JPH10131739A - Emission control device - Google Patents
Emission control deviceInfo
- Publication number
- JPH10131739A JPH10131739A JP8285292A JP28529296A JPH10131739A JP H10131739 A JPH10131739 A JP H10131739A JP 8285292 A JP8285292 A JP 8285292A JP 28529296 A JP28529296 A JP 28529296A JP H10131739 A JPH10131739 A JP H10131739A
- Authority
- JP
- Japan
- Prior art keywords
- filter
- trapper
- exhaust gas
- pressure loss
- gas purifying
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 238000011144 upstream manufacturing Methods 0.000 claims abstract description 21
- 239000000463 material Substances 0.000 claims abstract description 8
- 239000010419 fine particle Substances 0.000 claims description 4
- 230000004323 axial length Effects 0.000 claims description 3
- 238000005452 bending Methods 0.000 claims description 3
- 239000002184 metal Substances 0.000 abstract description 10
- 235000012054 meals Nutrition 0.000 abstract 1
- 239000002245 particle Substances 0.000 abstract 1
- 238000007789 sealing Methods 0.000 abstract 1
- 230000000052 comparative effect Effects 0.000 description 8
- 238000009434 installation Methods 0.000 description 6
- 238000011049 filling Methods 0.000 description 5
- 238000000034 method Methods 0.000 description 5
- 239000011148 porous material Substances 0.000 description 5
- 230000007423 decrease Effects 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 238000000746 purification Methods 0.000 description 3
- 230000033228 biological regulation Effects 0.000 description 2
- 239000000919 ceramic Substances 0.000 description 2
- 239000011810 insulating material Substances 0.000 description 2
- 230000008929 regeneration Effects 0.000 description 2
- 238000011069 regeneration method Methods 0.000 description 2
- 238000004904 shortening Methods 0.000 description 2
- 229910018072 Al 2 O 3 Inorganic materials 0.000 description 1
- 229910000838 Al alloy Inorganic materials 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 229910018487 Ni—Cr Inorganic materials 0.000 description 1
- 238000003915 air pollution Methods 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- WYTGDNHDOZPMIW-RCBQFDQVSA-N alstonine Natural products C1=CC2=C3C=CC=CC3=NC2=C2N1C[C@H]1[C@H](C)OC=C(C(=O)OC)[C@H]1C2 WYTGDNHDOZPMIW-RCBQFDQVSA-N 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 230000008602 contraction Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 230000002542 deteriorative effect Effects 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000013618 particulate matter Substances 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
Landscapes
- Exhaust Gas After Treatment (AREA)
- Processes For Solid Components From Exhaust (AREA)
- Filtering Of Dispersed Particles In Gases (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】この発明は、エンジンの排気
系の途中に設ける排気ガス浄化装置に関する。詳しく
は、優れた微粒子捕集性能と圧力損失特性を確保し、さ
らに、自動車等に対するスペース面での設置規制も緩和
した排気ガス浄化装置である。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an exhaust gas purifying device provided in an exhaust system of an engine. More specifically, it is an exhaust gas purifying apparatus that ensures excellent particulate collection performance and pressure loss characteristics, and that further reduces installation restrictions on space for automobiles and the like.
【0002】[0002]
【従来の技術】ディーゼルエンジンから発生する排気ガ
スには、カーボンを主体とする可燃性微粒子が含まれて
いる。この微粒子は、パティキュレートマター(以下P
Mと記す)と称され、大気汚染の原因となることから、
これを除去する排気ガス浄化の技術が種々開発されてい
る。2. Description of the Related Art Exhaust gas generated from a diesel engine contains combustible fine particles mainly composed of carbon. These fine particles are made of particulate matter (hereinafter P
M), which causes air pollution.
Various exhaust gas purification techniques have been developed to eliminate this.
【0003】例えば、一部で既に実用化されている浄化
装置の中に、セラミックの多孔体を用いてトラッパを構
成し、そのトラッパで捕集したPMをヒータやバーナで
焼却して排気ガスの通りが悪くなったトラッパを再生す
るものがある。また、最近では、金属多孔体を用いてト
ラッパを構成する装置も開発されている。For example, a trapper is formed by using a ceramic porous body in a purification device that has already been put into practical use in part, and PM trapped by the trapper is incinerated by a heater or a burner to remove exhaust gas. Some regenerate trappers whose streets have gone bad. Recently, an apparatus for forming a trapper using a porous metal body has also been developed.
【0004】これ等の装置によるPM捕集原理は、フィ
ルタによる濾過である。この方式の装置は、特に重要な
性能として、PM捕集性能が高いこと及び、堆積したP
Mによって生じるフィルタ部での圧力損失(以下圧損と
いう)が小さいことが要求される。[0004] The principle of trapping PM by these devices is filtration by a filter. The apparatus of this type has particularly important performances such as high PM trapping performance and accumulated P
It is required that the pressure loss (hereinafter referred to as pressure loss) in the filter portion caused by M is small.
