JP2006247532A - Filter device for purifying exhaust gas - Google Patents

Filter device for purifying exhaust gas Download PDF

Info

Publication number
JP2006247532A
JP2006247532A JP2005067849A JP2005067849A JP2006247532A JP 2006247532 A JP2006247532 A JP 2006247532A JP 2005067849 A JP2005067849 A JP 2005067849A JP 2005067849 A JP2005067849 A JP 2005067849A JP 2006247532 A JP2006247532 A JP 2006247532A
Authority
JP
Japan
Prior art keywords
filter
exhaust gas
valley
upstream
peak
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
JP2005067849A
Other languages
Japanese (ja)
Other versions
JP5044101B2 (en
Inventor
Seiji Ogawara
誠治 大河原
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.)
Vitesco Technologies Lohmar Verwaltungs GmbH
Toyota Motor Corp
Original Assignee
Emitec Gesellschaft fuer Emissionstechnologie mbH
Toyota Motor 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
Priority to JP2005067849A priority Critical patent/JP5044101B2/en
Application filed by Emitec Gesellschaft fuer Emissionstechnologie mbH, Toyota Motor Corp filed Critical Emitec Gesellschaft fuer Emissionstechnologie mbH
Priority to EP05730342A priority patent/EP1735077B1/en
Priority to RU2006139958/15A priority patent/RU2343961C2/en
Priority to KR1020067021142A priority patent/KR100860327B1/en
Priority to DE602005025992T priority patent/DE602005025992D1/en
Priority to PCT/JP2005/007377 priority patent/WO2005099867A1/en
Priority to US11/578,041 priority patent/US7959868B2/en
Publication of JP2006247532A publication Critical patent/JP2006247532A/en
Application granted granted Critical
Publication of JP5044101B2 publication Critical patent/JP5044101B2/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • Y02T10/144
    • Y02T10/24

Landscapes

  • Filtering Materials (AREA)
  • Filtering Of Dispersed Particles In Gases (AREA)
  • Exhaust Gas Treatment By Means Of Catalyst (AREA)
  • Catalysts (AREA)
  • Exhaust Gas After Treatment (AREA)
  • Processes For Solid Components From Exhaust (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide a filter device for purifying an exhaust gas in which a particulate material (PM) is prevented from being deposited on an end surface in an exhaust gas inflow side while both improving a collection efficiency of PM and preventing an increase of exhaust gas pressure loss. <P>SOLUTION: The filter device for purifying an exhaust gas comprises: a plurality of exhaust gas flow paths; and a filter 3 disposed in the exhaust gas flow paths, the exhaust gas flow path having: a filter introduction portion 100 for introducing the exhaust gas to the filter 3; and a filter bypass portion 200 for diverging the filter introduction portion 100 to the exhaust gas flow paths adjacent thereto to be bypassed, the filter bypass portion 202 in the most upstream being disposed toward the upper stream side than the filter introduction portion 100 in the most upstream and opened to an end surface in an exhaust gas inlet side, wherein the exhaust gas firstly passes through the filter bypass portion 202 in the most upstream and therefore PM can be prevented from being deposited on an end surface in an exhaust gas inflow side, whereby hardly causing clogging of PM on the end surface. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

本発明は、ディーゼルエンジンなどからの排ガス中の粒子状物質(以下、PMという)を捕集する排ガス浄化フィルタ装置に関する。   The present invention relates to an exhaust gas purification filter device that collects particulate matter (hereinafter referred to as PM) in exhaust gas from a diesel engine or the like.

ディーゼルエンジンなどからの排ガス中には、カーボン微粒子、 SOF、サルフェート類などからなるPMが含まれているため、排出前にPMを除去して清浄な排ガスを排出する必要がある。このPMは、通常の酸化触媒、三元触媒などでは除去することが困難であるため、フィルタに捕集した後に酸化除去する方法が一般的である。   Since exhaust gas from diesel engines, etc. contains PM composed of carbon fine particles, SOF, sulfates, etc., it is necessary to remove PM before discharging to discharge clean exhaust gas. Since it is difficult to remove this PM with a normal oxidation catalyst, a three-way catalyst, etc., a method of removing it by oxidation after collecting it on a filter is common.

このようなフィルタとしては、コーディエライトなどの耐熱性セラミックスからなり多数のセルをもつハニカム体に、下流側端部で目詰めされた流入側セルと、流入側セルに隣接し上流側端部で目詰めされた流出側セルを形成したウォールフロー型のものが広く用いられている。このフィルタでは、流入側セルに流入した排ガスがセル隔壁を通過して流出側セルから排出されるが、排ガスがセル隔壁を通過する際にPMがセル隔壁の細孔中に捕集される。そしてPMがある程度捕集されると、ヒータによる加熱などで捕集されたPMを燃焼させフィルタ機能を再生することが行われる。   As such a filter, a honeycomb body made of heat-resistant ceramics such as cordierite and having a large number of cells, an inflow side cell clogged at the downstream end, and an upstream end adjacent to the inflow side cell A wall flow type in which an outflow side cell clogged with the above is formed is widely used. In this filter, the exhaust gas flowing into the inflow side cell passes through the cell partition wall and is discharged from the outflow side cell, but when the exhaust gas passes through the cell partition wall, PM is collected in the pores of the cell partition wall. When PM is collected to some extent, PM collected by heating with a heater is burned to regenerate the filter function.

しかしこのようなフィルタでは、PM捕集量が多い場合には再生時の燃焼による発熱量が大きく、ヒートショックによって損傷する場合がある。また製造コストも高い。そこで近年では、金属製のフィルタ装置がいくつか提案されている。   However, with such a filter, when the amount of PM trapped is large, the amount of heat generated by combustion during regeneration is large and may be damaged by heat shock. In addition, the manufacturing cost is high. Therefore, in recent years, several metal filter devices have been proposed.

たとえば特開平09−262414号公報には、金属薄板からなる波板と金属不織布からなる平板とを交互に積層し、下流側端部で目詰めされた流入側セルと、流入側セルに隣接し上流側端部で目詰めされた流出側セルと、を形成したフィルタが記載されている。また特開2002−113798号公報には、金属不織布からなる平板と波板とを交互に積層し、下流側端部で目詰めされた流入側セルと、流入側セルに隣接し上流側端部で目詰めされた流出側セルと、を形成したフィルタが記載されている。   For example, in Japanese Patent Application Laid-Open No. 09-262414, a corrugated plate made of a thin metal plate and a flat plate made of a metal non-woven fabric are alternately laminated, and an inflow side cell clogged at a downstream end portion is adjacent to the inflow side cell. A filter is described which forms an outflow side cell clogged at an upstream end. Further, JP 2002-113798 A discloses an inflow side cell in which flat plates and corrugated plates made of a metal nonwoven fabric are alternately laminated and clogged at a downstream end, and an upstream end adjacent to the inflow side cell. And a filter formed with an outflow side cell clogged with.

これらのフィルタによれば、排ガス中のPMは金属不織布中に捕集される。そして加熱によってPMを燃焼させる再生処理を行っても、金属製であるためヒートショックが小さく損傷を抑制することができる。ところがこれらのフィルタは、いずれもウォールフロー型のフィルタであるので、PMの捕集に伴って排気圧損が上昇する。しかも流入側セルの目詰め部近傍にPMが集中して堆積するため排気圧損が一気に上昇するという不具合があり、エンジン効率や燃費などを重視する場合には再生処理を頻繁に行う必要がある。   According to these filters, PM in the exhaust gas is collected in the metal nonwoven fabric. And even if it performs the regeneration process which burns PM by heating, since it is metal, a heat shock is small and damage can be suppressed. However, since these filters are all wall flow type filters, the exhaust pressure loss increases as PM is collected. In addition, since PM concentrates and accumulates in the vicinity of the clogging portion of the inflow side cell, there is a problem that exhaust pressure loss increases at a stretch. When importance is attached to engine efficiency or fuel consumption, it is necessary to frequently perform regeneration processing.

一方、独国実用新案 20,117,873 U1号には、金属フォイル製の波板とフィルタ層とを交互に積層し、波板に爪状穴高さを有する複数の爪状穴を形成し、複数の爪状穴は内向爪状穴と外向爪状穴とを有する流路を形成し、内向爪状穴と外向爪状穴とは互いに角をなして配置され、爪状穴高さは構造高さの 100〜60%の高さがあり少なくとも20%の流動自由度が保証されたフィルタが記載されている。   On the other hand, in German utility model 20,117,873 U1, a corrugated plate made of metal foil and a filter layer are alternately laminated to form a plurality of claw-shaped holes having claw-shaped hole heights on the corrugated plate. The inner hole forms a flow path having an inward nail hole and an outward nail hole, the inward nail hole and the outward nail hole are arranged at an angle with each other, and the nail hole height is equal to the structural height. A filter is described which is 100-60% high and guarantees a flow freedom of at least 20%.

