参考) 3G090 AA01 AA06 BA08 CB22 3G091 AA02 AA04 AA06 AA18 AB01 AB13 AB15 BA07 CA12 CA15 GB02W GB03W HA14 HB03 4D031 AB02 AB23 BA03 BA07 BB04 DA01 DA04 EA01 4D032 AA03 AB07 AC01 BA06 BB07 DA10 4D048 AA14 AA18 AB01 BA01Y BA02Y BA14Y BA15Y CC26 CC41 DA01 DA02 DA07 DA20 EA08 4D064 AA40 BK05 DE01 Front page continuation (51) Int.Cl. 7 Identification code FI theme code (reference) B01D 47/06 F01N 3/04 D 4D064 53/94 3/18 F F01N 3/04 B01D 53/36 104B 3/18 35 / 14 101 (72) Inventor Yuichi Fujioka 5-717-1, Fukahori-cho, Nagasaki-shi, Nagasaki Sanhishi Heavy Industries Ltd. Nagasaki Research Institute (72) Inventor, Yukihiro Abe 3000, Tana, Sagamihara, Kanagawa Mitsubishi Heavy Industries, Ltd. General-purpose machine / special vehicle business headquarters (72) Inventor Yuji Oda 5-717-1, Fukahori-cho, Nagasaki-shi, Nagasaki Sanryo Heavy Industries Co., Ltd. Nagasaki Research Institute (72) Inventor Hiroyuki Endo 5-chome, Fukahori-cho, Nagasaki-shi, Nagasaki No. 717-1 Sanryishi Heavy Industries Co., Ltd. Nagasaki Research Laboratory F-term (reference) 3G090 AA01 AA06 BA08 CB22 3G091 AA02 AA04 AA06 AA18 AB01 AB13 AB15 BA07 CA12 CA15 GB02W GB03W HA14 HB03 4D031 AB02 AB23 BA03 BA07 BB04 DA01 DA04 A01 EA01 4A03 BA06 BB07 DA10 4D048 AA14 AA18 AB01 BA01Y BA02Y BA14Y BA15Y CC26 CC4 1 DA01 DA02 DA07 DA20 EA08 4D064 AA40 BK05 DE01

Claims (13)

