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JP4868713B2 - Exhaust gas purification filter device - Google Patents

Exhaust gas purification filter device Download PDF

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JP4868713B2
JP4868713B2 JP2004117189A JP2004117189A JP4868713B2 JP 4868713 B2 JP4868713 B2 JP 4868713B2 JP 2004117189 A JP2004117189 A JP 2004117189A JP 2004117189 A JP2004117189 A JP 2004117189A JP 4868713 B2 JP4868713 B2 JP 4868713B2
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Prior art keywords
filter
exhaust gas
valley
flat plate
peak
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JP2005296818A (en
JP2005296818A5 (en
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進 皿井
誠治 大河原
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Toyota Motor Corp
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Toyota Motor Corp
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Priority to JP2004117189A priority Critical patent/JP4868713B2/en
Application filed by Toyota Motor Corp filed Critical Toyota Motor Corp
Priority to DE602005025992T priority patent/DE602005025992D1/en
Priority to EP05730342A priority patent/EP1735077B1/en
Priority to CN 200580011086 priority patent/CN100500258C/en
Priority to US11/578,041 priority patent/US7959868B2/en
Priority to KR1020067021142A priority patent/KR100860327B1/en
Priority to PCT/JP2005/007377 priority patent/WO2005099867A1/en
Priority to ES05730342T priority patent/ES2358978T3/en
Priority to RU2006139958/15A priority patent/RU2343961C2/en
Publication of JP2005296818A publication Critical patent/JP2005296818A/en
Publication of JP2005296818A5 publication Critical patent/JP2005296818A5/ja
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    • Y02T10/144
    • Y02T10/24

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  • Processes For Solid Components From Exhaust (AREA)
  • Exhaust Gas Treatment By Means Of Catalyst (AREA)
  • Exhaust Gas After Treatment (AREA)
  • Filtering Materials (AREA)
  • Filtering Of Dispersed Particles In Gases (AREA)
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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捕集量が多い場合など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 collected PM 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 both are wall flow type filters, 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

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ことを課題とする。   This invention is made | formed in view of such a situation, and makes it a subject to make compatible the improvement of the collection efficiency of PM, and suppression of the raise of exhaust pressure loss.

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、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るガス透過性の平板と、が交互に積層されてなり、山部及び谷部が排ガス流路を構成し、平板がフィルタを構成する排ガス浄化フィルタ装置であって、
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、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、
波状板の上側に平板が積層された部位において、
中間山部と中間山部に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排ガスをフィルタへ導くフィルタ導入部を構成し、
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り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するように構成されたことにある。
A feature of the exhaust gas purifying filter device of the present invention that solves the above problems is that a corrugated plate made of a thin metal plate and having a crest and a trough alternately continuous in a direction intersecting the exhaust gas flow direction, and heat-resistant fibers are integrated. The gas permeable flat plates are alternately stacked, the crests and troughs constitute the exhaust gas flow path, and the flat plates constitute the filter.
The valley has a convex intermediate peak formed by the valley depth being shallow, and the peak has a concave intermediate valley formed by the peak height being reduced,
In the part where the flat plate is laminated on the upper side of the corrugated plate,
The intermediate crest and the crests on both sides adjacent to the crest and the flat plate in contact with the crest form a filter introduction part that blocks the flow path and guides exhaust gas to the filter,
The middle valley portion is composed of a branch portion where the exhaust gas branches off from the adjacent valley portion and can flow in, and an opening communicating with the mountain portion on the downstream side, and branches to the exhaust gas flow channel adjacent to the filter introduction portion. Configure the bypass filter part to bypass,
When the pressure in the filter introduction portion increases, at least a part of the exhaust gas flowing through the valley portion passes from the filter introduction portion to the adjacent peak portion through the filter bypass portion existing on the upstream side of the filter introduction portion. That is to be configured.

この場合、フィルタ導入部の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い。   In this case, it is desirable that there is a crest of an adjacent corrugated plate on the opposite side of the filter introduction portion through the flat plate.

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、中間谷部と中間谷部に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、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、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するように構成されている。 Moreover, if the characteristics of this exhaust gas purification filter device are expressed from the back side of the corrugated plate, the filter introduction portion in which the flow path is blocked by the intermediate valley portion, the valley portions on both sides adjacent to the intermediate valley portion, and the flat plate in contact with the valley portion The intermediate peak portion constitutes a filter bypass portion consisting of a branch portion into which exhaust gas branches off from an adjacent peak portion and can flow in, and an opening communicating with the valley portion on the downstream side, and the pressure in the filter introduction portion is When the height increases, at least a part of the exhaust gas flowing through the peak portion is configured to flow from the filter introduction portion to the adjacent valley portion through the filter bypass portion existing on the upstream side of the filter introduction portion.