このフィルタによれば、爪状穴から出る排ガスがフィルタ層を通過することでPMがフィルタ層に捕集される。しかしこのフィルタ装置では、フィルタ層と爪状穴の爪部分にPMの堆積が進行すると、排ガスの流路が塞がれて排気圧損が急激に上昇するため、捕集できるPMの量を多くすることができずPM捕集効率を低くせざるを得ないという欠点がある。
特開平09−262414号 特開2002−113798号 独国実用新案 20,117,873 U1号
According to this filter, PM is collected in the filter layer by the exhaust gas coming out of the claw-shaped holes passing through the filter layer. However, in this filter device, if PM deposits on the filter layer and the claw portion of the claw-shaped hole, the exhaust gas flow path is blocked and the exhaust pressure loss increases rapidly, so the amount of PM that can be collected is increased. However, there is a disadvantage that the PM collection efficiency must be lowered.
JP 09-262414 A JP 2002-113798 German utility model 20,117,873 U1

そこで本願発明者らは、特願2004−117189号において、複数の排ガス流路と、排ガス流路に設置されたフィルタと、を有する排ガス浄化フィルタ装置であって、排ガス流路は、排ガスをフィルタへ導くフィルタ導入部と、フィルタ導入部に隣接する排ガス流路へ分岐してフィルタ導入部を迂回するフィルタ迂回部と、を有する排ガス浄化フィルタ装置を提案している。   In view of this, the inventors of the present application disclosed in Japanese Patent Application No. 2004-117189, an exhaust gas purification filter device having a plurality of exhaust gas passages and filters installed in the exhaust gas passages. Has proposed an exhaust gas purification filter device having a filter introduction part that leads to the exhaust gas flow path adjacent to the filter introduction part and a filter bypass part that bypasses the filter introduction part.

ところが実用化のために種々の実験を行ったところ、上記排ガス浄化フィルタ装置においては、運転状況によって高濃度のPMを含む排ガスが長時間流入した場合に、フィルタ装置の流入側端面にPMが多く堆積する場合があることが明らかとなった。このように流入側端面にPMが多く堆積すると、排気圧損が増大するばかりか、高温条件下などで着火するとフィルタ全体としては許容限界量以下の堆積量であっても局部的に急激に昇温し、溶損などの障害が起きることが懸念される。   However, when various experiments were conducted for practical use, in the exhaust gas purification filter device described above, when exhaust gas containing high concentration PM flows in for a long time depending on operating conditions, there is a large amount of PM on the inflow side end face of the filter device. It became clear that it might accumulate. When a large amount of PM accumulates on the inflow side end face in this way, exhaust pressure loss increases, and when ignited under high-temperature conditions, the filter as a whole will rapidly increase in temperature even if it is less than the allowable limit amount. However, there are concerns that failures such as melting may occur.

本発明はこのような事情に鑑みてなされたものであり、PMの捕集効率の向上と、排気圧損の上昇の抑制を両立させるとともに、流入側端面へのPMの堆積を抑制することを課題とする。   The present invention has been made in view of such circumstances, and it is an object to achieve both improvement in PM collection efficiency and suppression of increase in exhaust pressure loss, and suppression of PM accumulation on the inflow side end face. And

上記課題を解決する本発明の排ガス浄化フィルタ装置の特徴は、複数の排ガス流路と、排ガス流路に設置されたフィルタと、を有する排ガス浄化フィルタ装置であって、
排ガス流路は、排ガスをフィルタへ導くフィルタ導入部と、フィルタ導入部に隣接する排ガス流路へ分岐してフィルタ導入部を迂回するフィルタ迂回部と、を有し、
最上流のフィルタ迂回部は、最上流のフィルタ導入部より上流側に設けられ排ガス入口側端面に開口していることにある。
A feature of the exhaust gas purification filter device of the present invention that solves the above problems is an exhaust gas purification filter device having a plurality of exhaust gas flow channels and a filter installed in the exhaust gas flow channel,
The exhaust gas flow path has a filter introduction part that guides the exhaust gas to the filter, and a filter bypass part that branches to the exhaust gas flow path adjacent to the filter introduction part and bypasses the filter introduction part,
The most upstream filter bypassing part is provided upstream of the most upstream filter introducing part and is open to the exhaust gas inlet side end face.

この排ガス浄化フィルタ装置をさらに具体化する排ガス浄化フィルタ装置の特徴は、金属薄板よりなり山部と谷部とが排ガス流れ方向と交差する方向に交互に連続する波状板と、耐熱性繊維が集積されてなり前記フィルタを構成するガス透過性の平板と、が交互に積層されてなり、
山部は山高さが低くなることで形成された凹状の中間谷部を有し、中間谷部は隣接する谷部から排ガスが分岐して流入可能な分岐部とその下流側で山部に連通する開口とよりなるフィルタ迂回部を構成し、
谷部は谷深さが浅くなることで形成された凸状の中間山部を有し、中間山部と隣接する両側の山部と山部に接する平板とで流路が閉塞されたフィルタ導入部を構成し、
フィルタ導入部内の圧力が高まった場合に、谷部を流れる排ガスの少なくとも一部がフィルタ導入部からフィルタ導入部の上流側に存在するフィルタ迂回部を通過して隣接する山部に流入し、最上流では排ガスは先ず最上流のフィルタ迂回部に流入するように構成されたことにある。
A feature of the exhaust gas purification filter device that further embodies this exhaust gas purification filter device is that a corrugated plate made of a thin metal plate and alternately continuous in a direction intersecting the exhaust gas flow direction and heat resistant fibers are integrated. And gas permeable flat plates constituting the filter are alternately laminated,
The ridge has a concave middle valley that is formed by lowering the mountain height, and the middle valley communicates with the ridge at the downstream side where the exhaust gas diverges and flows from the adjacent valley. A filter detour that consists of an opening and
The trough has a convex intermediate peak formed by the shallow valley depth, and the filter is introduced with the channel blocked by the peak on both sides adjacent to the intermediate peak and the flat plate in contact with the peak. Part
When the pressure in the filter inlet increases, at least a part of the exhaust gas flowing in the valley flows from the filter inlet to the adjacent peak by passing through the filter bypass located upstream of the filter inlet. Upstream, the exhaust gas is first configured to flow into the most upstream filter bypass.

また、この排ガス浄化フィルタ装置の特徴を波状板の裏側から表現すれば、金属薄板よりなり山部と谷部とが排ガス流れ方向と交差する方向に交互に連続する波状板と、耐熱性繊維が集積されてなりフィルタを構成するガス透過性の平板と、が交互に積層されてなり、
谷部は谷深さが浅くなることで形成された凸状の中間山部を有し、中間山部は隣接する山部から排ガスが分岐して流入可能な分岐部とその下流側で谷部に連通する開口とよりなるフィルタ迂回部を構成し、
山部は山高さが低くなることで形成された凹状の中間谷部を有し、中間谷部と隣接する両側の谷部と谷部に接する平板とで流路が閉塞されたフィルタ導入部を構成し、
フィルタ導入部内の圧力が高まった場合に、山部を流れる排ガスの少なくとも一部がフィルタ導入部からフィルタ導入部の上流側に存在するフィルタ迂回部を通過して隣接する谷部に流入し、最上流では排ガスは先ず最上流のフィルタ迂回部に流入するように構成されたことにある。
In addition, if the characteristics of the exhaust gas purification filter device are expressed from the back side of the corrugated plate, the corrugated plate made of a thin metal plate and alternately continuous in the direction in which the crests and troughs intersect the exhaust gas flow direction, and the heat-resistant fiber Gas-permeable flat plates that are integrated and constitute a filter are alternately laminated,
The valley portion has a convex intermediate mountain portion formed by decreasing the valley depth, and the intermediate mountain portion is a branch portion where exhaust gas can branch from the adjacent mountain portion and can flow in, and a valley portion on the downstream side thereof. A filter bypass portion comprising an opening communicating with the
The peak portion has a concave intermediate valley portion formed by lowering the peak height, and the filter introduction portion in which the flow path is blocked by the valley portion on both sides adjacent to the intermediate valley portion and the flat plate in contact with the valley portion. Configure
When the pressure in the filter inlet increases, at least a part of the exhaust gas flowing through the peak flows from the filter inlet through the filter bypass located upstream of the filter inlet and flows into the adjacent valley. Upstream, the exhaust gas is first configured to flow into the most upstream filter bypass.

最上流のフィルタ迂回部は、上流側開口と下流側開口をもつ山部と、下流側開口に連続した谷部と、谷部の深さが徐々に浅くなり下流側の山部に連続する逆中間谷部と、からなるものとすることができる。   The most upstream filter detour includes a crest having an upstream opening and a downstream opening, a trough that continues to the downstream opening, and a reverse that continues to the crest on the downstream side as the depth of the trough gradually decreases. And an intermediate valley portion.

また最上流のフィルタ迂回部は、谷部と、谷部に形成され上流側端部に開口するとともに下流側に向かって高さが徐々に低くなり下流側の谷部に連続する逆中間山部と、よりなるものとすることもできる。   The most upstream filter detour part is a valley part and an inverted intermediate mountain part that is formed in the valley part and opens to the upstream end part and gradually decreases in height toward the downstream side and continues to the downstream valley part. It can also be made up of.

