JP2006233846A - Exhaust gas treatment device - Google Patents

Exhaust gas treatment device Download PDF

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Publication number
JP2006233846A
JP2006233846A JP2005048871A JP2005048871A JP2006233846A JP 2006233846 A JP2006233846 A JP 2006233846A JP 2005048871 A JP2005048871 A JP 2005048871A JP 2005048871 A JP2005048871 A JP 2005048871A JP 2006233846 A JP2006233846 A JP 2006233846A
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exhaust gas
reactor
guide rail
porous
filter device
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Takeshi Hirota
健 広田
Kazuki Kobayashi
和樹 小林
Satoki Sasaki
郷紀 佐々木
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Mitsubishi Power Ltd
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Babcock Hitachi KK
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Abstract

<P>PROBLEM TO BE SOLVED: To provide an improved exhaust gas treatment device capable of easily exchanging a specific filter device (crossing honeycomb) by fewer people (or one person), without using a machine such as a crane. <P>SOLUTION: The exhaust gas treatment device has a reactor 2 disposed to an exhaust gas duct 1 to be detachable. The reactor 2 comprises: a filter device 5 in which a pair of a porous corrugated plate 3 and a porous flat plate 4 carrying an exhaust gas cleaning catalyst thereon is a base unit, molded bodies formed by laminating the porous corrugated plates so that corrugated plate ridge line of the porous corrugated plates are laminated alternately orthogonal, one face of side faces orthogonal to the corrugated plate ridge lines of the molded bodies or neighboring two faces is/are sealed, and exhaust gas inlet passages and exhaust gas outlet passages are formed between the porous corrugated plate through the porous flat plates; an inner case 6 holding the filter device 5; a guide rail 7 disposed integrally with the inner case 6; and a guide rail support member 8 disposed to an inner wall of the reactor so that the guide rail support member 8 fits the guide rail 7. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

本発明は、自動車用および定置用の排ガス中に含まれる粒状物質PMを除去するための排ガス処理装置に係り、特にエンジン始動直後の煤を系外に排出せずに、粒状物質除去用フィルタ(以下、DPFと称することがある)で捕捉、固定、燃焼除去し、排ガス温度が上昇した時には低差圧になり、長期連続運転可能な排ガス処理装置に関するものである。   The present invention relates to an exhaust gas treatment apparatus for removing particulate matter PM contained in automobile and stationary exhaust gas, and more particularly to a particulate matter removing filter ( In the following, the present invention relates to an exhaust gas treatment apparatus which is captured, fixed, burned and removed by DPF) and has a low differential pressure when the exhaust gas temperature rises, and which can be operated continuously for a long time.

最近、内燃機関である分散型電源用ディーゼルエンジンを利用したコジェネレーションシステムや自動車が都市部を中心として増加しており、これらの排ガスに対して、PM、NOxの排出規制が適用され、かつ地域によっては強化されるため、大型プラント同様に排ガス処理装置の設置が急務となっている。特にディーゼル排ガス処理装置に用いられるDPF(ディーゼルパティキュレートフィルタ)は排ガス中に含まれるPMを除去するもので重要である。   Recently, cogeneration systems and automobiles that use a diesel engine for distributed power source, which is an internal combustion engine, are increasing mainly in urban areas. PM and NOx emission regulations are applied to these exhaust gases, and the region However, it is urgently necessary to install an exhaust gas treatment device as in large plants. In particular, a DPF (diesel particulate filter) used in a diesel exhaust gas treatment apparatus is important because it removes PM contained in exhaust gas.