【0005】この2つの要求性能のうち、捕集性能につ
いては、フィルタの目孔を微細にしてフィルタに流入す
るPM量と捕集されるPM量の比で決まる捕集効率を高
める方法があるが、この方法を採ると、PMが主にフィ
ルタの排気ガス流入側表面に堆積して圧損が急激に上昇
する。[0005] Among the two required performances, regarding the trapping performance, there is a method of increasing the trapping efficiency determined by the ratio of the amount of PM flowing into the filter to the amount of PM trapped by making the pores of the filter fine. However, if this method is adopted, PM mainly accumulates on the exhaust gas inflow side surface of the filter, and the pressure loss rises sharply.
【0006】そこで、(1)フィルタの目孔を微細化
し、同時に捕集面積を広げる構造や、(2)フィルタに
よるPM捕集がフィルタ厚さ方向の各部で3次元的に行
われるようにしてフィルタ厚みを増加させる構造、にし
て圧損上昇を抑えることが考えられている。In view of this, (1) a structure in which the pores of the filter are made finer and the collection area is enlarged at the same time, and (2) PM collection by the filter is performed three-dimensionally in each part in the thickness direction of the filter. It has been considered that the thickness of the filter is increased to suppress an increase in pressure loss.
【0007】なお、(2)の構造については、フィルタ
を筒状にしたり、平板フィルタ材をつづら折れの状態に
折り曲げた形にして捕集面積を拡大することが提案され
ている。[0007] Regarding the structure (2), it has been proposed to increase the collection area by making the filter into a tubular shape or by bending a flat filter material into a folded shape.
【0008】また、(3)特開昭56−18016号公
報や特開昭57−190626号公報などに示されるよ
うに、目の粗いフィルタと目の細かいフィルタを前者が
排気路の上流側にあるように軸方向に積層配置して捕集
効率を高める提案もある。これも、(2)の構造を利用
した装置の一種といえる。(3) As shown in JP-A-56-18016 and JP-A-57-190626, a filter having a coarser filter and a filter having a finer filter are provided on the upstream side of the exhaust passage. There is also a proposal to increase the collection efficiency by arranging them in the axial direction as is. This can also be said to be a type of device utilizing the structure of (2).
【0009】[0009]
【発明が解決しようとする課題】上述した従来技術のう
ち、(1)の構造は、フィルタの表面にひだをつけるな
どして捕集面積を拡大する必要があるので、フィルタ形
状が複雑化し、フィルタ製造が難しくなるほか、フィル
タ強度にも影響が出てくる。Among the above-mentioned prior arts, the structure of (1) requires an increase in the trapping area by, for example, forming a fold on the surface of the filter. In addition to the difficulty in manufacturing the filter, the strength of the filter is affected.
【0010】また、(2)の構造は、筒状フィルタやつ
づら折れのフィルタを用いてその厚みを増加させると、
トラッパの外径が大きくなり、装置外径も大きくなって
しまう。In the structure of (2), when the thickness is increased by using a cylindrical filter or a broken filter,
The outer diameter of the trapper increases, and the outer diameter of the device also increases.
【0011】車両用の排気ガス浄化装置は、通常、車両
の床下に消音器と代替えして設けられるが、床下に確保
できる高さスペースには限りがある。車両の低床化が進
んでいる最近の状況においては、大きなスペース確保が
特に難しくなってきているため、外径の大きな浄化装置
はスペース面で設置規制を受ける。An exhaust gas purifying device for a vehicle is usually provided under the floor of the vehicle in place of a muffler, but the height space that can be secured under the floor is limited. In recent years where the floor of vehicles is being reduced, it is particularly difficult to secure a large space, and therefore, a purification device having a large outer diameter is subject to installation restrictions in terms of space.
【0012】さらに、(3)の構造は、目孔サイズの異
なるフィルタが縦列に並べられており、フィルタ厚みを
増加させてもトラッパの軸方向長さが長くなるだけでト
ラッパ径は大きくならないが、フィルタの捕集面積が小
さいため、圧損特性の改善効果が薄く、頻繁な再生が必
要となる結果、トラッパ寿命が短かくなる。Further, in the structure (3), filters having different eye sizes are arranged in tandem, and even if the thickness of the filter is increased, only the axial length of the trapper is increased, but the trapper diameter does not increase. In addition, since the collection area of the filter is small, the effect of improving the pressure loss characteristics is small, and frequent regeneration is required, so that the life of the trapper is shortened.
【0013】この発明は、フィルタ形状が複雑にならな
い3次元捕集原理のトラッパを用いて高捕集効率と低圧
損の両特性を両立させ、さらに、装置の外径増加を抑え
てスペース面での設置規制も緩和できるようにすること
を課題としている。According to the present invention, both characteristics of high collection efficiency and low pressure loss are achieved by using a trapper of a three-dimensional collection principle that does not complicate the shape of a filter. The issue is to make it possible to ease the restrictions on the installation of such facilities.