さらに最上流のフィルタ迂回部は、波状板の下側に積層された平板の山部に対向する位置に形成された排ガス中のPMが透過可能な貫通孔としてもよいし、波状板の下側に積層された平板の山部に対向する位置に形成された排ガス中のPMが透過可能な切欠き部としてもよい。   Further, the most upstream filter bypass portion may be a through-hole through which PM in the exhaust gas can be formed, which is formed at a position facing a crest of the flat plate laminated on the lower side of the corrugated plate, or the lower side of the corrugated plate It is good also as a notch part which can permeate | transmit PM in the waste gas formed in the position facing the peak part of the flat plate laminated | stacked by.

本発明の排ガス浄化フィルタ装置によれば、フィルタ導入部にPMが堆積して排気圧損が上昇すると、排ガスはフィルタ迂回部から分岐して流れるようになり、フィルタ迂回部を通って順次フィルタを迂回しながら流出側端部まで流通するので、排気圧損の上昇が抑制される。   According to the exhaust gas purifying filter device of the present invention, when PM accumulates in the filter introduction part and the exhaust pressure loss increases, the exhaust gas branches off from the filter bypass part and flows through the filter bypass part sequentially. However, since it flows to the outflow side end, an increase in exhaust pressure loss is suppressed.

そしてフィルタ導入部からフィルタ迂回部までのフィルタをPMの捕集に用いることができ、フィルタの大きな面積をPMの捕集に用いることができるので、効率的にPMを捕集することができる。また、そのことにより、捕集されたPMを酸化処理するにあたり、酸化剤や熱が効率的にPMに伝わるため、捕集されたPMを効率的に酸化処理することができる。   And since the filter from a filter introduction part to a filter detour part can be used for collection of PM, and the big area of a filter can be used for collection of PM, PM can be collected efficiently. Moreover, when oxidizing the collected PM, the oxidizing agent and heat are efficiently transmitted to the PM, so that the collected PM can be efficiently oxidized.

さらに排ガスは先ず最上流のフィルタ迂回部を通過するので、流入側端面へのPMの堆積を抑制することができ端面閉塞が起こり難い。したがって流入側端面の流路開口を常に大きく確保することができ、排気圧損の上昇を抑制できるとともに、過度の昇温による溶損を回避することができる。また、微視的にはPMの捕集効率が低下するものの、全排ガス流路が常時有効に機能するので、全体としての捕集効率は高く維持することができ、むしろPM捕集効率が向上するようにもなる。   Furthermore, since the exhaust gas first passes through the most upstream filter detour part, PM accumulation on the inflow side end face can be suppressed, and end face obstruction is unlikely to occur. Therefore, it is possible to always ensure a large flow path opening on the inflow side end face, to suppress an increase in exhaust pressure loss, and to avoid a melting loss due to excessive temperature rise. In addition, although the PM collection efficiency is microscopically reduced, the entire exhaust gas flow path always functions effectively, so the overall collection efficiency can be maintained high, and rather the PM collection efficiency is improved. It also comes to do.

本発明の排ガス浄化フィルタ装置は、複数の排ガス流路と、排ガス流路に設置されたフィルタと、を有し、排ガス流路は、排ガスをフィルタへ導くフィルタ導入部と、フィルタ導入部に隣接する排ガス流路へ分岐してフィルタ導入部を迂回するフィルタ迂回部と、を備えている。   The exhaust gas purification filter device of the present invention has a plurality of exhaust gas flow paths and a filter installed in the exhaust gas flow path, and the exhaust gas flow path is adjacent to the filter introduction part that guides the exhaust gas to the filter, and the filter introduction part And a filter bypass section that branches to the exhaust gas flow path that bypasses the filter introduction section.

フィルタはPMを捕集可能でかつ通気性を有するものであり、セラミックス、金属繊維集積体などを用いることができる。このフィルタを排ガス流路に配置することでフィルタ導入部を形成することができ、その上流側の排ガス流路に、隣接する排ガス流路と連通する貫通孔などを形成しておくことでフィルタ迂回部を形成することができる。特に好ましい形態としては、通気性をもたない波状板と平板状のフィルタとを交互に積層してなるハニカム形状のフィルタ装置とすることが望ましい。   The filter can collect PM and has air permeability, and ceramics, metal fiber aggregates, and the like can be used. By arranging this filter in the exhaust gas flow path, a filter introduction part can be formed, and by bypassing the filter by forming a through hole etc. communicating with the adjacent exhaust gas flow path in the exhaust gas flow path on the upstream side thereof The part can be formed. As a particularly preferred embodiment, it is desirable to make a honeycomb-shaped filter device in which corrugated plates having no air permeability and flat plate filters are alternately laminated.

このようなフィルタ装置としては、請求項2又は請求項3に記載のものが特に好ましい。請求項2に記載の排ガス浄化フィルタ装置では、谷部と上側の平板とで形成された流路に流入した排ガスは、中間山部に衝突してフィルタ導入部を仕切る上側の平板を通過し、PMが平板に捕集される。そしてフィルタ導入部を仕切る上側の平板のPM捕集量が多くなると、フィルタ導入部内の圧力が高まるため、排ガスはフィルタ導入部から上流側のフィルタ迂回部の分岐部を通過し、両側の山部の中間谷部から開口を通じて両側の山部に分岐流入する。   As such a filter apparatus, the thing of Claim 2 or Claim 3 is especially preferable. In the exhaust gas purifying filter device according to claim 2, the exhaust gas flowing into the flow path formed by the valley portion and the upper flat plate passes through the upper flat plate that collides with the intermediate mountain portion and partitions the filter introduction portion, PM is collected on the flat plate. When the amount of PM trapped on the upper flat plate that partitions the filter introduction portion increases, the pressure in the filter introduction portion increases, so the exhaust gas passes through the branch portion of the filter detour portion on the upstream side from the filter introduction portion, and the peaks on both sides Branch inflows from the middle valley to the peaks on both sides.

そして請求項3に記載のように波状板の裏面側では、中間谷部の裏面側が凸となって山部と下側の平板との間にフィルタ導入部が形成され、その上流側の谷部の中間山部にフィルタ迂回部が形成されているので、山部と下側の平板とで形成された流路に流入した排ガスは、中間谷部に衝突しフィルタ導入部内で圧力が高まった場合にフィルタ導入部から上流側のフィルタ迂回部を通過し、両側の谷部の中間山部の開口を通じて両側の谷部に分岐流入する。   And as described in claim 3, on the back side of the corrugated plate, the back side of the intermediate valley is convex and a filter introduction part is formed between the peak and the lower flat plate, and the upstream valley Since the filter detour part is formed at the intermediate peak of the exhaust gas, the exhaust gas flowing into the flow path formed by the peak and the lower flat plate collides with the intermediate valley and the pressure increases in the filter introduction part From the filter introduction part, it passes through the filter detour part on the upstream side, and branches and flows into the troughs on both sides through the opening of the intermediate peak part of the troughs on both sides.

この作用が排ガス流入側端面から流出側端面まで連続的に繰り返される。   This action is continuously repeated from the exhaust gas inflow side end surface to the outflow side end surface.

すなわち、本発明のフィルタ装置は基本的にウォールフロー構造であるので、PMの捕集効率が高い。そしてフィルタ導入部における平板のPM捕集量が多くなっても、排ガスは上流側のフィルタ迂回部から分岐して山部又は谷部に流入し、これが連続的に生じる。したがってPMの堆積による排気圧損の上昇が一気に生じることがなく、また平板の大部分をPMの捕集に利用することができるため、排気圧損の上昇を効果的に抑制することが可能となる。   That is, since the filter device of the present invention basically has a wall flow structure, the PM collection efficiency is high. Even if the amount of PM trapped on the flat plate in the filter introduction portion increases, the exhaust gas branches off from the upstream filter detour portion and flows into the peak portion or valley portion, which continuously occurs. Therefore, an increase in exhaust pressure loss due to PM accumulation does not occur all at once, and since most of the flat plate can be used for PM collection, an increase in exhaust pressure loss can be effectively suppressed.

さらに、最上流のフィルタ迂回部は、最上流のフィルタ導入部より上流側に設けられ排ガス入口側端面に開口している。したがって最上流では、排ガスは先ず最上流のフィルタ迂回部に流入するので、流入側端面へのPMの堆積を抑制することができ端面閉塞が起こり難い。   Further, the most upstream filter bypass portion is provided on the upstream side of the most upstream filter introduction portion and is open to the exhaust gas inlet side end surface. Therefore, in the uppermost stream, the exhaust gas first flows into the uppermost filter detour part, so that PM accumulation on the inflow side end face can be suppressed and end face blockage hardly occurs.