この場合は、フィルタ導入部の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。   In this case, it is desirable that a trough portion of an adjacent corrugated plate exists on the opposite side of the filter introduction portion through the flat plate.

中間谷部及び中間山部は、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。   It is desirable that the intermediate valley portion and the intermediate mountain portion are formed by deforming the mountain portion or the valley portion, and that the upstream end portion is smoothly continuous toward the bottom portion or the top portion, respectively.

また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%以上であることが好ましく、フィルタ導入部の合計容積は、山部及び谷部の全合計容積の50%以上であることが好ましい。   Further, the opening area of the corrugated plate in plan view in the filter introduction portion is preferably 30% or more of the total opening area of the corrugated plate in plan view, and the total volume of the filter introduction portion is the total of the peaks and valleys. It is preferably 50% or more of the total volume.

さらに、排ガス流路及びフィルタの少なくとも一方には、多孔質酸化物担体に貴金属を担持してなる触媒層が形成されていることが望ましい。   Furthermore, it is desirable that at least one of the exhaust gas flow path and the filter is formed with a catalyst layer in which a noble metal is supported on a porous oxide carrier.

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。したがって、捕集されたPMを燃焼させる再生処理までの時間を長くすることができる。   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. Therefore, the time until the regeneration process for burning the collected PM can be increased.

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、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, 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4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 4 is especially preferable. In the exhaust gas purification 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4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 4, on the back side of the corrugated plate, the back side of the intermediate valley portion is convex to form a filter introduction portion between the peak portion and the lower flat plate, and the upstream valley portion. 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.

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 automobile exhaust gas purification filter device, 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.

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.

(実施例1)
図1に本実施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60μmの波状板1と、ステンレス繊維製不織布からなる目付量 450g/m2 、厚さ60μm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。
Example 1
FIG. 1 is a perspective view and an enlarged view of a main part of the filter device of the present embodiment, FIG. 2 is an essential part perspective view of a corrugated plate, and FIGS. This filter device is made by alternately laminating corrugated plate 1 made of stainless steel and having a thickness of 60 μm and flat plate 3 having a basis weight of 450 g / m 2 and a thickness of 60 μm made of stainless steel nonwoven fabric. 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, a filter is introduced in which 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. Part 100 is formed. Further, on the back side of the corrugated plate 1, a filter introduction portion 101 is formed in which 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.

したがって本実施例の排ガス浄化フィルタ装置によれば、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。   Therefore, according to the exhaust gas purification filter device of the present embodiment, as shown in FIG. 4, the exhaust gas flowing through the flow path formed between the valley portion 11 and the upper flat plate 3 collides with the intermediate mountain portion 14, In a state where the amount of PM trapped on the upper flat plate 3 is small, most of the exhaust gas passes through the upper flat plate 3 and flows into the valleys 11 of the corrugated plate 1 on the opposite side of the flat plate 3, and most of the 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の実線矢印に示すように排ガスは逆流し、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 in the filter introduction section 100 increases, the exhaust gas flows backward as shown by the solid line arrow in FIG. 5 and in the filter bypass section 200 existing on the upstream side as shown by the dotted line arrow. The intermediate valley portion 12 passes through the opening 13 and branches into the adjacent mountain portion 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、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. When the collected amount is small, most of the exhaust gas passes through the lower flat plate 3 and flows into the valley 11 of the corrugated plate 1 on the opposite side of the flat plate 3, and most of the PM is captured by the flat plate 3. Be collected.

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の実線矢印に示すように排ガスは逆流し、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 unit 101 increases, the exhaust gas flows backward as shown by the solid line arrow in FIG. 7, and the exhaust gas flows upstream as shown by the dotted line arrow. In 201, the water flows into the adjacent valley portion 11 through the opening 15 from the intermediate mountain portion 14 and flows into the adjacent valley portion 11. Therefore, an increase in exhaust pressure loss is suppressed.

本実施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 the present embodiment, PM is collected on the flat plate 3 in the filter introduction parts 100 and 101 by continuously repeating the cycle from the exhaust gas inflow side end face toward the outflow side end face. 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.