【0014】[0014]
【課題を解決するための手段】この発明の排気ガス浄化
装置は、排気ガス中の微粒子を捕集するフィルタ部が、
複数の筒状の3次元的に入り込んだ骨格をもつフィル
タ、もしくは3次元的に入り込んだ骨格をもつ平板フィ
ルタ材をつづら折れの状態に折り曲げたフィルタで形成
され、このフィルタ部を備えるトラッパをケース内に複
数個直列配置にして設置したものである。According to the exhaust gas purifying apparatus of the present invention, the filter for collecting fine particles in the exhaust gas comprises:
A trapper formed of a plurality of cylindrical filters having a three-dimensionally inserted skeleton or a filter formed by bending a three-dimensionally inserted skeletal flat plate filter material into a folded state, and having a trapper provided with this filter portion as a case. A plurality of them are arranged in series.
【0015】この装置は、フィルタ部の捕集面積に差を
つけたトラッパを、捕集面積大のトラッパほど排気路の
上流側にあるように並べたり、フィルタ部の軸方向長さ
に差をつけたトラッパを、フィルタ部長さ大のトラッパ
ほど排気路の上流側にあるように並べたりすると望まし
い。In this apparatus, trappers having different collection areas of the filter section are arranged such that the trapper having a larger collection area is located on the upstream side of the exhaust path, or the difference in the axial length of the filter section is reduced. It is desirable to arrange the attached trappers so that the trapper having a longer filter portion is located on the upstream side of the exhaust path.
【0016】また、直列に並べるトラッパのうち、排気
路の下流側にあるものほどフィルタを厚くしたり、フィ
ルタの目孔を小さくしたりするのも有効なことであり、
この構造と上記の望ましいとした構造を併用するとより
好ましい。It is also effective to increase the thickness of the filter and decrease the size of the filter hole as the trappers arranged in series are located downstream of the exhaust path.
It is more preferable to use this structure in combination with the above-mentioned desirable structure.
【0017】[0017]
【作用】PMを3次元的に捕集する場合の捕集効率η
は、トラッパを構成するフィルタの厚さt、フィルタの
単位厚さt0 の比t/t0 をn(無次元数)とし、さら
にフィルタの単位厚さ当りの捕集効率をη0 とすると、
次式で表される。[Effect] Collection efficiency η when collecting PM three-dimensionally
Is defined as n (a dimensionless number) a ratio t / t 0 of the thickness t of the filter constituting the trapper and the unit thickness t 0 of the filter, and η 0 as a collection efficiency per unit thickness of the filter. ,
It is expressed by the following equation.
【0018】η=1−(1−η0 )n この発明の装置は、トラッパが直列に複数個数並べられ
ており、全体的に見るとフィルタを多層構造にしたのと
等価な状態になっているため、フィルタの実質厚みが増
加し、捕集効率ηが向上する。さらに、PM捕集に最も
有効なフィルタの表面が複数あり、表面での捕集が複数
回繰返えされるので、捕集効率はより向上する。Η = 1− (1−η 0 ) n In the device of the present invention, a plurality of trappers are arranged in series, and as a whole, it is equivalent to a filter having a multilayer structure. Therefore, the substantial thickness of the filter increases, and the collection efficiency η improves. Furthermore, since there are a plurality of filter surfaces most effective for PM collection and the collection on the surface is repeated a plurality of times, the collection efficiency is further improved.
【0019】また、各トラッパが筒状又はつづら折れの
フィルタを用いて構成されており、しかも、それぞれの
フィルタが独立しているので捕集面積も広く、多量のP
Mを捕集したときの圧損上昇も小さく抑えられる。Further, each trapper is formed using a cylindrical or serpentine filter, and since each filter is independent, a trapping area is large and a large amount of P
An increase in pressure loss when M is collected can be suppressed to a small value.
【0020】更に、トラッパ数をひとつにし、そのトラ
ッパの筒状フィルタやつづら折れのフィルタの厚みを増
加させる方法で捕集性能と圧損特性を向上させると、ト
ラッパ外径が増大し、フィルタ製造も難しくなってくる
(厚いものは製造し難い)が、この発明の装置は、多層
構造のフィルタで必要厚みを確保するため、各層のフィ
ルタを厚くする必要がなく、トラッパ外径(つまりは装
置外径)を小さく抑えることができ、フィルタの製造が
困難になることもない。Further, if the number of trappers is reduced to one, and the trapping performance and pressure drop characteristics are improved by increasing the thickness of the cylindrical filter or the broken filter of the trapper, the outer diameter of the trapper increases, and the manufacture of the filter also increases. Although it becomes difficult (thicker ones are difficult to manufacture), the device of the present invention does not require the filters of each layer to be thicker in order to secure the required thickness with a filter having a multi-layer structure. Diameter) can be kept small, and there is no difficulty in manufacturing the filter.