波状板は、金属薄板から形成されたものであり、コルゲート加工などにより製造することが望ましい。その材質は、排ガス温度及び再生時の熱に耐え得る以上の耐熱性を有すれば特に制限されないが、ステンレス鋼材が好ましい。また自動車用の場合には、厚さは20〜 110μmの範囲が好ましく、40〜80μmの範囲が特に好ましい。   The corrugated plate is formed from a thin metal plate, and is preferably manufactured by corrugating or the like. The material is not particularly limited as long as it has heat resistance that can withstand the exhaust gas temperature and heat during regeneration, but a stainless steel material is preferable. For automobiles, the thickness is preferably in the range of 20 to 110 μm, particularly preferably in the range of 40 to 80 μm.

平板は耐熱性繊維が集積されてなるガス透過性の部材であり、金属繊維、セラミックス繊維、金属ウィスカ、セラミックスウィスカなどの不織布、織布などから形成することができる。自動車用排ガス浄化フィルタ装置としてPM捕集効率の向上と排気圧損の上昇抑制とを両立させるためには、繊維径は15〜60μm程度が好ましく、目付量が300〜1000g/m2 のものが好ましい。   The flat plate is a gas-permeable member in which heat-resistant fibers are integrated, and can be formed from non-woven fabrics such as metal fibers, ceramic fibers, metal whiskers, and ceramic whiskers, and woven fabrics. In order to achieve both improvement in PM collection efficiency and suppression of increase in exhaust pressure loss as an exhaust gas purification filter device for automobiles, the fiber diameter is preferably about 15 to 60 μm, and the basis weight is preferably 300 to 1000 g / m 2.

本発明のフィルタ装置とするには、波状板と平板とを交互に積層して所定の外筒に挿入してもよいし、所定長さの波状板と平板とを重ねてロール状に巻回したものを所定の外筒に挿入することもできる。なお波状板は、全ての層で同じ向き及び同じ位相となるように積層してもよいし、交互に 180度異なる向きとなるように、あるいは位相が異なるように積層することもできる。しかし、フィルタ導入部が谷部に形成されている場合は、平板を介した反対側には隣接する波状板の山部が存在していることが望ましく、フィルタ導入部が山部に形成されている場合には、平板を介した反対側には隣接する波状板の谷部が存在していることが望ましい。これにより平板を透過した排ガスの流れが妨げられることなく、PMの捕集効率がより向上するとともに排気圧損の上昇をより抑制することができる。   In order to obtain the filter device of the present invention, the corrugated plates and the flat plates may be alternately stacked and inserted into a predetermined outer cylinder, or the corrugated plates and the flat plates of a predetermined length may be overlapped and wound into a roll shape. This can be inserted into a predetermined outer cylinder. Note that the corrugated plates may be laminated so that all layers have the same direction and the same phase, or can be laminated so that the directions are alternately different by 180 degrees or the phases are different. However, when the filter introduction part is formed in the valley part, it is desirable that there is a crest of the adjacent corrugated plate on the opposite side through the flat plate, and the filter introduction part is formed in the crest part. If there is, it is desirable that a trough portion of the adjacent corrugated plate exists on the opposite side through the flat plate. As a result, the PM collection efficiency can be further improved and the increase in exhaust pressure loss can be further suppressed without impeding the flow of the exhaust gas that has permeated the flat plate.

中間谷部あるいは中間山部は、山部又は谷部を変形させることで形成され、それぞれ上流側端部が底部又は頂部に向かって滑らかに連続していることが望ましい。すなわち上流側に向かって徐々に高さが低くなる、あるいは高くなる斜面で閉塞されていることが好ましい。このようにすることで、フィルタ導入部内の排ガスにはフィルタ導入部を仕切る平板に向かうベクトルが生成するので、PM捕集効率がさらに向上する。   The intermediate valley portion or the intermediate mountain portion is formed by deforming the mountain portion or the valley portion, and it is desirable that the upstream end portion is smoothly continuous toward the bottom portion or the top portion, respectively. That is, it is preferable that the height is gradually reduced toward the upstream side, or is blocked by a slope that becomes higher. By doing in this way, since the vector which goes to the flat plate which partitions a filter introduction part produces | generates in the exhaust gas in a filter introduction part, PM collection efficiency improves further.

フィルタ導入部における平面視での波状板の開口面積は、平面視における波状板の合計開口面積の30%以上であることが望ましい。フィルタ導入部における平面視での波状板の開口面積が合計開口面積の30%未満では、平板の利用面積が低下しPM捕集効率が低下する。またフィルタ導入部の合計容積は、山部及び谷部の合計容積の50%以上であることが望ましい。この比率が50%未満になると、PMの捕集効率が低下するようになる。   The opening area of the corrugated plate in plan view in the filter introduction part is desirably 30% or more of the total opening area of the corrugated plate in plan view. When the opening area of the corrugated plate in plan view at the filter introduction portion is less than 30% of the total opening area, the use area of the flat plate is reduced and the PM collection efficiency is reduced. The total volume of the filter introduction part is preferably 50% or more of the total volume of the peak part and the valley part. When this ratio is less than 50%, the PM collection efficiency decreases.

またフィルタ導入部からその上流側の分岐部までの距離が長いほどPMの捕集効率が向上するが、反面、排気圧損が上昇しやすくなる。したがってその距離には最適値がある。   Also, the longer the distance from the filter introduction part to the upstream branch part, the better the PM collection efficiency, but the exhaust pressure loss tends to increase. Therefore, there is an optimum value for the distance.

最上流のフィルタ迂回部は、上流側開口と下流側開口をもつ山部と、下流側開口に連続した谷部と、谷部の深さが徐々に浅くなり下流側の山部に連続する逆中間谷部と、からなるものとすることができる。この場合、排ガスは上流側端面から先ず山部に流入し、山部から出た排ガスは谷部から逆中間谷部に流入する。逆中間谷部は下流側の山部に連続しているので、先端部が平板で塞がれている。しかしその部分にPMが堆積したとしても、逆中間谷部の途中までは平板との間に隙間があり、排ガスはその隙間から両側の谷部に分岐して流入するので、山部及び逆中間谷部はフィルタ迂回部として機能する。   The most upstream filter detour includes a crest having an upstream opening and a downstream opening, a trough that continues to the downstream opening, and a reverse that continues to the crest on the downstream side as the depth of the trough gradually decreases. And an intermediate valley portion. In this case, the exhaust gas first flows into the peak from the upstream end face, and the exhaust gas that has exited from the peak flows into the reverse intermediate valley from the valley. Since the reverse intermediate valley portion is continuous with the peak portion on the downstream side, the tip portion is closed with a flat plate. However, even if PM accumulates in that part, there is a gap between the flat plate up to the middle of the reverse intermediate valley, and the exhaust gas branches and flows into the valley on both sides from the gap. The trough functions as a filter bypass.

また最上流のフィルタ迂回部は、谷部と、谷部に形成され上流側端部に開口するとともに下流側に向かって高さが徐々に低くなり下流側の谷部に連続する逆中間山部と、よりなるものとしてもよい。この場合、排ガスは上流側端面から先ず谷部に流入し、次いで逆中間山部に流入する。逆中間山部は天井部が下流側の谷部に連続しているので、裏面側では先端部が平板で塞がれている。しかしその部分にPMが堆積したとしても、逆中間山部の途中までは平板との間に隙間があり、排ガスはその隙間から両側の山部に分岐して流入するので、谷部及び逆中間山部はフィルタ迂回部として機能する。   The most upstream filter detour part is a valley part and an inverted intermediate mountain part that is formed in the valley part and opens to the upstream end part and gradually decreases in height toward the downstream side and continues to the downstream valley part. It is good also as what consists of. In this case, the exhaust gas first flows into the valley from the upstream end face, and then flows into the reverse intermediate peak. Since the inverted intermediate mountain part has a ceiling part that is continuous with the valley part on the downstream side, the tip part is closed with a flat plate on the back side. However, even if PM accumulates in that part, there is a gap between the flat plate up to the middle of the reverse intermediate peak, and the exhaust gas branches and flows from the gap to the peaks on both sides. The peak functions as a filter bypass.

さらに最上流のフィルタ迂回部は、波状板の下側に積層された平板の山部に対向する位置に形成された排ガス中のPMが透過可能な貫通孔としてもよいし、波状板の下側に積層された平板の山部に対向する位置に形成された切欠き部としてもよい。この場合、排ガスは先ず山部に流入し、下流側のフィルタ導入部にPMが堆積したとしても、貫通孔あるいは切欠きを通じて、平板を介して下側に積層された波状板の排ガス流路に流入するので、貫通孔及び切欠き部はフィルタ迂回部として機能する。   Further, the most upstream filter bypass portion may be a through-hole through which PM in the exhaust gas can be formed, which is formed at a position facing a crest of the flat plate laminated on the lower side of the corrugated plate, or the lower side of the corrugated plate It is good also as a notch part formed in the position facing the peak part of the flat plate laminated | stacked by. In this case, even if the exhaust gas first flows into the peak and PM accumulates in the filter introduction part on the downstream side, it passes through the through hole or notch and enters the exhaust gas flow path of the corrugated plate stacked on the lower side through the flat plate. Since it flows in, the through hole and the notch function as a filter bypass.

