JPH068257Y2 - Particle collection and purification device - Google Patents

Particle collection and purification device

Info

Publication number
JPH068257Y2
JPH068257Y2 JP15927287U JP15927287U JPH068257Y2 JP H068257 Y2 JPH068257 Y2 JP H068257Y2 JP 15927287 U JP15927287 U JP 15927287U JP 15927287 U JP15927287 U JP 15927287U JP H068257 Y2 JPH068257 Y2 JP H068257Y2
Authority
JP
Japan
Prior art keywords
filter
exhaust gas
passage
purification device
particulate collection
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.)
Expired - Lifetime
Application number
JP15927287U
Other languages
Japanese (ja)
Other versions
JPH0163719U (en
Inventor
洋一郎 河野
浩司 荻田
信章 武田
保昭 熊谷
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Motors Corp
Original Assignee
Mitsubishi Motors 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
Application filed by Mitsubishi Motors Corp filed Critical Mitsubishi Motors Corp
Priority to JP15927287U priority Critical patent/JPH068257Y2/en
Priority to KR1019880008638A priority patent/KR930000473B1/en
Priority to DE3824578A priority patent/DE3824578A1/en
Priority to US07/221,091 priority patent/US4881959A/en
Publication of JPH0163719U publication Critical patent/JPH0163719U/ja
Application granted granted Critical
Publication of JPH068257Y2 publication Critical patent/JPH068257Y2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Description

【考案の詳細な説明】 (産業上の利用分野) 本考案はディーゼルエンジンの排気ガス通路に配設され
る微粒子捕集浄化装置に関する。
DETAILED DESCRIPTION OF THE INVENTION (Industrial field of application) The present invention relates to a particulate collection and purification device arranged in an exhaust gas passage of a diesel engine.

(従来の技術) ディーゼルエンジンからの排気ガス中には、炭素を主体
とする微粒子(パティキュレート)が含まれており、こ
のパティキュレートを捕集して浄化し、大気中に排出す
ることが必要である。かかるパティキュレートを捕集す
るために、従来、例えばセラミックス等の多孔質体より
なる微粒子捕集フィルタを具備した微粒子捕集浄化装置
をエンジンの排気ガス通路に配設している。
(Prior Art) Exhaust gas from a diesel engine contains fine particles (particulates) mainly composed of carbon, and these particulates need to be collected, purified, and discharged into the atmosphere. Is. In order to collect such particulates, conventionally, a particulate collection and purification device equipped with a particulate collection filter made of a porous material such as ceramics is arranged in the exhaust gas passage of the engine.

第3図はこのような微粒子捕集浄化装置をエンジンの排
気ガス通路に配設した状態を示し、微粒子捕集浄化装置
1は、金属製の容器11、この容器11内に収納された
微粒子捕集フィルタ12、及び、容器11内の前記フィ
ルタ12の上流側に配設された微粒子燃焼用ヒータ13
とから構成される。容器11は通常円筒状に形成され、
両端のフランジ部11a、11bにより、排気通路4の
途中に取り付けられている。微粒子捕集フィルタ12は
例えばセラミックス等の多孔質体よりなり、容器11よ
りも僅かに小径の円筒状に形成されており、このフィル
タ12外周面と容器11内周面との間には、例えばワイ
ヤメッシュ等の弾性支持部材14が介在されて、フィル
タ12を容器11内に弾性的に支持している。又、ヒー
タ13はバッテリ2に接続されている。
FIG. 3 shows a state in which such a fine particle collecting and purifying device is arranged in an exhaust gas passage of an engine. The fine particle collecting and purifying device 1 includes a metallic container 11 and a fine particle collecting and purifying device housed in the container 11. Collecting filter 12 and heater 13 for burning particulates arranged upstream of the filter 12 in the container 11.
Composed of and. The container 11 is usually formed in a cylindrical shape,
It is attached in the middle of the exhaust passage 4 by the flange portions 11a and 11b at both ends. The particulate collection filter 12 is made of, for example, a porous body such as ceramics and is formed in a cylindrical shape having a diameter slightly smaller than the container 11. Between the outer peripheral surface of the filter 12 and the inner peripheral surface of the container 11, for example, An elastic support member 14 such as a wire mesh is interposed to elastically support the filter 12 in the container 11. Further, the heater 13 is connected to the battery 2.