本発明者らは、本願の先願である特願2003−393879において、排ガス浄化触媒が担持された多孔質波板と多孔質平板の対を基本単位とし、該多孔質波板の波板稜線が交互に直交するように積層された成形体(以下、交差ハニカムと称することがある)を有し、該成形体の前記波板稜線と直交する側面の一つの面、または互いに隣接する二つの面がシールされ、前記多孔質平板を介して前記多孔質波板との間にそれぞれ排ガスの流入経路と流出経路が形成されるPM含有排ガス浄化用フィルタ装置を提案した。このフィルタ装置は、排ガス処理と、フィルタに蓄積した灰のパージを行なうために、排ガスの入口部、出口部(1または2箇所)およびパージ出口を遮断する必要がある。前述の交差ハニカムは、通常の排ガス処理時には、排ガス入口部から入ったガス中のPMはフィルタ処理され、排ガス出口部から排出される(図3参照)。交差ハニカム内に灰が蓄積した場合は、排ガスパージ出口部のバルブ(常時閉)を開けることによって、蓄積した灰をパージ排出することができる。これらの操作を排ガスのリークなしで行うためには、各部のシールを完全にする必要がある。各部のシールが不完全であると、排ガスがリークし、有害なPMを排出することになる。そこで、一旦、前記交差ハニカムをインナーケースに設置し、インナーケースを反応器の中にシール材を用いて、反応器内に固定した後、その反応器を排ガス管に設置する方法が用いられる。交差ハニカムが設置されたインナーケースは、排ガスの入口部と出口およびパージ出口の各四面端のシール材と反応器の接触部を目視で確認しながら、反応器に設置し、排ガス管内に取り付けられる。   In Japanese Patent Application No. 2003-393879, which is a prior application of the present application, the inventors have a basic unit of a pair of a porous corrugated plate and a porous flat plate on which an exhaust gas purification catalyst is supported, and corrugated plate ridge lines of the porous corrugated plate. Are formed so as to be alternately perpendicular to each other (hereinafter sometimes referred to as a crossed honeycomb), and one of the side surfaces orthogonal to the corrugated ridge line of the formed body, or two adjacent to each other A PM-containing exhaust gas purifying filter device in which a surface is sealed and an exhaust gas inflow path and an outflow path are formed between the porous flat plate and the porous corrugated plate has been proposed. In order to perform exhaust gas treatment and purge of ash accumulated in the filter, this filter device needs to shut off the exhaust gas inlet portion, the outlet portion (one or two places), and the purge outlet. In the above-described crossed honeycomb, during normal exhaust gas treatment, PM in the gas entering from the exhaust gas inlet is filtered and discharged from the exhaust gas outlet (see FIG. 3). When ash accumulates in the crossed honeycomb, the accumulated ash can be purged and discharged by opening a valve (normally closed) at the exhaust gas purge outlet. In order to perform these operations without exhaust gas leakage, it is necessary to completely seal each part. If the seal of each part is incomplete, the exhaust gas leaks and harmful PM is discharged. Therefore, a method is used in which the crossed honeycomb is once installed in the inner case, the inner case is fixed in the reactor using a sealing material in the reactor, and then the reactor is installed in the exhaust gas pipe. The inner case in which the cross honeycomb is installed is installed in the reactor and installed in the exhaust gas pipe while visually checking the contact portions of the sealing material and the reactor at the four sides of the exhaust gas inlet and outlet and purge outlet. .

このような反応器を用いてPM濃度が高い排ガスの処理や、連続的な低負荷運転を行った場合、1〜数年経過すると、交差ハニカム内部に蓄積した鉄錆や灰に起因する差圧上昇が発生する場合があった。また排ガス処理時間が短くても、まれにエンジン振動等により交差ハニカムがインナーケースからずれて、排ガスがリークする場合があった。このような場合には、交差ハニカムを交換する必要があるが、交換のためにはクレーン等を用いて反応器を取外し、さらに反応器から交差ハニカムを取り外すという煩雑な作業が必要であった。   When exhaust gas with high PM concentration or continuous low-load operation is performed using such a reactor, after 1 to several years, the differential pressure due to iron rust and ash accumulated inside the cross honeycomb An increase could occur. Even when the exhaust gas treatment time is short, the cross honeycomb may be displaced from the inner case due to engine vibration or the like, and the exhaust gas may leak. In such a case, it is necessary to replace the crossed honeycomb. However, for the replacement, a complicated operation of removing the reactor using a crane or the like and further removing the crossed honeycomb from the reactor is necessary.

本発明の課題は、上記特定のフィルタ装置(交差ハニカム)を、クレーン等の機械を用いずに、少人数(または一人)で容易に交換することができる改善された排ガス処理装置を提供することにある。   An object of the present invention is to provide an improved exhaust gas treatment device that can easily replace the specific filter device (crossing honeycomb) with a small number of people (or one person) without using a machine such as a crane. It is in.

上記課題を達成するため、本発明者らは、反応器を配管に設置したまま、交差ハニカムの交換が可能なシステムとして、排ガス入口、出口およびパージ出口の流路を設けた反応器を用い、交差ハニカムのインナーケースにガイドレールを設けてスライド式にして反応器に直接、挿入/取出し可能にすることにより、容易に交差ハニカムの交換ができることを見出した。   In order to achieve the above object, the present inventors used a reactor provided with a flow path of an exhaust gas inlet, an outlet and a purge outlet as a system capable of exchanging crossed honeycombs while the reactor is installed in a pipe. It was found that the crossed honeycomb can be easily replaced by providing a guide rail on the inner case of the crossed honeycomb so that it can be inserted into and removed from the reactor directly.