以下、実施例及び比較例により本発明を具体的に説明する。   Hereinafter, the present invention will be specifically described with reference to Examples and Comparative Examples.

(比較例1)
図1に本比較例のフィルタ装置の斜視図と要部拡大図を、図2に波状板の要部斜視図を、図3〜5に要部拡大断面図を示す。このフィルタ装置は、ステンレス鋼よりなりコルゲート加工により形成された厚さ65μmの波状板1と、ステンレス繊維製ファイバーマットからなる目付量 450g/m2 、厚さ 300μmの平板3とが交互に積層されてなるフィルタエレメントと、フィルタエレメントが圧入保持された外筒4と、から構成されている。
(Comparative Example 1)
FIG. 1 is a perspective view and an enlarged view of a main part of the filter device of this comparative example, FIG. 2 is an essential part perspective view of a corrugated plate, and FIGS. This filter device is made of a corrugated plate made of stainless steel and having a thickness of 65 μm, and a flat plate 3 made of stainless steel fiber mat and having a basis weight of 450 g / m 2 and a thickness of 300 μm. And the outer cylinder 4 in which the filter element is press-fitted and held.

図2に示す波状板1は、山部10と谷部11が排ガス流れ方向と直交する方向に交互に連続している。山部10には、凹状の中間谷部12が排ガス流れ方向に平行に互いに間隔を隔てて複数個形成されている。中間谷部12は排ガス上流側から下流側に向かって徐々に高さが低くなり、その先端は切り欠かれて再び山部10に連通する開口13が形成されている。中間谷部12の底部の深さは、谷部11の底部の位置と同一である。   In the corrugated plate 1 shown in FIG. 2, the crests 10 and the troughs 11 are alternately continued in a direction orthogonal to the exhaust gas flow direction. In the peak portion 10, a plurality of concave intermediate valley portions 12 are formed in parallel to the exhaust gas flow direction and spaced from each other. The intermediate valley portion 12 gradually decreases in height from the upstream side to the downstream side of the exhaust gas, and the tip thereof is cut away to form an opening 13 communicating with the mountain portion 10 again. The depth of the bottom of the intermediate valley 12 is the same as the position of the bottom of the valley 11.

また谷部11には、凸状の中間山部14が排ガス流れ方向に平行に互いに間隔を隔てて複数個形成されている。中間山部14は、排ガス流れ方向において二つの中間谷部12の間に配置され、その高さは山部10の高さと同一である。   In the valley portion 11, a plurality of convex intermediate mountain portions 14 are formed in parallel to the exhaust gas flow direction and spaced from each other. The intermediate mountain portion 14 is disposed between the two intermediate valley portions 12 in the exhaust gas flow direction, and the height thereof is the same as the height of the mountain portion 10.

複数の波状板1は、図3にも示すように、中間谷部12及び中間山部14の位相が排ガス流れ方向及び排ガス流れ方向と直角方向でそれぞれ同一となるように平板3と交互に積層され、フィルタエレメントの排ガス流れ方向に直角に切断した断面において中間谷部12及び中間山部14はそれぞれ同一位置となるように配置されている。また山部10は上側の平板3に当接し、谷部11は下側の平板3に当接している。   As shown in FIG. 3, the plurality of corrugated plates 1 are alternately laminated with the flat plate 3 so that the phases of the intermediate valley portions 12 and the intermediate mountain portions 14 are the same in the exhaust gas flow direction and in the direction perpendicular to the exhaust gas flow direction. The intermediate valley portion 12 and the intermediate mountain portion 14 are arranged at the same position in the cross section cut at right angles to the exhaust gas flow direction of the filter element. Further, the peak portion 10 is in contact with the upper flat plate 3, and the valley portion 11 is in contact with the lower flat plate 3.

このフィルタ装置では、図4〜図7に示すように、波状板1の表面側では、中間山部14と隣接する両側の山部10と上側の平板3とで流路の大部分が閉塞されたフィルタ導入部 100が形成されている。また波状板1の裏面側では、中間谷部12と隣接する両側の谷部11と下側の平板3とで流路の大部分が閉塞されたフィルタ導入部 101が形成されている。そしてフィルタ導入部 100の上流側では、中間谷部12の位置で山部10の高さが低くなり、開口13が形成されているので、谷部11を流れる排ガスは両側の開口13から両側の山部10へ分岐流入可能であり、その部分にフィルタ迂回部 200が形成されている。また裏面側では、フィルタ導入部 101の上流側の中間山部14の位置で谷部11の深さが浅くなり、開口15が形成されているので、山部10を流れる排ガスは両側の開口15から両側の谷部11へ分岐流入可能であり、その部分にもフィルタ迂回部 201が形成されている。   In this filter device, as shown in FIGS. 4 to 7, on the surface side of the corrugated plate 1, most of the flow path is blocked by the peak portions 10 on both sides adjacent to the intermediate peak portion 14 and the upper flat plate 3. A filter introduction part 100 is formed. Further, on the back side of the corrugated plate 1, a filter introduction portion 101 is formed in which most of the flow path is closed by the valley portions 11 on both sides adjacent to the intermediate valley portion 12 and the lower flat plate 3. Further, on the upstream side of the filter introduction part 100, the height of the peak part 10 is lowered at the position of the intermediate valley part 12, and the opening 13 is formed, so that the exhaust gas flowing through the valley part 11 flows from the opening 13 on both sides to the both sides. A branch can flow into the mountain portion 10, and a filter bypass portion 200 is formed there. In addition, on the back side, the depth of the valley portion 11 becomes shallow and the opening 15 is formed at the position of the intermediate peak portion 14 on the upstream side of the filter introduction portion 101. Can flow into the troughs 11 on both sides, and the filter bypassing part 201 is also formed there.

そして図4に示すように、谷部11と上側の平板3との間に形成された流路を流れる排ガスは、中間山部14に衝突し、上側の平板3のPM捕集量が少ない状態では、大部分の排ガスは上側の平板3を透過して平板3の反対側に存在する波状板1の谷部11に流入し、PMの大部分が平板3で捕集される。   And as shown in FIG. 4, the exhaust gas which flows through the flow path formed between the trough part 11 and the upper flat plate 3 collides with the intermediate mountain part 14, and the amount of PM trapped on the upper flat plate 3 is small. Then, most of the exhaust gas passes through the upper flat plate 3 and flows into the trough 11 of the corrugated plate 1 existing on the opposite side of the flat plate 3, and most of PM is collected by the flat plate 3.

PM捕集量が増大してフィルタ導入部 100における排ガスの圧力が高くなると、図5に示すように排ガスはフィルタ導入部 100の平板3を通過しにくくなり、点線矢印に示すように上流側に存在するフィルタ迂回部 200において中間谷部12から開口13を通過して隣接する山部10に分岐流入する。したがって排気圧損の上昇が抑制される。   When the amount of collected PM increases and the pressure of the exhaust gas at the filter introduction part 100 increases, the exhaust gas does not easily pass through the flat plate 3 of the filter introduction part 100 as shown in FIG. In the existing filter bypass part 200, it branches from the intermediate valley part 12 through the opening 13 and flows into the adjacent peak part 10. Therefore, an increase in exhaust pressure loss is suppressed.

同様に山部10と下側の平板3の間に形成された流路を流れる排ガスは、図6に示すようにフィルタ導入部 101において中間谷部12に衝突し、下側の平板3のPM捕集量が少ない状態では、大部分の排ガスは下側の平板3を透過して平板3の反対側に存在する波状板1の谷部11に流入し、これによりPMの大部分が平板3で捕集される。   Similarly, the exhaust gas flowing through the flow path formed between the peak portion 10 and the lower flat plate 3 collides with the intermediate valley portion 12 in the filter introduction portion 101 as shown in FIG. In a state where the collected amount is small, most of the exhaust gas passes through the lower flat plate 3 and flows into the trough portion 11 of the corrugated plate 1 on the opposite side of the flat plate 3. It is collected at.

PM捕集量が増大してフィルタ導入部 101における排ガスの圧力が高くなると、図7に示すように排ガスはフィルタ導入部 100の平板3を通過しにくくなり、点線矢印に示すように排ガスは上流側に存在するフィルタ迂回部 201において中間山部14から開口15を通過して隣接する谷部11に分岐流入する。したがって排気圧損の上昇が抑制される。   When the amount of collected PM increases and the pressure of the exhaust gas at the filter introduction part 101 increases, the exhaust gas becomes difficult to pass through the flat plate 3 of the filter introduction part 100 as shown in FIG. The filter bypass portion 201 located on the side passes through the opening 15 from the intermediate peak portion 14 and branches into the adjacent valley portion 11. Therefore, an increase in exhaust pressure loss is suppressed.