【特許請求の範囲】[Claims] 【請求項1】 排ガス中の浮遊微粒子を除去する浮遊微
粒子除去装置であって、 上記排ガスを通気させて、上記浮遊微粒子を捕獲する捕
獲部を内装して前室と後室とを備えた微粒子除去装置本
体と、 該捕獲部を通気した排ガスを排出する排出ラインと、 上記捕集部で捕集した排ガス中の微粒子表面に触媒溶液
を付着させる触媒付着手段と備えてなると共に、 上記微粒子除去装置本体内の捕獲部を通過することなく
捕獲部の前室側から排ガスラインへ排ガスを逃がすバイ
パスラインを設けたことを特徴とする排ガス中の浮遊微
粒子除去装置。
1. A suspended particulates removing apparatus for removing suspended particulates in exhaust gas, which comprises a front chamber and a rear chamber in which a trapping unit for ventilating the exhaust gas and capturing the suspended particulates is installed. The apparatus includes a main body of a removing device, an exhaust line for exhausting the exhaust gas ventilated through the trapping section, and a catalyst adhering means for adhering a catalyst solution to the surface of the fine particles in the exhaust gas trapped by the trapping section. A device for removing suspended particulates in exhaust gas, comprising a bypass line for allowing exhaust gas to escape from the front chamber side of the capture unit to the exhaust gas line without passing through the capture unit in the apparatus body.
【請求項2】 請求項1において、 上記触媒溶液がアルカリ金属或いはアルカリ土類金属の
少なくとも1種を含む触媒を含有してなり、上記捕獲部
の表面で捕集された微粒子を排ガス通気時に触媒燃焼さ
せ、除去することを特徴とする浮遊微粒子除去装置。
2. The catalyst solution according to claim 1, wherein the catalyst solution contains a catalyst containing at least one kind of alkali metal or alkaline earth metal, and the fine particles trapped on the surface of the trapping part are used as a catalyst when ventilating exhaust gas. A device for removing suspended particles characterized by burning and removing.
【請求項3】 請求項1又は2において、 上記微粒子除去装置本体内の捕獲部の後室側から触媒溶
液を排出する排出ラインと、触媒溶液を貯蔵する触媒溶
液貯蔵手段とを備えたことを特徴とする浮遊微粒子除去
装置。
3. The discharge line for discharging the catalyst solution from the rear chamber side of the capturing section in the main body of the fine particle removing apparatus according to claim 1, and a catalyst solution storing means for storing the catalyst solution. A device for removing suspended particulates.
【請求項4】 請求項3において、 上記触媒溶液貯蔵手段から触媒溶液を触媒付着手段に送
給する送給ラインを設けたことを特徴とする浮遊微粒子
除去装置。
4. The suspended particle removing device according to claim 3, further comprising a feed line for feeding the catalyst solution from the catalyst solution storage means to the catalyst adhering means.
【請求項5】 請求項3において、 上記触媒溶液貯蔵手段内の触媒溶液を冷却する冷却手段
を設けたことを特徴とする浮遊微粒子除去装置。
5. The suspended particulates removing device according to claim 3, further comprising a cooling means for cooling the catalyst solution in the catalyst solution storage means.
【請求項6】 請求項4において、 上記送給ラインに冷却フィンを設け、触媒溶液を冷却す
ることを特徴とする浮遊微粒子除去装置。
6. The suspended particle removing device according to claim 4, wherein a cooling fin is provided in the feeding line to cool the catalyst solution.
【請求項7】 請求項1において、 上記微粒子除去装置本体内の捕獲部の後室内にフィルタ
を設けてなり、触媒溶液を濾過することを特徴とする浮
遊微粒子除去装置。
7. The suspended particulates removing apparatus according to claim 1, wherein a filter is provided in the rear chamber of the capturing section in the particulates removing apparatus main body to filter the catalyst solution.
【請求項8】 請求項1において、 上記微粒子除去装置本体から排ガスを排出する排出ライ
ンにドレン手段を設けたことを特徴とする浮遊微粒子除
去装置。
8. The suspended particulates removing apparatus according to claim 1, wherein a drain means is provided in an exhaust line for exhausting the exhaust gas from the particulates removing apparatus main body.
【請求項9】 請求項8において、 上記ドレン手段で捕集した触媒溶液貯蔵手段で回収する
回収ラインを設けたことを特徴とする浮遊微粒子除去装
置。
9. The suspended particulate removal device according to claim 8, further comprising a recovery line for recovering the catalyst solution storage means collected by the drain means.
【請求項10】 請求項1乃至9のいずれか一の排ガス
中の浮遊微粒子除去装置を用い、排ガスを通気する際に
バイパスラインを開放することを特徴とする排ガス中の
浮遊微粒子除去方法。
10. A method for removing suspended particulates in exhaust gas, which comprises using the apparatus for removing suspended particulates in exhaust gas according to claim 1 and opening a bypass line when ventilating the exhaust gas.
【請求項11】 請求項1乃至9のいずれか一の排ガス
中の浮遊微粒子除去装置を用い、微粒子除去装置本体内
の捕獲部で仕切られた前室と後室との圧力差を測定し、
所定圧力差以上となった場合に、排ガスを一時的に通気
するバイパスラインを開放することを特徴とする排ガス
中の浮遊微粒子除去方法。
11. A device for removing suspended particulates in exhaust gas according to claim 1, wherein a pressure difference between a front chamber and a rear chamber partitioned by a trap in the body of the particulate removal device is measured.
A method for removing suspended particulates in exhaust gas, which comprises opening a bypass line for temporarily venting exhaust gas when a pressure difference exceeds a predetermined value.
【請求項12】 排ガスを浄化する排ガス処理システム
であって、排ガスの煙道に介装され、排ガス中の浮遊微
粒子を分解処理する請求項1乃至9の浮遊微粒子除去装
置を有することを特徴とする排ガス処理システム。
12. An exhaust gas treatment system for purifying exhaust gas, comprising the suspended particle removing device according to claim 1, which is installed in a flue of the exhaust gas and decomposes suspended particles in the exhaust gas. Exhaust gas treatment system.
【請求項13】 請求項12において、 上記微粒子除去装置の前流側又は後流側に排ガス中の窒
素酸化物を分解処理する脱硝装置を有することを特徴と
する排ガス処理システム。
13. The exhaust gas treatment system according to claim 12, further comprising a denitration device for decomposing nitrogen oxides in the exhaust gas, on the upstream side or the downstream side of the fine particle removing device.
JP2002087723A 2002-03-27 2002-03-27 Apparatus and method for removing suspended particulate matter in exhaust gas Expired - Fee Related JP4215994B2 (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100568699B1 (en) * 2004-02-23 2006-04-11 정하영 The purifier and method for the filert off smoke gas

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR102241219B1 (en) * 2019-02-22 2021-04-19 주식회사 유진테크 Air purifier

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100568699B1 (en) * 2004-02-23 2006-04-11 정하영 The purifier and method for the filert off smoke gas

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