本願で特許請求される発明は以下のとおりである。
(1)排ガス管路に着脱可能に設けられた反応器を有する排ガス処理装置であって、該反応器は、排ガス浄化触媒が担持された多孔質波板と多孔質平板の対を基本単位とし、該多孔質波板の波板稜線が交互に直交するように積層された成形体を有し、該成形体の前記波板稜線と直交する側面の一つの面、または互いに隣接する二つの面がシールされ、前記多孔質平板を介して前記多孔質波板との間にそれぞれ排ガスの流入経路と流出経路が形成されるフィルタ装置と、該フィルタ装置を保持するインナーケースと、該インナーケースに一体的に設けられたガイドレールと、該ガイドレールに適合するように排ガス管路内壁に設けられたガイドレール支持部材とを有することを特徴とする装置。
(2)前記フィルタ装置の排ガス流出経路を経由するフィルタ管路と、前記フィルタ装置の排ガスが流入する側面と対向する面を開放して排ガスにより該フィルタ装置をパージするためのパージ用管路と、前記二つの管路のいずれかを選択するための切替弁とをさらに有することを特徴とする(1)記載の排ガス浄化装置。
(3)前記排ガス管路は、それぞれ前記反応器が配置された分岐管を有し、該分岐管は、それぞれ前記パージ用管路およびフィルタ管路に連結されていることを特徴とする(2)記載の装置。
(4)前記ガイドレールおよび前記ガイドレール支持部材が断面コ字状ないし鍵状であり、これらの間にパッキンまたは緩衝材が挟持されていることを特徴とする(1)ないし(3)のいずれかに記載の装置。
The invention claimed in the present application is as follows.
(1) An exhaust gas treatment apparatus having a reactor detachably provided in an exhaust gas conduit, wherein the reactor is based on a pair of a porous corrugated plate and a porous flat plate carrying an exhaust gas purification catalyst. And having a molded body laminated such that corrugated ridge lines of the porous corrugated sheet are alternately orthogonal to each other, one surface of the side surface orthogonal to the corrugated ridge line of the molded body, or two surfaces adjacent to each other A filter device in which an exhaust gas inflow path and an outflow path are formed between the porous flat plate and the porous corrugated plate via the porous flat plate, an inner case for holding the filter device, and an inner case An apparatus comprising: a guide rail provided integrally; and a guide rail support member provided on an inner wall of the exhaust gas pipe so as to be fitted to the guide rail.
(2) a filter line passing through the exhaust gas outflow path of the filter device, and a purge line for purging the filter device with the exhaust gas by opening a surface opposite to the side surface of the filter device into which the exhaust gas flows. The exhaust gas purifier according to (1), further comprising a switching valve for selecting one of the two pipe lines.
(3) Each of the exhaust gas pipes has a branch pipe in which the reactor is arranged, and the branch pipes are connected to the purge pipe line and the filter pipe line, respectively (2 ) The device described.
(4) The guide rail and the guide rail support member each have a U-shaped or key-shaped cross section, and a packing or cushioning material is sandwiched between them. A device according to the above.

本発明によれば、反応器を配管から取外さず、容易に交差ハニカムの交換を行なうことができ、メンテナンスが容易で、かつガスリークの発生し難い排ガス処理装置を得ることができる。   According to the present invention, it is possible to obtain an exhaust gas treatment apparatus that can easily replace a crossed honeycomb without removing the reactor from the piping, is easy to maintain, and hardly causes gas leakage.

図1は、本発明の排ガス処理装置の側面図、図2はその正面図である。この装置は、排ガス管路1の分岐管路にそれぞれ着脱可能に設けられた反応器2を有し、該反応器2は、排ガス浄化触媒(例えば排ガス中のNOをNO2に酸化する機能を有する白金などの貴金属触媒)が担持された多孔質波板3と多孔質平板4の対を基本単位とし、該多孔質波板の波板稜線が交互に直交するように積層された成形体を有し、該成形体の前記波板稜線と直交する側面の一つの面がシールされ、前記多孔質平板を介して前記多孔質波板との間にそれぞれ排ガスの流入経路と流出経路が形成されるフィルタ装置5と、該フィルタ装置を保持するインナーケース6と、該インナーケースに一体的に設けられたガイドレール7と、該ガイドレール7に適合するように排ガス管路内壁に設けられたガイドレール支持部材8と、前記フィルタ装置5の排ガス流出経路を経由するフィルタ管路9と、前記フィルタ装置5の排ガスが流入する側面と対向する面を開放して排ガスにより該フィルタ装置をパージするためのパージ用管路10と、前記二つの管路のいずれかを選択するための切替弁11とを有する。上記フィルタ管路9は、フィルタ装置(交差DPF)5の二方向の排ガス出口側面と連通する分岐管(4本)と、これらが後流で集合したものであり、またパージ用管路10は、前記フィルタ装置5の排ガス入口側の側面と対向する面に連通する分岐管(3本)と、これらが後流で集合したものである。パージ用管路10には、上記二つの管路9および10のいずれかを選択するための切替弁(開閉弁)11が設けられている。   FIG. 1 is a side view of the exhaust gas treatment apparatus of the present invention, and FIG. 2 is a front view thereof. This apparatus has a reactor 2 detachably provided in each branch pipe of the exhaust gas pipe 1, and the reactor 2 has a function of oxidizing an exhaust gas purification catalyst (for example, NO in exhaust gas to NO 2). It has a molded body in which a pair of a porous corrugated plate 3 and a porous flat plate 4 on which a noble metal catalyst (such as platinum) is supported is laminated so that corrugated ridges of the porous corrugated plate are alternately orthogonal. Then, one surface of the side surface orthogonal to the corrugated ridge line of the molded body is sealed, and an exhaust gas inflow path and an outflow path are formed between the porous corrugated plate and the porous corrugated plate, respectively. Filter device 5, inner case 6 that holds the filter device, guide rail 7 that is provided integrally with the inner case, and guide rail that is provided on the inner wall of the exhaust gas pipe so as to fit the guide rail 7 A support member 8; A filter line 9 that passes through an exhaust gas outflow path of the filter device 5, and a purge line 10 for opening the surface of the filter device 5 that faces the side surface into which the exhaust gas flows in and purging the filter device with the exhaust gas, And a switching valve 11 for selecting one of the two pipe lines. The filter pipe 9 is a branch pipe (four pipes) communicating with the two-side exhaust gas outlet side surfaces of the filter device (cross DPF) 5 and these are gathered in the downstream, and the purge pipe 10 is The branch pipes (three pipes) communicating with the side of the filter device 5 facing the side face on the exhaust gas inlet side, and these are assembled in the wake. The purge line 10 is provided with a switching valve (open / close valve) 11 for selecting one of the two lines 9 and 10.