第4図は微粒子捕集フィルタ12の構成の一例を示した
ものであり、第4図(a)はその縦断面図、同図(b)はその
端面図である。この微粒子捕集フィルタ12はその軸方
向に沿って、上流側が閉塞された通路12aと下流側が
閉塞された通路12a′とが例えば碁盤目状に交互に多
数形成されており、各通路12aと12a′とは多孔質
の薄壁12bにより隔てられている(第4図(b))。従
って、第4図(a)に示すように、上流側が開口する通路1
2a′から流入した排気ガスは当該通路12a′を進む
が、この通路12a′の下流側は閉塞されているため、
排気ガスは多孔質薄壁12bを通過して隣接する通路1
2aに流れ込み、この際排気ガス中の微粒子の捕集が行
われて多孔質薄壁12bにパティキュレートが付着す
る。そして、パティキュレートの除去が行われた後、排
気ガスは下流側が開口する通路12aから排気通路4に
排出される。
FIG. 4 shows an example of the structure of the particulate collection filter 12, FIG. 4 (a) is a longitudinal sectional view thereof, and FIG. 4 (b) is an end view thereof. Along the axial direction of the particulate collection filter 12, a large number of passages 12a closed on the upstream side and a plurality of passages 12a 'closed on the downstream side are alternately formed in, for example, a grid pattern, and the passages 12a and 12a are formed. It is separated from ′ by a porous thin wall 12b (FIG. 4 (b)). Therefore, as shown in FIG. 4 (a), the passage 1 having an upstream opening
The exhaust gas flowing in from 2a 'proceeds through the passage 12a', but the downstream side of this passage 12a 'is blocked, so
Exhaust gas passes through the porous thin wall 12b and is adjacent to the passage 1
It flows into 2a, at which time particulates in the exhaust gas are collected and particulates adhere to the porous thin wall 12b. Then, after the particulates are removed, the exhaust gas is discharged to the exhaust passage 4 from the passage 12a which is open on the downstream side.

排気通路4には微粒子捕集浄化装置1をバイパスするバ
イパス通路5が形成されており、当該バイパス通路5の
上流側分岐点にはバイパスバルブ6が配設されている。
エンジン運転時には、このバイパスバルブ6を閉じて、
排気ガスを微粒子捕集浄化装置1に通過させて微粒子捕
集フィルタ12によりパティキュレートを捕集する。パテ
ィキュレートがフィルタ12の多孔質薄壁12bに所定
量以上付着したとき、即ち、フィルタ12の再生が必要と
なったときには、フィルタ12の通路12a、12a′内
を排気ガスが流れにくくなり、当該フィルタ12の上流
側と下流側との間の排気ガスの差圧が大きくなる。従っ
て、例えば圧力センサによりこの差圧を検出し、当該差
圧が所定値を超えた時に前記圧力センサからの信号によ
り作動する制御回路(図示せず)がバルブ7を開弁させ
てエアタンク8からアクチュエータ9にエアを供給し、
当該アクチュエータ9を作動させてバイパスバルブ6を
開弁させると共にヒータ13に通電して加熱させる。バ
イパスバルブ6が開弁すると排気通路4を流れる排気ガ
スの大部分がバイパス通路5を流れ、残量の排気ガスが
ヒータ13により加熱されて高温ガスとなり微粒子捕集
浄化装置1のフィルタ20内を流れる。この高温ガスに
より前記パティキュレートを着火燃焼させてフィルタ1
2の再生を行う。
A bypass passage 5 that bypasses the particulate collection and purification device 1 is formed in the exhaust passage 4, and a bypass valve 6 is provided at an upstream branch point of the bypass passage 5.
When the engine is running, close this bypass valve 6,
The exhaust gas is passed through the particulate collection / purification device 1 and particulates are collected by the particulate collection filter 12. When the particulate adheres to the porous thin wall 12b of the filter 12 by a predetermined amount or more, that is, when the filter 12 needs to be regenerated, the exhaust gas becomes difficult to flow in the passages 12a and 12a 'of the filter 12, The differential pressure of the exhaust gas between the upstream side and the downstream side of the filter 12 becomes large. Therefore, for example, a pressure sensor detects this differential pressure, and when the differential pressure exceeds a predetermined value, a control circuit (not shown) that operates by a signal from the pressure sensor opens the valve 7 to open the air tank 8 from the air tank 8. Air is supplied to the actuator 9,
The actuator 9 is operated to open the bypass valve 6 and energize the heater 13 to heat it. When the bypass valve 6 is opened, most of the exhaust gas flowing through the exhaust passage 4 flows through the bypass passage 5, and the remaining exhaust gas is heated by the heater 13 to become a high temperature gas. Flowing. The high-temperature gas ignites and burns the particulates to filter 1
Play back 2.