【0021】なお、複数個のトラッパを直列配置したこ
とによって装置の長さが長くなるが、車両の床下スペー
スは、長さ方向には充分な余裕があるので、装置径を小
さくすれば長さは増加しても設置規制が緩和される。Although the length of the device is increased by arranging a plurality of trappers in series, the space under the floor of the vehicle has a sufficient margin in the length direction. Even if it increases, installation regulations will be relaxed.
【0022】次に、上流側のトラッパほど捕集面積を大
きくすると、圧損の上昇を抑えて装置の更なる小型化を
図ることができる。その理由を下に述べる。Next, if the trapping area of the trapper on the upstream side is increased, the increase in pressure loss can be suppressed, and the size of the apparatus can be further reduced. The reason is described below.
【0023】排気ガス中のPM濃度は、トラッパ通過に
よって下がっていくので下流側のトラッパほど流入する
PM量が減少して捕集するPM量が少なくなる。一方、
圧損は、一般に捕集PM量が増加するに従って増大す
る。従って、捕集量が少なくて済む下流側のトラッパ
は、上流側トラッパと同等の圧損特性を捕集面積を小さ
くして確保することができ、この捕集面積縮小により装
置が更に小型化される。Since the PM concentration in the exhaust gas decreases by passing through the trapper, the amount of PM flowing in decreases as the trapper is located downstream, so that the amount of PM trapped decreases. on the other hand,
Pressure loss generally increases as the amount of trapped PM increases. Therefore, the trapper on the downstream side, which requires a small amount of trapping, can secure the same pressure loss characteristics as the trapper on the upstream side by reducing the trapping area, and the apparatus is further downsized by reducing the trapping area. .
【0024】ここで、捕集面積の縮小は、(イ)フィル
タの長さを短くする、(ロ)多重筒フィルタの場合には
筒数を少なくする、(ハ)つづら折れフィルタの場合は
平板フィルタ材の折り曲げ回数を少なくするの各方法で
行える。(イ)の方法を採ると装置長さが短縮され、ま
た、(ロ)、(ハ)の方法を採ると装置径が縮小され
る。先に述べたように、装置長さは、装置の設置規制に
対して大して影響しないが、装置は取扱いの便や無駄な
設置スペースの削減の面からより小型であるに越したこ
とはなく、この点で、長さの短縮も有効なことと言え
る。Here, the collection area can be reduced by (a) shortening the length of the filter, (b) reducing the number of cylinders in the case of a multi-cylinder filter, and (c) flat plate in the case of a broken filter. It can be performed by each method of reducing the number of times the filter material is bent. When the method (a) is employed, the length of the apparatus is reduced, and when the methods (b) and (c) are employed, the diameter of the apparatus is reduced. As mentioned earlier, the device length has little effect on the device installation regulations, but the device is still smaller in terms of ease of handling and reduction of wasted installation space. In this regard, it can be said that shortening the length is also effective.
【0025】また、トラッパのフィルタ厚を厚くするこ
とにより捕集性能が向上する。上流側、下流側に関係な
く、各トラッパともフィルタ厚を厚くすれば捕集性能の
改善が図れるが、圧損特性の面からは、下流側トラッパ
のフィルタ厚を厚くするのが望ましい。圧損は、捕集P
M量に対して2次関数的に増大するので、ひとつのフィ
ルタで多量のPMを捕集するよりも、複数のフィルタで
平均的に捕集する方が装置の総圧損が小さく抑えられる
からである。下流側トラッパは、上流側トラッパに比べ
て流入する総PM量が少なく、従って、下流側トラッパ
のフィルタ厚を厚くして下流側トラッパの捕集効率を上
流側トラッパの捕集効率よりも高くすると、複数フィル
タによるPM捕集量の平均化が図れる。The trapping performance is improved by increasing the thickness of the trapper filter. Regardless of the upstream side or the downstream side, the trapping performance can be improved by increasing the filter thickness of each trapper, but from the viewpoint of pressure loss characteristics, it is desirable to increase the filter thickness of the downstream trapper. The pressure loss is collected P
Since it increases quadratically with respect to the amount of M, the average pressure loss of the apparatus can be suppressed to be smaller by collecting a plurality of filters on average than by collecting a large amount of PM by one filter. is there. The downstream trapper has a smaller total PM amount flowing in than the upstream trapper, and therefore, if the filter thickness of the downstream trapper is increased and the collection efficiency of the downstream trapper is made higher than the collection efficiency of the upstream trapper. In addition, the amount of PM trapped by the plurality of filters can be averaged.
【0026】下流側トラッパの捕集効率は、フィルタの
目孔を小さくすることによっても高め得るが、この発明
では、3次元捕集のメカニズムによって捕集がなされる
フィルタを用いるので、目孔を小さくする構造よりもフ
ィルタ厚を増加させて捕集効率を上げる方が有利であ
る。Although the trapping efficiency of the downstream trapper can be increased by reducing the size of the holes in the filter, in the present invention, a filter is used which is collected by a three-dimensional trapping mechanism. It is more advantageous to increase the filter thickness to increase the collection efficiency than to make the structure smaller.