切替弁11は、通常運転時に閉、パージ時に開となる。フィルタ管路9は後流部で集合した部分以降に開閉弁を設置しなくても良いが、パージ効果をより高めるためには、設置した方が良い(パージ時に閉)。   The switching valve 11 is closed during normal operation and opened during purging. The filter pipe 9 does not need to be provided with an on-off valve after the part gathered in the wake part, but in order to further enhance the purge effect, it is better to install it (closed at the time of purging).

図4は、本発明に用いる反応器2の説明図である。この反応器2は、フィルタ装置(交差ハニカム)5を保持するインナーケース6と、該インナーケース6に一体的に設けられたガイドレール7と、インナーケース支持板12とからなる。フィルタ装置5の上下二方向(図面上から見て)の排ガス出口流路は分岐管を経て図1のパージ用管路10に連通する。反応器2を装着する分岐管の内壁には、前記インナーケース6のガイドレール7に適合するガイドレール支持部材8が設けられている。   FIG. 4 is an explanatory diagram of the reactor 2 used in the present invention. The reactor 2 includes an inner case 6 that holds a filter device (crossed honeycomb) 5, a guide rail 7 that is provided integrally with the inner case 6, and an inner case support plate 12. The exhaust gas outlet passage in the upper and lower two directions (viewed from the drawing) of the filter device 5 communicates with the purge conduit 10 in FIG. A guide rail support member 8 adapted to the guide rail 7 of the inner case 6 is provided on the inner wall of the branch pipe to which the reactor 2 is mounted.

図1において、反応器2を分岐管に装着するには、図4に示すようにインナーケース6に収納されたフィルタ装置5をインナーケース支持板12と共に持ち上げ、分岐管の所定の開口部からガイドレール支持部材8にガイドレール7の先端を合致させ、インナーケース支持板12ごと前方にスライドさせて分岐管内に装入し、固着すればよい。   In FIG. 1, in order to attach the reactor 2 to the branch pipe, as shown in FIG. 4, the filter device 5 housed in the inner case 6 is lifted together with the inner case support plate 12 and guided from a predetermined opening of the branch pipe. What is necessary is just to make the front-end | tip of the guide rail 7 agree | coincide with the rail support member 8, to slide ahead with the inner case support plate 12, to insert in a branch pipe, and to fix.

図5は、多孔質波板と多孔質平板が積層された前記成形体の側面の互いに隣接する二つの面がシールされたフィルタ装置5Aを二つの分岐管内に設置する以外は、図1の実施例と同様にした排ガス処理装置の側面図である。   FIG. 5 is the same as FIG. 1 except that the filter device 5A in which two adjacent surfaces of the side surface of the molded body in which a porous corrugated plate and a porous flat plate are laminated is sealed is installed in two branch pipes. It is a side view of the exhaust gas processing apparatus made the same as an example.