本比較例のフィルタ装置によれば、排ガス流入側端面から流出側端面に向かって上記サイクルが連続的に繰り返されることで、フィルタ導入部 100、 101において平板3にPMが捕集される。そして多数のフィルタ導入部 100、 101が形成されているので、PMは平板3の全体に均一に分散して捕集されることとなり、捕集効率が向上するとともに、PMが捕集されても排気圧損が上昇しにくい。すなわちPM捕集効率の向上と、排気圧損の上昇の抑制とが両立することになる。   According to the filter device of this comparative example, PM is collected on the flat plate 3 in the filter introduction units 100 and 101 by continuously repeating the above-described cycle from the exhaust gas inflow side end surface toward the outflow side end surface. Since a large number of filter introduction parts 100 and 101 are formed, PM is uniformly dispersed and collected over the entire flat plate 3, and the collection efficiency is improved and PM is collected. Exhaust pressure loss is unlikely to rise. That is, the improvement of the PM collection efficiency and the suppression of the increase of the exhaust pressure loss are compatible.

(実施例1)
本実施例のフィルタ装置は、排ガス流入側端部における波状板の構造が異なること以外は、比較例1と同様の構造である。本実施例のフィルタ装置では、図8及び図9に示すように、排ガス流入側端面には、下流側に切欠かれた開口をもつ山部10が形成され、その下流側開口に連続して谷部11が形成されている。この谷部11には、深さが徐々に浅くなる逆中間谷部16が形成され、逆中間谷部16は下流側の山部10に連続して、この部分に最上流のフィルタ迂回部 202が形成されている。
Example 1
The filter device of this example has the same structure as that of Comparative Example 1 except that the structure of the corrugated plate at the end portion on the exhaust gas inflow side is different. In the filter device of the present embodiment, as shown in FIGS. 8 and 9, the exhaust gas inflow side end face is formed with a peak portion 10 having an opening cut out on the downstream side, and the valley is continuously formed on the downstream side opening. Part 11 is formed. In this valley portion 11, an inverted intermediate valley portion 16 having a gradually shallower depth is formed. The inverted intermediate valley portion 16 is continuous with the downstream peak portion 10, and the upstreammost filter bypassing portion 202 is formed in this portion. Is formed.

すなわち本実施例のフィルタ装置では、図9に矢印で示すように、排ガスは上流側端面から先ず山部10に流入し、山部10から出た排ガスは谷部11から逆中間谷部16に流入する。逆中間谷部16は下流側の山部10に連続しているので、先端部上面が平板3で塞がれている。しかしその部分にPMが堆積したとしても、逆中間谷部16の途中までは平板3との間に隙間があり、排ガスはその隙間から両側の谷部11に分岐して流入する。   That is, in the filter device of this embodiment, as indicated by arrows in FIG. 9, the exhaust gas first flows into the peak portion 10 from the upstream end face, and the exhaust gas that has exited from the peak portion 10 passes from the valley portion 11 to the reverse intermediate valley portion 16. Inflow. Since the reverse intermediate valley portion 16 is continuous with the peak portion 10 on the downstream side, the top surface of the tip end portion is covered with the flat plate 3. However, even if PM accumulates in that portion, there is a gap with the flat plate 3 up to the middle of the reverse intermediate valley portion 16, and the exhaust gas branches and flows into the valley portions 11 on both sides from the gap.

したがって最上流にフィルタ迂回部 202が形成されているので、排ガス流入側端面へのPMの堆積が抑制され、端面閉塞が防止されるとともに、過度の昇温による溶損も回避できる。   Therefore, since the filter detour portion 202 is formed in the most upstream, PM accumulation on the exhaust gas inflow side end surface is suppressed, end surface blockage is prevented, and melting damage due to excessive temperature rise can be avoided.

(実施例2)
本実施例のフィルタ装置は、排ガス流入側端部における波状板1の構造が異なること以外は、比較例1と同様の構造である。本実施例のフィルタ装置では、図10に示すように、排ガス流入側端面には谷部11と、谷部11に形成され上流側に開口するとともに下流側に向かって高さが徐々に低くなり下流側の谷部11に連続する逆中間山部17が形成され、この部分に最上流のフィルタ迂回部 202が形成されている。
(Example 2)
The filter device of the present embodiment has the same structure as that of the comparative example 1 except that the structure of the corrugated plate 1 at the exhaust gas inflow side end is different. In the filter device of the present embodiment, as shown in FIG. 10, a trough 11 is formed on the exhaust gas inflow side end surface, and the trough 11 is formed in the trough 11 and opens upstream, and the height gradually decreases toward the downstream. An inverted intermediate mountain 17 that is continuous with the valley 11 on the downstream side is formed, and the most upstream filter bypass 202 is formed in this portion.

すなわち本実施例のフィルタ装置では、図10に矢印で示すように、排ガスは上流側端面から先ず谷部11に流入し、次いで逆中間山部17に流入する。逆中間山部17は徐々に高さが低くなって下流側の谷部11に連続しているので、裏面側では先端部下面が平板3で塞がれている。しかしその部分にPMが堆積したとしても、逆中間山部17の途中までは平板3との間に隙間があり、排ガスはその隙間から両側の山部10に分岐して流入する。   That is, in the filter device of the present embodiment, as indicated by arrows in FIG. 10, the exhaust gas first flows into the valley portion 11 from the upstream end face, and then flows into the reverse intermediate mountain portion 17. Since the reverse intermediate mountain portion 17 gradually decreases in height and continues to the valley portion 11 on the downstream side, the lower surface of the tip portion is closed by the flat plate 3 on the back surface side. However, even if PM accumulates in that portion, there is a gap with the flat plate 3 up to the middle of the reverse intermediate peak portion 17, and the exhaust gas branches into the peak portions 10 on both sides and flows in from the gap.

したがって最上流にフィルタ迂回部 202が形成されているので、排ガス流入側端面へのPMの堆積が抑制され、端面閉塞が防止されるとともに、過度の昇温による溶損も回避できる。   Therefore, since the filter detour portion 202 is formed in the most upstream, PM accumulation on the exhaust gas inflow side end surface is suppressed, end surface blockage is prevented, and melting damage due to excessive temperature rise can be avoided.

(実施例3)
図11に示す本実施例のフィルタ装置は、排ガス流入側端部における平板3の構造が異なること以外は、比較例1と同様の構造である。平板3は、排ガス流入側端部のみが金属板30から形成され、その金属板30には、孔径数mmの貫通孔31が複数個形成されている。
(Example 3)
The filter device of the present embodiment shown in FIG. 11 has the same structure as that of Comparative Example 1 except that the structure of the flat plate 3 at the exhaust gas inflow side end is different. Only the exhaust gas inflow side end of the flat plate 3 is formed from a metal plate 30, and a plurality of through holes 31 having a hole diameter of several mm are formed in the metal plate 30.

すなわち本実施例のフィルタ装置では、フィルタ導入部 100の上流側に貫通孔31が形成されているので、山部10に流入した排ガスはPMとともに貫通孔31を通過して裏面側に積層された次の波状板1に流入する。したがって最上流にフィルタ迂回部 202が形成されているので、排ガス流入側端面へのPMの堆積が抑制され、端面閉塞が防止されるとともに、過度の昇温による溶損も回避できる。   That is, in the filter device of the present embodiment, since the through hole 31 is formed on the upstream side of the filter introduction part 100, the exhaust gas flowing into the peak part 10 passes through the through hole 31 together with PM and is laminated on the back side. It flows into the next corrugated plate 1. Therefore, since the filter detour portion 202 is formed in the most upstream, PM accumulation on the exhaust gas inflow side end surface is suppressed, end surface blockage is prevented, and melting damage due to excessive temperature rise can be avoided.

(実施例4)
図12に示す本実施例のフィルタ装置は、排ガス流入側端部における平板3の構造が異なること以外は、比較例1と同様の構造である。平板3は排ガス流れ方向の長さが波状板1より短くされ、波状板1の排ガス流入側端部では、山部10の下側には平板3が存在していない。
Example 4
The filter device of the present embodiment shown in FIG. 12 has the same structure as that of Comparative Example 1 except that the structure of the flat plate 3 at the exhaust gas inflow side end is different. The length of the flat plate 3 in the exhaust gas flow direction is shorter than that of the corrugated plate 1, and the flat plate 3 does not exist below the peak portion 10 at the exhaust gas inflow side end of the corrugated plate 1.

すなわち本実施例のフィルタ装置では、フィルタ導入部 100の上流側で平板3が存在しないので、山部10に流入した排ガスはPMとともに裏面側に積層された次の波状板1に流入する。したがって最上流にフィルタ迂回部 202が形成されているので、排ガス流入側端面へのPMの堆積が抑制され、端面閉塞が防止されるとともに、過度の昇温による溶損も回避できる。   That is, in the filter device of this embodiment, since the flat plate 3 does not exist on the upstream side of the filter introduction unit 100, the exhaust gas flowing into the peak portion 10 flows into the next corrugated plate 1 laminated on the back side together with PM. Therefore, since the filter detour portion 202 is formed in the most upstream, PM accumulation on the exhaust gas inflow side end surface is suppressed, end surface blockage is prevented, and melting damage due to excessive temperature rise can be avoided.

(比較例2)
独国実用新案 20,117,873 U1号の実施例1に記載のフィルタ装置を比較例2とした。
(Comparative Example 2)
The filter device described in Example 1 of German utility model 20,117,873 U1 was used as Comparative Example 2.