【0027】図1は、フィルタの厚さと充填率(孔径が
小さいほど充填率が高い)を変化させたときの捕集効率
と圧損の変化を比較している。これから判るように、捕
集効率は、フィルタ厚を厚くする、フィルタの充填率を
高める(目孔を小さくする)のどちらによっても向上す
るが、充填率を高めると圧損が上昇するのに対し、フィ
ルタ厚を増大させる場合にはその圧損増加がなく、圧損
特性を悪化させずに捕集性能を改善することができる。FIG. 1 compares the change in the collection efficiency and the change in pressure loss when the thickness and the filling rate (the smaller the pore size, the higher the filling rate) of the filter. As can be seen, the collection efficiency can be improved by either increasing the filter thickness or increasing the filter filling rate (reducing the pore size). However, increasing the filling rate increases the pressure loss. When the filter thickness is increased, the pressure loss does not increase, and the trapping performance can be improved without deteriorating the pressure loss characteristics.
【0028】なお、この発明の装置は、複数のトラッパ
をひとつのケースに収納する。複数トラッパの直列配置
は、ひとつのケースにひとつのトラッパを収納した装置
を直列に接続する構造でも実現できるが、これは圧損特
性及びトラッパ再生時の熱効率の面で得策でない。即
ち、PM捕集の特に初期の圧損は、トラッパによるもの
よりもケースによるものの方が圧倒的に大きい。このケ
ースによる圧損は、排気路が小径配管から大径ケース、
その後再度小径配管へと拡大、縮小を繰り返すことによ
って生じるので、ケース(即ち装置)を多段に配置する
と、その段数に比例して圧損が増加する。In the apparatus of the present invention, a plurality of trappers are housed in one case. The serial arrangement of a plurality of trappers can also be realized by a structure in which devices in which one trapper is housed in one case are connected in series, but this is not advisable in terms of pressure loss characteristics and thermal efficiency during trapper regeneration. That is, the pressure drop in the PM collection, particularly in the initial stage, is much larger in the case than in the trapper. The pressure loss due to this case is as follows.
After that, it is caused by repeating expansion and contraction to a small-diameter pipe again. Therefore, if the cases (that is, devices) are arranged in multiple stages, the pressure loss increases in proportion to the number of stages.
【0029】また、ケースを多段に配置すると、捕集し
たPMを電気ヒータで加熱して燃焼させる際の熱効率も
低下する。ケースの外周部は断熱材を巻いて熱の逃げを
抑制できるが、ケースの両端部は断熱材で包むことがで
きず、そこが放熱面となって内部の熱が外に逃げる。ケ
ースの数が多くなれば、それだけ放熱面が増えて外部に
逃げる熱量が多くなり、安定したPM燃焼のためにはヒ
ータ出力が余分に必要になる。ケースをひとつにするこ
の発明の装置は、かかる不具合が生じない。Further, when the cases are arranged in multiple stages, the heat efficiency when the collected PM is heated by the electric heater and burned is also reduced. The outer periphery of the case can be wrapped with a heat insulating material to prevent heat from escaping, but the ends of the case cannot be wrapped with the heat insulating material, which serves as a heat radiating surface to allow the internal heat to escape. As the number of cases increases, the heat radiation surface increases and the amount of heat escaping to the outside increases, and an extra heater output is required for stable PM combustion. The device of the present invention having one case does not have such a problem.
【0030】[0030]
【発明の実施の形態】図2乃至図8に、この発明の排気
ガス浄化装置の実施形態を簡略化して示す。図2の装置
は、金属製のケース1内に、トラッパ2を2個、直列配
置にして収納したものである。2 to 8 show a simplified embodiment of an exhaust gas purifying apparatus according to the present invention. The apparatus shown in FIG. 2 has two trappers 2 housed in a metal case 1 arranged in series.
【0031】トラッパ2は、金属多孔体製の異径円筒状
フィルタ3、4を同心的に配置し、必要箇所を端板7等
で塞いで上流側と下流側からケース軸方向に交互に内部
に入り込む流路8、9を生じさせ、さらに、流路8に電
気ヒータ10を挿入して作られている。電気ヒータ10
は、流路9内に配置してもよいが、流路8、9のどちら
に組込む場合も、フィルタの表面に広く対面する面状ヒ
ータが好ましい。The trapper 2 has concentrically arranged cylindrical filters 3 and 4 made of a porous metal body and covers necessary portions with an end plate 7 or the like, and alternately has an internal portion in the case axial direction from the upstream side and the downstream side. Channels 8 and 9 are formed to enter, and an electric heater 10 is inserted into the channel 8. Electric heater 10
May be arranged in the flow path 9, but in the case of being incorporated in either of the flow paths 8 and 9, a planar heater widely facing the surface of the filter is preferable.