図6は、分岐管1Aに設置させる反応器2のガイドレール7とその支持部材8の種々の実施例を示すもので、断面I字状、コ字状、L字状、鍵状等の形状が好ましく、特にコ字状ないし鍵状がシール性の点で好ましく、またパッキンまたは緩衝材13をこれらの間に挟持する構造とすることが好ましい。このような構造とすることにより、反応器2と排ガス管の間のシールを確実にし、ガス漏れを防ぐことができる。   FIG. 6 shows various embodiments of the guide rail 7 and the supporting member 8 of the reactor 2 installed in the branch pipe 1A, and has a cross-sectional I shape, a U shape, an L shape, a key shape, and the like. In particular, a U-shape or a key shape is preferable in terms of sealing properties, and it is preferable to have a structure in which a packing or cushioning material 13 is sandwiched between them. By setting it as such a structure, the seal | sticker between the reactor 2 and an exhaust gas pipe can be ensured, and a gas leak can be prevented.

図7は、本発明の反応器2を排ガス管1Aに装着した概略平面図を示すが、インナーケース支持板12には把手14が設けられ、また反応器2の排ガス管1Aと接する後面には断熱材支持部17により断熱材15が、および開口部周縁にはパッキン16が設けられ、断熱材とともにシールを完全にしている。   FIG. 7 shows a schematic plan view in which the reactor 2 of the present invention is mounted on the exhaust gas pipe 1A. The inner case support plate 12 is provided with a handle 14, and on the rear surface of the reactor 2 in contact with the exhaust gas pipe 1A. A heat insulating material 15 is provided by the heat insulating material support portion 17 and a packing 16 is provided at the periphery of the opening, and the seal is completed together with the heat insulating material.

上記実施例によれば、ガイドレールをスライドさせることによって、交差ハニカムの挿入/取出しおよび固定が容易になる。また交差ハニカムと配管の接合部である、配管内部奥側面、ガイドレールおよび間口周辺には、気密を保つためにパッキンを設置したことにより、通ガス時に交差ハニカムの入口、出口およびパージ出口のガスリークを防ぐことが可能となる。   According to the above-described embodiment, the insertion / removal and fixing of the intersecting honeycomb are facilitated by sliding the guide rail. In addition, gas is leaked at the inlet, outlet, and purge outlet of the crossed honeycomb when gas is passed by installing packing to keep airtightness around the inner side of the pipe, the guide rail, and the front opening, which is the joint between the crossed honeycomb and the pipe. Can be prevented.

なお、上記実施例において、反応器2は、排ガス配管に対して左右から取付け/取出しする構造、および上下から取付け/取出しする構造のどちらを用いてもかまわない。またガイドレールおよびガイドレール支持部材は、反応器をスライドさせて着脱できる構造であれば、反応器側に上記支持部材を設けてもよい。   In addition, in the said Example, the reactor 2 may use either the structure attached / taken out from right and left with respect to exhaust gas piping, or the structure attached / taken out from upper and lower sides. The guide rail and the guide rail support member may be provided on the reactor side as long as the guide rail and the guide rail support member can be attached and detached by sliding the reactor.

以下、既設のフィルタ装置(交差ハニカム)を本発明の装置(反応器)に改造する実施例について説明するが、本発明は勿論、新設の装置にも適用できることは言うまでもない。
[実施例1]
本発明による定置ディ−ゼル排ガス処理システムの交差ハニカムDPFの交換実験を行った。発電能力500kWのディーゼルエンジンの排ガス出口に内径200mmΦの配管を設置し、排ガス出口から2.5m後流側の位置に反応器を取付けた。反応器(図3)は、入口400×400mm角、長さ300mmの交差ハニカム(図2)が、6個取付けられる構造である。各交差ハニカムへの流路は、内寸405×405mm角で、DPF取付け部には厚さ5mm、高さ40mm、長さ405mmのステンレス製のガイドレールを、280mm間隔で上下、各々二箇所(計四個)取付けた。反応器の交差ハニカムの取付け間口は402×302mmの長方形状に開口した。交換する交差ハニカムのインナーケースは、出口を支持する両端面(幅20mm)に厚さ5mm、高さ40mm、長さ405mmのガイドレールが設置され、挿入時の奥面後流側の端に厚さ5mm、高さ4mm、長さ405mmのパッキンずれ防止用の支持部を取付けた。さらに、挿入時の手前面には、取っ手および外周に厚さ5mm、幅50mmのパッキン押えおよび交差ハニカム固定用の支持部(ボルト固定)を取付けた。
既設の交差ハニカムのボルトを外して引抜いて取外し、各所要部にパッキンを取付けた交差ハニカムを挿入し、ボルト閉めを行った。一人で6個の交差ハニカムの交換に要した時間は約三時間で、取外し機械は不要であった。
Hereinafter, an example in which an existing filter device (crossed honeycomb) is modified to the device (reactor) of the present invention will be described, but it goes without saying that the present invention can be applied to a new device.
[Example 1]
An exchange experiment of the crossed honeycomb DPF of the stationary diesel exhaust gas treatment system according to the present invention was conducted. A pipe with an inner diameter of 200 mmΦ was installed at the exhaust gas outlet of a diesel engine with a power generation capacity of 500 kW, and a reactor was installed at a position 2.5 m behind the exhaust gas outlet. The reactor (FIG. 3) has a structure in which six crossing honeycombs (FIG. 2) having an inlet of 400 × 400 mm square and a length of 300 mm are attached. The flow path to each cross honeycomb is an inner dimension of 405 x 405 mm square, and the DPF mounting part is 5 mm thick, 40 mm high, and 405 mm long stainless steel guide rails at two locations (up and down at intervals of 280 mm) ( A total of four) were installed. The installation front of the crossing honeycomb of the reactor was opened in a rectangular shape of 402 × 302 mm. The inner case of the crossed honeycomb to be replaced has guide rails with a thickness of 5 mm, height of 40 mm, and length of 405 mm installed on both end faces (width 20 mm) that support the outlet. A 5 mm long, 4 mm high, and 405 mm long support for preventing packing slippage was attached. Further, a packing presser having a thickness of 5 mm and a width of 50 mm and a support for fixing the crossed honeycomb (bolt fixing) were attached to the front face of the hand at the time of insertion.
The existing cross-honeycomb bolts were removed and pulled out, and the cross-honeycomb with packings attached to each required portion was inserted, and the bolts were closed. The time required for exchanging six cross honeycombs by one person was about three hours, and no removal machine was required.