さらに本実施例のフィルタ装置では、フィルタ導入部 100、 101における平面視での波状板1の開口面積は、平面視における波状板1の合計開口面積の約40%を占め、フィルタ導入部 100、 101の合計容積は、山部10及び谷部11の合計容積の約50%を占めている。これにより平板3の利用面積が大きく、PMの捕集効率が高く排気圧損の上昇が抑制されている。   Further, in the filter device of the present embodiment, the opening area of the corrugated plate 1 in the plan view in the filter introducing portions 100 and 101 occupies about 40% of the total opening area of the corrugated plate 1 in the plan view. The total volume of 101 occupies about 50% of the total volume of the peak 10 and the valley 11. Thereby, the utilization area of the flat plate 3 is large, the PM collection efficiency is high, and the increase in exhaust pressure loss is suppressed.

(実施例2)
本実施例のフィルタ装置は、波状板1の積層状態が異なること以外は実施例1と同様である。このフィルタ装置では、図8に示すように、実施例1と同様の波状板1を、正逆交互に、つまり平板3の表面と平行に 180度ずつ交互に反転させながら積層している。
(Example 2)
The filter device of this example is the same as that of Example 1 except that the laminated state of the corrugated plates 1 is different. In this filter device, as shown in FIG. 8, corrugated plates 1 similar to those of the first embodiment are laminated while being reversed alternately forward and reverse, that is, alternately by 180 degrees parallel to the surface of the flat plate 3.

本実施例のフィルタ装置でも、実施例1より劣るものの、PM捕集効率の向上と排気圧損の上昇抑制の効果が発現される。   Even in the filter device of the present embodiment, although it is inferior to the first embodiment, the effect of improving the PM collection efficiency and suppressing the increase in exhaust pressure loss is exhibited.

(比較例)
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とした。
(Comparative example)
The filter apparatus described in Example 1 of German utility model 20,117,873 U1 was used as a comparative example.

すなわち比較例のフィルタ装置は、実施例1と同様の波状板1が用いられ、実施例1と同様の平板3と交互に積層されているが、実施例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 the comparative example uses the same corrugated plate 1 as in the first embodiment and is alternately laminated with the flat plate 3 as in the first embodiment, but the exhaust gas inlet side in the first embodiment is on the outlet side, and the outlet Inverted 180 degrees so that the side is the entrance side.

<試験・評価>
実施例1及び比較例のフィルタ装置を用い、PM捕集率と排気圧損を測定した。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 device of Example 1 and the comparative example, the PM collection rate and the exhaust pressure loss 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1と比較例の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、定常走行時のPM捕集効率と排気圧損を所定時間毎に測定した。エンジンからのPM排出量は既知であるので、測定時間に応じて捕集されたPM量が計算され、捕集PM量に対するPM捕集効率と排気圧損の測定値を図9に示す。   The filter devices of Example 1 and the comparative example were respectively attached to the exhaust pipe of a diesel engine, and PM collection efficiency and exhaust pressure loss during steady running were measured every predetermined time. Since the PM emission amount from the engine is known, the PM amount collected according to the measurement time is calculated, and the measured values of PM collection efficiency and exhaust pressure loss with respect to the collected PM amount are shown in FIG.

図9より、実施例1のフィルタ装置は比較例のフィルタ装置に比べてPM捕集効率が高く、排気圧損の上昇が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が明らかである。   From FIG. 9, it can be seen that the filter device of Example 1 has higher PM collection efficiency than the filter device of the comparative example, and the increase in exhaust pressure loss is suppressed, and these differences are the differences in the structure of the corrugated plate 1. It is clear that this is caused by

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することができ、再生処理を不要とすることができる。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 using such a filter catalyst, PM can be oxidized and burned at the same time as collection, and regeneration processing can be made unnecessary. Moreover, it becomes possible to purify harmful gas components such as HC and CO in the exhaust gas by the catalytic metal.

本発明一実施例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 and main part expansion perspective view of the filter apparatus of one Example of this invention. 本発明一実施例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 one Example of this invention. 本発明一実施例のフィルタ装置の要部拡大断面図である。It is a principal part expanded sectional view of the filter apparatus of one Example of this invention. 本発明一実施例のフィルタ装置の要部拡大断面図である。It is a principal part expanded sectional view of the filter apparatus of one Example of this invention. 本発明一実施例のフィルタ装置の要部拡大断面図である。It is a principal part expanded sectional view of the filter apparatus of one Example of this invention. 本発明一実施例のフィルタ装置の要部拡大断面図である。It is a principal part expanded sectional view of the filter apparatus of one Example of this invention. 本発明一実施例のフィルタ装置の要部拡大断面図である。It is a principal part expanded sectional view of the filter apparatus of one Example of this invention. 本発明第2実施例のフィルタ装置を示す要部拡大断面図である。It is a principal part expanded sectional view which shows the filter apparatus of 2nd Example of this invention. 実施例及び比較例のフィルタ装置のPM捕集量に対するPM捕集率及び排気圧損の関係を示すグラフである。It is a graph which shows the relationship between the PM collection rate with respect to the PM collection amount of the filter apparatus of an Example and a comparative example, and exhaust pressure loss.