(考案が解決しようとする問題点) このフィルタ12の再生時には、微粒子捕集浄化装置1
にも排気ガスが供給されるが、ヒータ13の限られた電力
で高温ガスを発生させなければならないので、微粒子捕
集浄化装置1に流入するガス量は上述したように僅少量
に設定される。しかしながら、上記したパティキュレー
トの燃焼時にはヒータ13で加熱され高温となったガス
は輻射熱として外部に放散されたり、或いは、自然対流
により上昇して容器11の上部を流れそのままフィルタ
12の上部通路を通過する。従って、僅かな量の高温ガ
スが有効に利用されないので、フィルタ12の通路が均
一に加熱されず、特に、下部の通路に捕集されたパティ
キュレートの燃焼が充分に行われず、しかも、フィルタ
12自体にも温度勾配に起因する熱応力が発生するという
問題がある。
(Problems to be Solved by the Invention) When the filter 12 is regenerated, the particulate collection and purification device 1
Although the exhaust gas is also supplied to this, since the high-temperature gas must be generated with the limited electric power of the heater 13, the amount of gas flowing into the particulate collection and purification device 1 is set to a very small amount as described above. . However, when the above particulates are burned, the gas heated by the heater 13 and having a high temperature is dissipated to the outside as radiant heat, or rises by natural convection to flow in the upper part of the container 11 and pass through the upper passage of the filter 12 as it is. To do. Therefore, since a small amount of high temperature gas is not effectively used, the passage of the filter 12 is not uniformly heated, and in particular, the particulate matter trapped in the lower passage is not sufficiently burned, and the filter is not
12 itself has a problem that thermal stress is generated due to the temperature gradient.

本考案は上記従来の問題点に鑑みてなされたもので、パ
ティキュレート燃焼時に燃焼手段により高温となったガ
スがフィルタ入口において略均一な温度分布をなし、且
つ当該フィルタの各通路の通過量を均一にして、フィル
タに熱応力が発生することを防止した微粒子捕集浄化装
置を提供することを目的とする。
The present invention has been made in view of the above-mentioned conventional problems, in which the gas heated by the combustion means during particulate combustion has a substantially uniform temperature distribution at the filter inlet, and the amount of passage through each passage of the filter is It is an object of the present invention to provide a particulate collection and purification device which is made uniform and prevents the generation of thermal stress in the filter.