[実施例2]
実施例1と同様に定置ディ−ゼル排ガス処理システムの交差ハニカムDPFの交換実験を行った。発電能力180kWのディーゼルエンジンの排ガス出口に内径150mmΦの配管を設置し、排ガス出口から1.5m後流側の位置に反応器を取付けた。反応器(図3)は、入口400×400mm角、長さ300mmの交差ハニカムが、二個取付けられる構造である。実施例1と違い、出口が一箇所の交差ハニカムを用いた。各交差ハニカムへの流路は、内寸405×405mm角で、DPF取付け部には厚さ5mm、高さ40mm、長さ405mmのステンレス製のガイドレールを、280mm間隔で上下、各々二箇所(計四個)取付けた。反応器の交差ハニカムの取付け間口は402×302mmの長方形状に開口した。交換する交差ハニカムのインナーケースは、出口を支持する両端面(幅20mm)に厚さ5mm、高さ40mm、長さ405mmのガイドレールが設置され、挿入時の奥面後流側の端に厚さ5mm、高さ4mm、長さ405mmのパッキンずれ防止用の支持部を取付けた。さらに、挿入時の手前面には、取っ手および外周に厚さ5mm、幅50mmのパッキン押えおよび交差ハニカム固定用の支持部(ボルト固定)を取付けた。
既設の交差ハニカムのボルトを外して引抜いて取外し、各所要部にパッキンを取付けた交差ハニカムを挿入し、ボルトを行った。一人で二個の交差ハニカムの交換に要した時間は約一時間で、取外し機械は不要であった。
[Example 2]
In the same manner as in Example 1, an exchange experiment of the crossed honeycomb DPF of the stationary diesel exhaust gas treatment system was performed. A pipe with an inner diameter of 150 mmΦ was installed at the exhaust gas outlet of a diesel engine with a power generation capacity of 180 kW, and a reactor was installed at a position 1.5 m behind the exhaust gas outlet. The reactor (FIG. 3) has a structure in which two crossed honeycombs having an inlet of 400 × 400 mm square and a length of 300 mm are attached. Unlike Example 1, a crossed honeycomb with one exit was used. The flow path to each cross honeycomb is an inner dimension of 405 x 405 mm square, and the DPF mounting part is 5 mm thick, 40 mm high, and 405 mm long stainless steel guide rails at two locations (up and down at intervals of 280 mm) ( A total of four) were installed. The installation front of the crossing honeycomb of the reactor was opened in a rectangular shape of 402 × 302 mm. The inner case of the crossed honeycomb to be replaced has guide rails with a thickness of 5 mm, height of 40 mm, and length of 405 mm installed on both end faces (width 20 mm) that support the outlet. A 5 mm long, 4 mm high, and 405 mm long support for preventing packing slippage was attached. Further, a packing presser having a thickness of 5 mm and a width of 50 mm and a support for fixing the crossed honeycomb (bolt fixing) were attached to the front face of the hand at the time of insertion.
The bolts of existing cross honeycombs were removed and pulled out and removed, and cross honeycombs with packings attached to each required portion were inserted and bolted. The time required for exchanging two crossed honeycombs by one person was about one hour, and no removal machine was required.