すなわち比較例2のフィルタ装置は、比較例1と同様の波状板1が用いられ、比較例1と同様の平板3と交互に積層されているが、比較例1における排ガス入口側が出口側に、出口側が入口側となるように、 180度反転されている。   That is, the filter device of Comparative Example 2 uses the same corrugated plate 1 as in Comparative Example 1, and is alternately laminated with the same flat plate 3 as in Comparative Example 1, but the exhaust gas inlet side in Comparative Example 1 is on the outlet side, It is inverted 180 degrees so that the exit side becomes the entrance side.

<試験・評価>
実施例1〜4及び比較例1〜2のフィルタ装置を用い、PM捕集率と排気圧損及び前端面閉塞率を測定した。フィルタエレメントは、それぞれ直径 130mm、長さ75mmの約1Lのものであり、断面の面積1平方インチあたりのセル数はそれぞれ 200セルである。
<Test and evaluation>
Using the filter devices of Examples 1 to 4 and Comparative Examples 1 and 2, the PM collection rate, the exhaust pressure loss, and the front end face blocking rate were measured. The filter elements are about 1 L each having a diameter of 130 mm and a length of 75 mm, and the number of cells per square inch of the cross section is 200 cells.

実施例と比較例の各フィルタ装置をそれぞれディーゼルエンジンの排気管に装着し、その上流側に 1.3Lの酸化触媒を配置した。そして高濃度のPMが排出される条件である2Lエンジン、 UDC疑似モードにて、EGR 全開状態で10時間運転し、フィルタの前端面におけるセル開口がPMで閉塞されている割合を目視で測定した。また、定常走行時(2Lエンジン、2400rpm 、50Nm、PM排出量3g/hr)においてPM堆積量が1g/Lとなった時点でのPM捕集率と排気圧損を測定した。結果を表1に示す。なお、ここでいうPMは煤(スート)を意味している。   The filter devices of the example and the comparative example were respectively mounted on the exhaust pipe of a diesel engine, and a 1.3 L oxidation catalyst was disposed upstream thereof. Then, in the 2L engine, which is a condition for discharging high concentration PM, UDC pseudo mode, it was operated for 10 hours in the EGR fully open state, and the ratio of the cell opening on the front end face of the filter being blocked with PM was visually measured. . Further, the PM collection rate and the exhaust pressure loss were measured when the PM accumulation amount became 1 g / L during steady running (2 L engine, 2400 rpm, 50 Nm, PM emission amount 3 g / hr). The results are shown in Table 1. Note that PM here means soot.

Figure 2006247532
Figure 2006247532

表1より、実施例1〜4のフィルタ装置は比較例1のフィルタ装置に比べて前端面閉塞率が低いことがわかり、これは最上流にフィルタ迂回部 202を形成した効果であることが明らかである。また実施例1〜4のフィルタ装置は、比較例2のフィルタ装置に比べてPM捕集効率が高く、排気圧損の上昇も大きく抑制されていることがわかり、これらの差異は波状板1の構造の差異に起因していることも明らかである。   From Table 1, it can be seen that the filter devices of Examples 1 to 4 have a lower front end face blocking rate than the filter device of Comparative Example 1, and this is the effect of forming the filter bypass portion 202 in the uppermost stream. It is. Moreover, it turns out that the filter apparatus of Examples 1-4 has high PM collection efficiency compared with the filter apparatus of the comparative example 2, and the raise of exhaust pressure loss is also suppressed largely, These differences are the structures of the corrugated board 1 It is also clear that this is due to the difference.

本発明の排ガス浄化フィルタ装置は、そのまま用いてもよいし、波状板及び平板の少なくとも一部表面にPtなどの触媒金属を担持したフィルタ触媒とすることもできる。触媒金属は波状板及び平板の少なくとも一部に直接担持することもできるし、多孔質酸化物からなるコート層を形成し、そのコート層に担持してもよい。このようなフィルタ触媒とすることで、PMを捕集と同時に酸化燃焼を促進することができる。また触媒金属によって、排ガス中のHC、COなどの有害ガス成分を浄化することも可能となる。   The exhaust gas purification filter device of the present invention may be used as it is, or may be a filter catalyst in which a catalyst metal such as Pt is supported on at least a part of the corrugated plate and the flat plate. The catalyst metal may be directly supported on at least a part of the corrugated plate and the flat plate, or a coating layer made of a porous oxide may be formed and supported on the coating layer. By setting it as such a filter catalyst, oxidation combustion can be promoted simultaneously with PM collection. Moreover, it becomes possible to purify harmful gas components such as HC and CO in the exhaust gas by the catalytic metal.

比較例1のフィルタ装置の斜視図と要部拡大斜視図である。It is the perspective view of the filter apparatus of the comparative example 1, and the principal part expansion perspective view. 比較例1のフィルタ装置に用いた波状板の要部斜視図である。5 is a perspective view of a main part of a corrugated plate used in the filter device of Comparative Example 1. FIG. 比較例1のフィルタ装置の要部拡大断面図である。6 is an enlarged cross-sectional view of a main part of a filter device of Comparative Example 1. FIG. 比較例1のフィルタ装置の要部拡大断面図である。6 is an enlarged cross-sectional view of a main part of a filter device of Comparative Example 1. FIG. 比較例1のフィルタ装置の要部拡大断面図である。6 is an enlarged cross-sectional view of a main part of a filter device of Comparative Example 1. FIG. 比較例1のフィルタ装置の要部拡大断面図である。6 is an enlarged cross-sectional view of a main part of a filter device of Comparative Example 1. FIG. 比較例1のフィルタ装置の要部拡大断面図である。6 is an enlarged cross-sectional view of a main part of a filter device of Comparative Example 1. FIG. 実施例1のフィルタ装置の斜視図と要部拡大斜視図である。It is the perspective view of the filter apparatus of Example 1, and the principal part expansion perspective view. 実施例1のフィルタ装置に用いた波状板の要部斜視図である。It is a principal part perspective view of the corrugated board used for the filter apparatus of Example 1. FIG. 実施例2のフィルタ装置に用いた波状板の要部斜視図である。It is a principal part perspective view of the corrugated board used for the filter apparatus of Example 2. FIG. 実施例3のフィルタ装置の要部斜視図である。It is a principal part perspective view of the filter apparatus of Example 3. FIG. 実施例4のフィルタ装置の要部斜視図である。It is a principal part perspective view of the filter apparatus of Example 4.

符号の説明Explanation of symbols

1:波状板 3:平板 4:外筒 10:山部
11:谷部 12:中間谷部 13:開口 14:中間山部
15:開口 16:逆中間谷部 17:逆中間山部
100、 101:フィルタ導入部 200、 201、 202:フィルタ迂回部
1: Corrugated plate 3: Flat plate 4: Outer tube 10: Mountain
11: Valley 12: Middle valley 13: Opening 14: Middle mountain
15: Opening 16: Reverse intermediate valley 17: Reverse intermediate mountain
100, 101: Filter introduction part 200, 201, 202: Filter bypass part

Claims (7)