【0032】この装置は、図中左側を入口とすると、そ
こからケース1内に流入した排気ガスが矢印で示すよう
に流れ、その間に2つのトラッパ2を通過して浄化され
る。In this apparatus, when the left side in the figure is an inlet, the exhaust gas flowing into the case 1 therefrom flows as shown by the arrows, and passes through the two trappers 2 to be purified.
【0033】排気ガスは、図中右側からケース1内に導
入してもよく、このときには、ガスの流れが図とは逆に
なる。The exhaust gas may be introduced into the case 1 from the right side in the figure, and at this time, the flow of the gas is opposite to that in the figure.
【0034】図3の装置は、下流側(図中右側)トラッ
パ2のフィルタ部長さを上流側トラッパのフィルタ部長
さよりも短かくして各トラッパの圧損を平均化したも
の、さらに、図4の装置は、ケース1内に収納するトラ
ッパ2を3個とし、下流側(図中右側)のトラッパほど
フィルタ部長さを短かくして各トラッパの圧損の平均化
を図ったものである。The apparatus shown in FIG. 3 is configured such that the length of the filter section of the downstream trapper 2 (right side in the figure) is shorter than the length of the filter section of the upstream trapper to average the pressure loss of each trapper. The number of trappers 2 accommodated in the case 1 is three, and the length of the filter portion is shorter in the trapper on the downstream side (right side in the figure), so that the pressure loss of each trapper is averaged.
【0035】また、図5の装置は、金属多孔体製の1個
の円筒状フィルタ3を用いてトラッパ12を形成し、か
つ下流側(図中右側)トラッパ12のフィルタ厚を上流
側トラッパ12のフィルタ厚よりも大きくし、このトラ
ッパ12を2個、金属ケース1内に直列に収納してお
り、装置外径の縮小効果が特に高い。また、下流側トラ
ッパの捕集効率が高くなっており、各トラッパの圧損の
平均化も図られている。In the apparatus shown in FIG. 5, the trapper 12 is formed by using one cylindrical filter 3 made of a porous metal body, and the filter thickness of the downstream (right side in the figure) trapper 12 is adjusted by the upstream trapper 12. , And two of the trappers 12 are housed in series in the metal case 1, so that the effect of reducing the outer diameter of the apparatus is particularly high. In addition, the trapping efficiency of the downstream trappers is high, and the pressure loss of each trapper is averaged.
【0036】図6の装置は、金属ケース1内に3個のト
ラッパ12を直列に収納し、下流側トラッパのフィルタ
部長さを図中左端の最上流トラッパのフィルタ部長さよ
りも短かくし、さらに、下流側トラッパほどフィルタ厚
を厚くしたもので、この点が図5の装置と異なる。In the apparatus shown in FIG. 6, three trappers 12 are accommodated in series in the metal case 1, and the length of the filter portion of the downstream trapper is made shorter than the length of the filter portion of the most upstream trapper at the left end in the figure. This filter differs from the apparatus in FIG. 5 in that the filter thickness is increased in the downstream trapper.
【0037】図7の装置は、金属多孔体製の異径円筒状
フィルタ3、4、5を同心的に組合わせて作ったトラッ
パ22と、図1の装置のトラッパと同様の構成にしたト
ラッパ2を、トラッパ22が排気路の上流側にあるよう
にして金属ケース1内に直列に挿入したもので、上流側
トラッパの捕集面積が大きいため、これも各トラッパの
圧損の平均化が図れる。なお、以上の装置に用いるフィ
ルタは角筒状のものであってもよい。The apparatus shown in FIG. 7 includes a trapper 22 formed by concentrically combining different diameter cylindrical filters 3, 4, and 5 made of a porous metal body, and a trapper having the same configuration as the trapper of the apparatus shown in FIG. 2 are inserted in series in the metal case 1 so that the trapper 22 is located on the upstream side of the exhaust path. Since the trapping area of the upstream trapper is large, the pressure loss of each trapper can also be averaged. . The filter used in the above device may be a rectangular tube.
【0038】図8の装置は、金属多孔体製の平板フィル
タ材をつづら折れにし、その両側と外周を側板(図示せ
ず)及び端板7で塞いで作ったフィルタ6を用いてトラ
ッパ32を形成し、このトラッパ32をケース1内に2
個、直列に収納したものである。ここでは、下流側(図
中右側)トラッパのフィルタ部長さを上流側トラッパの
フィルタ部長さよりも短かくして各トラッパの圧損を平
均化しているが、この装置も、上流側トラッパと下流側
トラッパのフィルタ厚、捕集面積、或いはフィルタの目
孔径に差をつける方法で各トラッパの圧損を平均化する
ことができる。In the apparatus shown in FIG. 8, the trapper 32 is formed using a filter 6 formed by folding a flat filter material made of a porous metal body and closing both sides and the outer periphery thereof with side plates (not shown) and end plates 7. And the trapper 32 is
The pieces are stored in series. Here, the length of the filter portion of the downstream trapper (right side in the figure) is made shorter than the length of the filter portion of the upstream trapper to average the pressure loss of each trapper. However, this device also has the filter of the upstream trapper and the filter of the downstream trapper. The pressure loss of each trapper can be averaged by making a difference in the thickness, the collecting area, or the pore size of the filter.