[比較例1]
実施例1と同様の定置ディ−ゼルエンジンを用い、交差ハニカムを内部に格納する反応器での交差ハニカムの交換実験を行った。発電能力500kWのディーゼルエンジンの排ガス出口に内径200mmΦの配管を設置し、排ガス出口から2.5m後流側の位置に反応器を取付けた。反応器には、入口400×400mm角、長さ300mmの交差ハニカムが、二個格納できる構造である。反応器は、内寸が150mmΦから1.2m×700mm角に広がり、300mm後流側に二個の並列に交差ハニカムの入口外周部および出口外周部を完全に保持/密閉する構造であった。
[Comparative Example 1]
Using the same stationary diesel engine as in Example 1, an experiment for exchanging the intersecting honeycomb was performed in a reactor in which the intersecting honeycomb was housed. A pipe with an inner diameter of 200 mmΦ was installed at the exhaust gas outlet of a diesel engine with a power generation capacity of 500 kW, and a reactor was installed at a position 2.5 m behind the exhaust gas outlet. The reactor has a structure that can store two crossed honeycombs with an entrance of 400 × 400 mm square and a length of 300 mm. The reactor had a structure in which the inner dimension expanded from 150 mmΦ to 1.2 m × 700 mm square, and the inlet outer peripheral part and the outer peripheral part of the crossed honeycomb were completely held / sealed in parallel on the downstream side of 300 mm.

既設の交差ハニカムを交換するため、反応器をクレーンで吊り下げて取外し、さらに反応器から既設の交差ハニカムを取外した。新しい交差ハニカムを反応器内に取付けた後、反応器をクレーンで吊り下げて配管に取付けた。交換作業は三人で二個の交差ハニカムの交換に要した時間は約10時間であった。   In order to replace the existing cross honeycomb, the reactor was suspended by a crane and removed, and the existing cross honeycomb was removed from the reactor. After the new cross honeycomb was installed in the reactor, the reactor was suspended by a crane and attached to the pipe. The time required for replacement of two crossed honeycombs by three people was about 10 hours.

本発明の排ガス処理装置の側面図である、It is a side view of the exhaust gas treatment apparatus of the present invention, 本発明の排ガス処理装置の正面図である、It is a front view of the exhaust gas treatment apparatus of the present invention, 本発明による交差ハニカムDPFの排ガス流れ様子を示す説明図、Explanatory drawing which shows the waste gas flow mode of the cross honeycomb DPF by this invention, 本発明に用いる反応器の説明図、交差ハニカムインナーケースを示した図である。It is explanatory drawing of the reactor used for this invention, and the figure which showed the cross honeycomb inner case. 本発明の他の実施例を示す排ガス処理装置の側面図、Side view of an exhaust gas treatment apparatus showing another embodiment of the present invention, 本発明の反応器の設置方法を示す説明図、Explanatory drawing which shows the installation method of the reactor of this invention, 本発明の反応器を排ガス管路に設置した状態の平面図。The top view of the state which installed the reactor of this invention in the exhaust gas pipeline.

符号の説明Explanation of symbols

1.排ガス管路、1A.分岐管、2.反応器、3.多孔質波板、4.多孔質平板、5.5A.フィルタ装置、6.インナーケース、7.ガイドレール、8.ガイドレール支持部材、9.フィルタ管路、10.パージ用管路、11.切替弁、12.支持板、 13.緩衝材、14.把手、15.断熱材、16.パッキン、17.断熱材支持部。   1. Exhaust gas line, 1A. Branch pipe, 2. 2. reactor, 3. porous corrugated plate; Porous flat plate, 5.5A. Filter device, 6. 6. Inner case Guide rails, 8. 8. guide rail support member, Filter line, 10. 10. purge line; Switching valve, 12. Support plate, 13. Cushioning material, 14. Handle, 15. Insulation, 16. Packing, 17. Insulation support.

Claims (4)