複数の排ガス流路と、該排ガス流路に設置されたフィルタと、を有する排ガス浄化フィルタ装置であって、
該排ガス流路は、排ガスを該フィルタへ導くフィルタ導入部と、該フィルタ導入部に隣接する該排ガス流路へ分岐して該フィルタ導入部を迂回するフィルタ迂回部と、を有し、
最上流の該フィルタ迂回部は、最上流の該フィルタ導入部より上流側に設けられ排ガス入口側端面に開口していることを特徴とする排ガス浄化フィルタ装置。
An exhaust gas purification filter device having a plurality of exhaust gas passages and a filter installed in the exhaust gas passages,
The exhaust gas flow path has a filter introduction part that guides the exhaust gas to the filter, and a filter bypass part that branches to the exhaust gas flow path adjacent to the filter introduction part and bypasses the filter introduction part,
The exhaust gas purification filter device, wherein the most upstream filter bypassing portion is provided upstream of the upstreammost filter introduction portion and is open to an end surface on the exhaust gas inlet side.
金属薄板よりなり山部と谷部とが排ガス流れ方向と交差する方向に交互に連続する波状板と、耐熱性繊維が集積されてなり前記フィルタを構成するガス透過性の平板と、が交互に積層されてなり、
該山部は山高さが低くなることで形成された凹状の中間谷部を有し、該中間谷部は隣接する該谷部から排ガスが分岐して流入可能な分岐部とその下流側で該山部に連通する開口とよりなる前記フィルタ迂回部を構成し、
該谷部は谷深さが浅くなることで形成された凸状の中間山部を有し、該中間山部と隣接する両側の該山部と該山部に接する該平板とで流路が閉塞された前記フィルタ導入部を構成し、
該フィルタ導入部内の圧力が高まった場合に、該谷部を流れる排ガスの少なくとも一部が該フィルタ導入部から該フィルタ導入部の上流側に存在する該フィルタ迂回部を通過して隣接する該山部に流入し、最上流では排ガスは先ず最上流の該フィルタ迂回部に流入するように構成された請求項1に記載の排ガス浄化フィルタ装置。
A corrugated plate made of a thin metal plate and having alternating peaks and valleys alternately in the direction intersecting the exhaust gas flow direction, and gas permeable flat plates constituting heat-resistant fibers and constituting the filter alternately. Laminated,
The peak portion has a concave middle valley portion formed by lowering the mountain height, and the middle valley portion has a branch portion where exhaust gas can branch from the adjacent valley portion and can flow in, and downstream of the branch portion. Constructing the filter detour part comprising an opening communicating with the mountain part,
The valley portion has a convex intermediate peak portion formed by decreasing the depth of the valley, and the flow path is formed by the peak portions on both sides adjacent to the intermediate peak portion and the flat plate in contact with the peak portion. Constituting the blocked filter introduction part,
When the pressure in the filter introduction part increases, at least a part of the exhaust gas flowing through the valley part passes through the filter bypass part existing upstream from the filter introduction part and is adjacent to the mountain. The exhaust gas purifying filter device according to claim 1, wherein the exhaust gas purifying filter device is configured to flow into the first part and to flow into the filter detour part at the uppermost stream first.
金属薄板よりなり山部と谷部とが排ガス流れ方向と交差する方向に交互に連続する波状板と、耐熱性繊維が集積されてなりフィルタを構成するガス透過性の平板と、が交互に積層されてなり、
該谷部は谷深さが浅くなることで形成された凸状の中間山部を有し、該中間山部は隣接する該山部から排ガスが分岐して流入可能な分岐部とその下流側で該谷部に連通する開口とよりなるフィルタ迂回部を構成し、
該山部は山高さが低くなることで形成された凹状の中間谷部を有し、該中間谷部と隣接する両側の該谷部と該谷部に接する該平板とで流路が閉塞されたフィルタ導入部を構成し、
該フィルタ導入部内の圧力が高まった場合に、該山部を流れる排ガスの少なくとも一部が該フィルタ導入部から該フィルタ導入部の上流側に存在する該フィルタ迂回部を通過して隣接する該谷部に流入し、最上流では排ガスは先ず最上流の該フィルタ迂回部に流入するように構成された請求項1に記載の排ガス浄化フィルタ装置。
A corrugated plate made of a thin metal plate, with ridges and valleys alternately arranged in the direction intersecting the exhaust gas flow direction, and gas-permeable flat plates that constitute a filter made up of heat-resistant fibers are laminated alternately. Being
The valley portion has a convex intermediate mountain portion formed by a shallow valley depth, and the intermediate mountain portion is a branched portion where exhaust gas can branch from the adjacent mountain portion and can flow in, and the downstream side thereof. And a filter bypass portion composed of an opening communicating with the valley portion.
The peak portion has a concave intermediate valley portion formed by decreasing the peak height, and the flow path is blocked by the valley portion on both sides adjacent to the intermediate valley portion and the flat plate in contact with the valley portion. The filter introduction part,
When the pressure in the filter introduction part increases, at least part of the exhaust gas flowing through the peak part passes through the filter bypass part existing on the upstream side of the filter introduction part from the filter introduction part and is adjacent to the valley. The exhaust gas purifying filter device according to claim 1, wherein the exhaust gas purifying filter device is configured to flow into the first part and to flow into the filter detour part at the uppermost stream first.
最上流の前記フィルタ迂回部は、上流側開口と下流側開口をもつ前記山部と、該下流側開口に連続した前記谷部と、該谷部の深さが徐々に浅くなり下流側の前記山部に連続する逆中間谷部と、よりなる請求項2又は請求項3に記載の排ガス浄化フィルタ装置。   The most upstream filter bypass portion includes the crest portion having an upstream opening and a downstream opening, the trough portion continuous to the downstream opening, and the depth of the trough portion gradually becoming shallower, The exhaust gas purification filter device according to claim 2 or 3, further comprising an inverted intermediate valley portion that is continuous with the mountain portion. 最上流の前記フィルタ迂回部は、前記谷部と、該谷部に形成され上流側端部に開口するとともに下流側に向かって高さが徐々に低くなり下流側の前記谷部に連続する逆中間山部と、よりなる請求項2又は請求項3に記載の排ガス浄化フィルタ装置。   The most upstream filter bypass portion is formed in the valley and the reverse formed in the valley and opening at the upstream end and gradually lowering toward the downstream and continuing to the valley on the downstream side. The exhaust gas purification filter device according to claim 2 or 3, comprising an intermediate mountain portion. 最上流の前記フィルタ迂回部は、前記波状板の下側に積層された前記平板の前記山部に対向する位置に形成された排ガス中の粒子状物質が透過可能な貫通孔である請求項2又は請求項3に記載の排ガス浄化フィルタ装置。   The uppermost filter bypass portion is a through-hole through which particulate matter in the exhaust gas is formed at a position facing the peak portion of the flat plate stacked below the corrugated plate. Or the exhaust gas purification filter apparatus of Claim 3. 最上流の前記フィルタ迂回部は、前記波状板の下側に積層された前記平板の前記山部に対向する位置に形成された排ガス中の粒子状物質が透過可能な切欠き部である請求項2又は請求項3に記載の排ガス浄化フィルタ装置。   The uppermost filter bypass portion is a cutout portion through which particulate matter in the exhaust gas can be transmitted, which is formed at a position facing the crest portion of the flat plate stacked below the corrugated plate. The exhaust gas purification filter device according to claim 2 or claim 3.
JP2005067849A 2004-04-12 2005-03-10 Exhaust gas purification filter device Expired - Fee Related JP5044101B2 (en)

Priority Applications (7)

Application Number Priority Date Filing Date Title
JP2005067849A JP5044101B2 (en) 2005-03-10 2005-03-10 Exhaust gas purification filter device
RU2006139958/15A RU2343961C2 (en) 2004-04-12 2005-04-12 Device for exhaust gas treatment
KR1020067021142A KR100860327B1 (en) 2004-04-12 2005-04-12 Exhaust gas purifying apparatus
DE602005025992T DE602005025992D1 (en) 2004-04-12 2005-04-12 EMISSION CONTROL DEVICE
EP05730342A EP1735077B1 (en) 2004-04-12 2005-04-12 Exhaust gas purifying apparatus
PCT/JP2005/007377 WO2005099867A1 (en) 2004-04-12 2005-04-12 Exhaust gas purifying apparatus
US11/578,041 US7959868B2 (en) 2004-04-12 2005-04-12 Exhaust gas purifying apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2005067849A JP5044101B2 (en) 2005-03-10 2005-03-10 Exhaust gas purification filter device

Publications (2)

Publication Number Publication Date
JP2006247532A true JP2006247532A (en) 2006-09-21
JP5044101B2 JP5044101B2 (en) 2012-10-10

Family

ID=37088564

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2005067849A Expired - Fee Related JP5044101B2 (en) 2004-04-12 2005-03-10 Exhaust gas purification filter device

Country Status (1)

Country Link
JP (1) JP5044101B2 (en)

Also Published As

Publication number Publication date
JP5044101B2 (en) 2012-10-10

Similar Documents

Publication Publication Date Title
US7566425B2 (en) Refractory exhaust filtering method and apparatus
US8673064B2 (en) Partial wall-flow filter and method
JP5313159B2 (en) Partial wall flow filter and diesel exhaust system and method
KR100860327B1 (en) Exhaust gas purifying apparatus
US9757675B2 (en) Partial wall-flow filter and method
US8012244B2 (en) Method of removing particulates from exhaust gases, and corresponding fiber layer, particulate filter, exhaust system and vehicle
JP2002113798A (en) Honeycomb form using nonwoven fabric of metal fiber
TW200809077A (en) Bypass flow filter with improved filter efficiency
JP4868713B2 (en) Exhaust gas purification filter device
US7563415B2 (en) Catalytic exhaust filter device
US20140238242A1 (en) Ceramic partial wall-flow filter with low deep bed
JP4347120B2 (en) Exhaust gas purification device
AU2006311275B2 (en) Refractory exhaust filtering method and device
JP4868714B2 (en) Exhaust gas purification filter catalyst
JP5044101B2 (en) Exhaust gas purification filter device
JP2005296820A (en) Filter catalyst for cleaning exhaust gas
JP4648269B2 (en) Exhaust gas particulate matter removal filter, exhaust gas purification apparatus and exhaust gas purification method using the filter
JP4358054B2 (en) Exhaust gas purification honeycomb structure
JP2006329042A (en) Diesel exhaust emission control device and operation control method
JP2006226185A (en) Device and method for purifying exhaust gas containing particular matter
JP2003155909A (en) Filter for diesel particulate filter device
MX2008005953A (en) Refractory exhaust filtering method and device
JP2006102636A (en) Diesel exhaust emission treatment apparatus

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20080216

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20100202

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20100427

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20110628

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20110906

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20120626

A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20120713

R151 Written notification of patent or utility model registration

Ref document number: 5044101

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R151

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20150720

Year of fee payment: 3

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

LAPS Cancellation because of no payment of annual fees