【0039】なお、図2の装置は方向性がないが、図2
〜図8の装置はケース1の左側を排気路の上流側に配置
して使用する。Although the apparatus shown in FIG. 2 has no direction, FIG.
8 is used by disposing the left side of the case 1 on the upstream side of the exhaust path.
【0040】また、例示の装置は、各トラッパのフィル
タ材質として、耐熱性、耐腐食性に優れるNi−Cr−
Al合金、Ni−Cr合金などを用いたが、使用するフ
ィルタがAl2 O3 及びその複合成分で構成されるセラ
ミック材のファイバの集合体で作られている場合にも同
様の性能を得ることができる。Further, the illustrated apparatus uses Ni-Cr- as a filter material for each trapper, which is excellent in heat resistance and corrosion resistance.
Al alloy, Ni-Cr alloy, etc. are used, but the same performance is obtained even when the filter used is made of an aggregate of ceramic fibers composed of Al 2 O 3 and its composite component. Can be.
【0041】以下に、より詳細な実施例を挙げる。Hereinafter, more detailed examples will be described.
【0042】[0042]
【実施例】表1及び表2に示す仕様のA〜Gの排気ガス
浄化装置を試作した。EXAMPLE An exhaust gas purifying apparatus of A to G having the specifications shown in Tables 1 and 2 was prototyped.
【0043】[0043]
【表1】 [Table 1]
【0044】[0044]
【表2】 [Table 2]
【0045】図9は、図2の装置(表1の試料A)と同
じトラッパをケース1内に1個収納した従来構造の浄化
装置(これを比較例Hとする)である。また、図10
は、図9の装置のフィルタ厚を2倍にした装置(これを
比較例Iとする)である。FIG. 9 shows a purifying apparatus having a conventional structure in which one trapper same as the apparatus shown in FIG. 2 (sample A in Table 1) is housed in a case 1 (this is referred to as Comparative Example H). FIG.
Is a device in which the filter thickness of the device of FIG. 9 is doubled (this is referred to as Comparative Example I).
【0046】図11は、試作装置の中から表1のAを代
表として選び、これと比較例H、Iの捕集性能を調べて
比較したものである。このように、発明品Aは、捕集効
率が比較例Hに比べて向上している。なお、図10の比
較例Iは、表1の発明品Aとほぼ同等の捕集性能が得ら
れるが、僅かに発明品Aの方が優れている。一方、寸法
面では、比較例Iは最外層フィルタの外径が136mm
になって装置外径が大きくなる。FIG. 11 shows a comparison result obtained by selecting A in Table 1 as a representative from the prototypes and examining the trapping performance of Comparative Examples H and I. Thus, the invention product A has improved collection efficiency as compared with the comparative example H. It should be noted that the comparative example I of FIG. 10 has almost the same trapping performance as the inventive product A of Table 1, but the inventive product A is slightly better. On the other hand, in terms of dimensions, Comparative Example I has an outer diameter of the outermost layer filter of 136 mm.
And the outer diameter of the device becomes larger.
【0047】図12は、発明品Aと比較例Hの圧損特性
を比較した結果であり、発明品Aは比較例Hよりも圧損
特性に優れている。FIG. 12 shows the result of comparing the pressure loss characteristics of the invention product A and the comparative example H. The invention product A is superior to the comparative example H in the pressure loss characteristics.
【0048】[0048]
【発明の効果】以上説明したように、この発明の排気ガ
ス浄化装置は、捕集性能と圧損特性に優れる。また、そ
れ等の性能を犠牲にせずに装置外径を縮小でき、高さ方
向のスペースを大きく確保できない車両の床下にも設置
可能となる。従って、スペース上の制限が厳しく、ま
た、PM排出が問題となっているディーゼルエンジン搭
載車の排気ガス浄化装置として利用すると特に効果的で
ある。As described above, the exhaust gas purifying apparatus of the present invention has excellent trapping performance and pressure loss characteristics. Further, the outer diameter of the device can be reduced without sacrificing such performance, and the device can be installed under the floor of a vehicle where a large space in the height direction cannot be secured. Therefore, it is particularly effective when used as an exhaust gas purifying device for a vehicle equipped with a diesel engine, which has a severe space restriction and has a problem of PM emission.
【図1】トラッパのフィルタの厚さと充填率を変化させ
たときの圧損と捕集効率を比較した図FIG. 1 is a diagram comparing pressure loss and trapping efficiency when the thickness and filling rate of a trapper filter are changed.
【図2】この発明の排気ガス浄化装置の実施形態を簡略
化して示す断面図FIG. 2 is a simplified cross-sectional view showing an embodiment of an exhaust gas purifying apparatus of the present invention.
【図3】他の実施形態を簡略化して示す断面図FIG. 3 is a cross-sectional view schematically showing another embodiment.