排ガス管路に着脱可能に設けられた反応器を有する排ガス処理装置であって、該反応器は、排ガス浄化触媒が担持された多孔質波板と多孔質平板の対を基本単位とし、該多孔質波板の波板稜線が交互に直交するように積層された成形体を有し、該成形体の前記波板稜線と直交する側面の一つの面、または互いに隣接する二つの面がシールされ、前記多孔質平板を介して前記多孔質波板との間にそれぞれ排ガスの流入経路と流出経路が形成されるフィルタ装置と、該フィルタ装置を保持するインナーケースと、該インナーケースに一体的に設けられたガイドレールと、該ガイドレールに適合するように排ガス管路内壁に設けられたガイドレール支持部材とを有することを特徴とする排ガス処理装置。 An exhaust gas treatment apparatus having a reactor detachably provided in an exhaust gas conduit, the reactor having a porous corrugated plate and a porous flat plate carrying an exhaust gas purification catalyst as a basic unit, the porous unit The corrugated sheet ridges are formed so that the corrugated ridges of the corrugated sheet are alternately orthogonal to each other, and one surface of the corrugated sheet orthogonal to the corrugated ridge lines or two surfaces adjacent to each other are sealed. A filter device in which an exhaust gas inflow path and an outflow path are formed between the porous corrugated plate and the porous corrugated plate via the porous flat plate, an inner case holding the filter device, and the inner case integrally An exhaust gas treatment apparatus comprising: a guide rail provided; and a guide rail support member provided on an inner wall of the exhaust gas pipe so as to be fitted to the guide rail. 前記フィルタ装置の排ガス流出経路を経由するフィルタ管路と、前記フィルタ装置の排ガスが流入する側面と対向する面を開放して排ガスにより該フィルタ装置をパージするためのパージ用管路と、前記二つの管路のいずれかを選択するための切替弁とをさらに有することを特徴とする請求項1記載の装置。 A filter line through the exhaust gas outflow path of the filter device, a purge line for purging the filter device with the exhaust gas by opening a surface facing the side surface of the filter device into which the exhaust gas flows, and the two The apparatus according to claim 1, further comprising a switching valve for selecting one of the two pipe lines. 前記排ガス管路は、それぞれ前記反応器が配置された分岐管を有し、該分岐管は、それぞれ前記パージ用管路およびフィルタ管路に連結されていることを特徴とする請求項2記載の装置。 3. The exhaust gas pipe according to claim 2, wherein the exhaust pipe has a branch pipe in which the reactor is arranged, and the branch pipe is connected to the purge pipe and the filter pipe, respectively. apparatus. 前記ガイドレールおよび前記ガイドレール支持部材が断面コ字状ないし鍵状であり、これらの間にパッキンまたは緩衝材が挟持されていることを特徴とする請求項1ないし3のいずれかに記載の装置。 The apparatus according to any one of claims 1 to 3, wherein the guide rail and the guide rail support member have a U-shaped cross-section or a key shape, and a packing or a cushioning material is sandwiched therebetween. .
JP2005048871A 2005-02-24 2005-02-24 Exhaust gas treatment device Pending JP2006233846A (en)

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Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2010045285A2 (en) * 2008-10-16 2010-04-22 Cummins Filtration Ip Inc. Detachable decomposition reactor with an integral mixer
DE102008062217A1 (en) * 2008-12-13 2010-06-17 Deutz Ag Particle filter system with variable separation efficiency
US8114364B2 (en) 2009-02-02 2012-02-14 Cummins Filtration Ip, Inc. Increased reductant decomposition reactor robustness through the use of a hydrolytic catalyst coating
KR101214097B1 (en) * 2010-10-01 2012-12-20 대지금속 주식회사 Diesel Particulate Filter
KR200469821Y1 (en) 2012-09-28 2013-11-12 두산엔진주식회사 Reactor for selective catalytic reuction
KR101672316B1 (en) * 2016-05-11 2016-11-04 (주)동경기전 Filter device and generation appratus therin
CN107754553A (en) * 2017-11-24 2018-03-06 绍兴市英强橡塑科技有限公司 Waste gas treatment equipment and technique
CN107754553B (en) * 2017-11-24 2024-05-03 绍兴市英强橡塑科技有限公司 Exhaust gas treatment equipment and process

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2010045285A2 (en) * 2008-10-16 2010-04-22 Cummins Filtration Ip Inc. Detachable decomposition reactor with an integral mixer
WO2010045285A3 (en) * 2008-10-16 2010-07-08 Cummins Filtration Ip Inc. Detachable decomposition reactor with an integral mixer
US7976788B2 (en) 2008-10-16 2011-07-12 Cummins Filtration Ip, Inc. Detachable decomposition reactor with an integral mixer
DE102008062217A1 (en) * 2008-12-13 2010-06-17 Deutz Ag Particle filter system with variable separation efficiency
US8935916B2 (en) 2008-12-13 2015-01-20 Deutz Aktiengesellschaft Particulate filter system having a variable degree of separation
US8114364B2 (en) 2009-02-02 2012-02-14 Cummins Filtration Ip, Inc. Increased reductant decomposition reactor robustness through the use of a hydrolytic catalyst coating
KR101214097B1 (en) * 2010-10-01 2012-12-20 대지금속 주식회사 Diesel Particulate Filter
KR200469821Y1 (en) 2012-09-28 2013-11-12 두산엔진주식회사 Reactor for selective catalytic reuction
KR101672316B1 (en) * 2016-05-11 2016-11-04 (주)동경기전 Filter device and generation appratus therin
CN107754553A (en) * 2017-11-24 2018-03-06 绍兴市英强橡塑科技有限公司 Waste gas treatment equipment and technique
CN107754553B (en) * 2017-11-24 2024-05-03 绍兴市英强橡塑科技有限公司 Exhaust gas treatment equipment and process

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