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 100、 101:フィルタ導入部 200、 201: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 100, 101: Filter introduction part 200, 201: Filter bypass part

Claims (6)

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るガス透過性の平板と、が交互に積層されてなり、該山部及び該谷部が排ガス流路を構成し、該平板がフィルタを構成する排ガス浄化フィルタ装置であって、
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、
該波状板の上側に該平板が積層された部位において、
該中間山部と該中間山部に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排ガスを該フィルタへ導くフィルタ導入部を構成し、
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り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するように構成されたことを特徴とする排ガス浄化フィルタ装置。
A corrugated plate made of a thin metal plate and alternately continuous in a direction in which peaks and troughs intersect the exhaust gas flow direction, and a gas permeable flat plate in which heat-resistant fibers are accumulated, are alternately laminated, The peak portion and the valley portion constitute an exhaust gas flow path, and the flat plate is an exhaust gas purification filter device constituting a filter,
The valley has a convex intermediate peak formed by a shallow valley depth, the peak has a concave intermediate valley formed by a low peak height,
In the portion where the flat plate is laminated on the upper side of the corrugated plate,
A flow path is blocked by the intermediate crests and the crests on both sides adjacent to the intermediate crests and the flat plate in contact with the crests to constitute a filter introduction part that guides exhaust gas to the filter;
The intermediate valley portion includes a branch portion into which exhaust gas branches off from the adjacent valley portion, and an opening communicating with the peak portion on the downstream side, and branches into the exhaust gas flow channel adjacent to the filter introduction portion. A filter bypass unit that bypasses the filter introduction unit,
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. An exhaust gas purifying filter device configured to flow into a section.
前記フィルタ導入部の前記平板を介した反対側には、隣接する前記波状板の前記山部が存在している請求項1に記載の排ガス浄化フィルタ装置。   2. The exhaust gas purification filter device according to claim 1, wherein the peak portion of the adjacent corrugated plate is present on the opposite side of the filter introduction portion through the flat plate. 前記中間谷部及び前記中間山部は、前記山部又は前記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請求項1に記載の排ガス浄化フィルタ装置。The said intermediate | middle valley part and the said intermediate | middle peak part are formed by deform | transforming the said peak part or the said valley part, respectively, and each upstream end part is continuing smoothly toward the bottom part or the top part. Exhaust gas purification filter device. 前記フィルタ導入部からその上流側に存在する前記フィルタ迂回部の開口の位置までにおける前記谷部の平面視での開口面積の合計値は、平面視における前記谷部の合計開口面積の30%以上である請求項1に記載の排ガス浄化フィルタ装置。The total value of the opening area in plan view of the valley from the filter introduction part to the position of the opening of the filter bypass part existing upstream is 30% or more of the total opening area of the valley in plan view The exhaust gas purification filter device according to claim 1. 前記フィルタ導入部からその上流側に存在する前記フィルタ迂回部の開口の位置までにおける前記谷部の合計容積は、前記谷部の全合計容積の50%以上である請求項1に記載の排ガス浄化フィルタ装置。2. The exhaust gas purification according to claim 1, wherein a total volume of the valley portion from the filter introduction portion to a position of an opening of the filter bypass portion existing upstream thereof is 50% or more of a total total volume of the valley portion. Filter device. 前記排ガス流路及び前記フィルタの少なくとも一方には、多孔質酸化物担体に貴金属を担持してなる触媒層が形成されている請求項1に記載の排ガス浄化フィルタ装置。The exhaust gas purification filter device according to claim 1, wherein a catalyst layer in which a noble metal is supported on a porous oxide carrier is formed in at least one of the exhaust gas flow path and the filter.
JP2004117189A 2004-04-12 2004-04-12 Exhaust gas purification filter device Expired - Fee Related JP4868713B2 (en)

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JP2004117189A JP4868713B2 (en) 2004-04-12 2004-04-12 Exhaust gas purification filter device
RU2006139958/15A RU2343961C2 (en) 2004-04-12 2005-04-12 Device for exhaust gas treatment
CN 200580011086 CN100500258C (en) 2004-04-12 2005-04-12 Exhaust gas cleaning device
US11/578,041 US7959868B2 (en) 2004-04-12 2005-04-12 Exhaust gas purifying apparatus
KR1020067021142A KR100860327B1 (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
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
ES05730342T ES2358978T3 (en) 2004-04-12 2005-04-12 EXHAUST GAS PURIFICATION DEVICE.

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