【図4】他の実施形態を簡略化して示す断面図FIG. 4 is a simplified cross-sectional view showing another embodiment.
【図5】他の実施形態を簡略化して示す断面図FIG. 5 is a cross-sectional view schematically showing another embodiment.
【図6】他の実施形態を簡略化して示す断面図FIG. 6 is a simplified cross-sectional view showing another embodiment.
【図7】他の実施形態を簡略化して示す断面図FIG. 7 is a cross-sectional view showing another embodiment in a simplified manner.
【図8】他の実施形態を簡略化して示す断面図FIG. 8 is a simplified cross-sectional view showing another embodiment.
【図9】従来例を簡略化して示す断面図FIG. 9 is a simplified cross-sectional view showing a conventional example.
【図10】図9のものと比較してフィルタ厚を2倍にし
た装置の断面図FIG. 10 is a sectional view of an apparatus in which the filter thickness is doubled as compared with that of FIG.
【図11】図2、図9、図10の装置の捕集性能を比較
した図FIG. 11 is a diagram comparing the trapping performance of the devices of FIGS. 2, 9 and 10;
【図12】図2と図9の装置の圧損特性を比較した図FIG. 12 is a diagram comparing the pressure drop characteristics of the devices of FIGS. 2 and 9;
【符号の説明】 1 ケース 2、12、22、32 トラッパ 3、4、5 円筒状フィルタ 6 つづら折れのフィルタ 7 端板 8、9 流路 10 電気ヒータ[Description of Signs] 1 Case 2, 12, 22, 32 Trapper 3, 4, 5 Cylindrical filter 6 Filter with broken shape 7 End plate 8, 9 Flow path 10 Electric heater
Claims (5)
気ガス浄化装置であって、排気ガス中の微粒子を捕集す
るフィルタ部が、複数の筒状の3次元的に入り込んだ骨
格をもつフィルタ、もしくは3次元的に入り込んだ骨格
をもつ平板フィルタ材をつづら折れの状態に折り曲げた
フィルタで形成され、このフィルタ部を備えるトラッパ
をケース内に複数個直列配置にして設置したことを特徴
とする排気ガス浄化装置。1. An exhaust gas purifying device installed in the middle of an exhaust system of an engine, wherein a filter section for trapping fine particles in the exhaust gas has a plurality of cylindrical three-dimensionally skeletons. A filter or a filter formed by bending a flat filter material having a three-dimensionally inserted skeleton into a zigzag state, and a plurality of trappers having this filter portion are arranged in series in a case and installed. Exhaust gas purifying device.
ルタ部の捕集面積を大としてある請求項1記載の排気ガ
ス浄化装置。2. The exhaust gas purifying apparatus according to claim 1, wherein the trapping area on the upstream side of the exhaust path has a larger collecting area of the filter section.
ルタ部の軸方向長さを大としてある請求項1記載の排気
ガス浄化装置。3. The exhaust gas purifying apparatus according to claim 1, wherein the trapper located on the upstream side of the exhaust path has a longer axial length of the filter portion.
ルタ厚みを厚くしてある請求項1乃至3のいずれかに記
載の排気ガス浄化装置。4. The exhaust gas purifying apparatus according to claim 1, wherein the thickness of the filter is increased in the trapper on the downstream side of the exhaust passage.
ルタ部の目孔を小さくしてある請求項1乃至4のいずれ
かに記載の排気ガス浄化装置。5. The exhaust gas purifying device according to claim 1, wherein the trapper located on the downstream side of the exhaust path has a smaller hole in the filter section.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP8285292A JPH10131739A (en) | 1996-10-28 | 1996-10-28 | Emission control device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP8285292A JPH10131739A (en) | 1996-10-28 | 1996-10-28 | Emission control device |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH10131739A true JPH10131739A (en) | 1998-05-19 |
Family
ID=17689643
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP8285292A Pending JPH10131739A (en) | 1996-10-28 | 1996-10-28 | Emission control device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH10131739A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6829891B2 (en) | 2000-11-17 | 2004-12-14 | Toyota Jidosha Kabushiki Kaisha | Exhaust emission control device and method of controlling exhaust emission |
JP2010504466A (en) * | 2006-09-20 | 2010-02-12 | アリストトル ユニバーシティ テッサロニキ−リサーチ コミッティー | Gas processing equipment |
-
1996
- 1996-10-28 JP JP8285292A patent/JPH10131739A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6829891B2 (en) | 2000-11-17 | 2004-12-14 | Toyota Jidosha Kabushiki Kaisha | Exhaust emission control device and method of controlling exhaust emission |
JP2010504466A (en) * | 2006-09-20 | 2010-02-12 | アリストトル ユニバーシティ テッサロニキ−リサーチ コミッティー | Gas processing equipment |
JP2013151939A (en) * | 2006-09-20 | 2013-08-08 | Aristotle Univ Thessaloniki-Research Committee | Gas treatment device |
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