(問題点を解決するための手段) 上記目的を達成するために本考案によれば、排気通路に
配設された円筒状容器と、該容器内に収納されると共に
排気ガスが通過する多数の通路を有し当該排気ガス中の
微粒子を捕集する微粒子捕集フィルタと、該フィルタの
上流に配設され当該フィルタに捕集された微粒子を燃焼
させるために前記排気ガスの温度を上昇させる着火・燃
焼手段とを備えた微粒子捕集浄化装置において、前記容
器内且つ前記着火・燃焼手段の上流側に、多数の排気ガ
ス通路が形成され、且つ下部の空隙率が上部の空隙率よ
りも大きく設定された伝熱変換素子を配設した構成とし
たものである。
(Means for Solving the Problems) According to the present invention in order to achieve the above-mentioned object, according to the present invention, a cylindrical container disposed in an exhaust passage and a large number of exhaust gas passing through the cylindrical container are provided. A particulate collection filter having a passageway for collecting particulates in the exhaust gas, and an ignition for increasing the temperature of the exhaust gas for burning the particulates collected in the filter, which is arranged upstream of the filter. In the particulate collection and purification device provided with a combustion means, a large number of exhaust gas passages are formed in the container and on the upstream side of the ignition / combustion means, and the porosity of the lower part is larger than that of the upper part. The heat transfer conversion element thus set is arranged.

(作用) 着火・燃焼手段の上流側に配設された伝熱変換素子は、
当該着火・燃焼手段により加熱され高温となった排気ガ
スの熱が輻射熱の影響で外部に放散されることを防止す
ると共に、下流にある着火・燃焼手段へ供給する排気ガ
ス量を排気通路の下部ほど多くする。着火・燃焼手段を
通過して高温となったガスは下流に配設されたフィルタ
入口まで移動する間に、自然対流によって排気通路内を
次第に上昇し、当該フィルタの入口近傍では略均一な温
度分布且つ均一なガス通過量となる。その結果、フィル
タの均一な加熱が行われ、パティキュレートの燃焼が略
均一になされると共に、フィルタの下部から上部にかけ
ての温度勾配に起因する熱応力の発生が防止される。
(Operation) The heat transfer conversion element arranged on the upstream side of the ignition / combustion means
The heat of the exhaust gas heated to a high temperature by the ignition / combustion means is prevented from being dissipated to the outside due to the effect of radiant heat, and the amount of exhaust gas supplied to the ignition / combustion means in the downstream is controlled at the lower part of the exhaust passage. Do more. The gas that has passed through the ignition / combustion means and has reached a high temperature gradually rises in the exhaust passage by natural convection while moving to the inlet of the filter arranged downstream, and the temperature distribution near the inlet of the filter is almost uniform. In addition, the amount of passing gas is uniform. As a result, the filter is uniformly heated, the particulates are burned substantially uniformly, and the generation of thermal stress due to the temperature gradient from the lower part to the upper part of the filter is prevented.

(実施例) 以下、本考案の一実施例を添付図面に基づいて詳述す
る。尚、図において第3図と同一の構成素には同一の符
号を付して示してある。
Embodiment An embodiment of the present invention will be described below in detail with reference to the accompanying drawings. In the figure, the same constituents as those in FIG. 3 are designated by the same reference numerals.

第1図は本考案の微粒子捕集浄化装置を示し、微粒子捕
集浄化装置1′において、微粒子捕集フィルタ12の上
流側に配設されたヒータ13の更に上流側に伝熱変換素
子15が配設されている。伝熱変換素子15は、例え
ば、空隙率の大きなセラミック多孔体から構成される。
セラミックとしては、特に限定されるものではないが、
耐熱性、耐薬品性及び耐熱衝撃性等に優れていることが
要求されるため、例えばコージェライト等が使用され
る。
FIG. 1 shows a particle collecting and purifying device of the present invention. In a particle collecting and purifying device 1 ′, a heat transfer conversion element 15 is provided further upstream of a heater 13 arranged upstream of the particle collecting filter 12. It is arranged. The heat transfer conversion element 15 is made of, for example, a ceramic porous body having a large porosity.
The ceramic is not particularly limited,
For example, cordierite is used because it is required to have excellent heat resistance, chemical resistance, and thermal shock resistance.

第2図は伝熱変換素子の構成を示し、伝熱変換素子15
はメッシュの大きさが相互に異なる2個の半円形のセラ
ミック多孔体15a及び15bを上下に組み合わせて一
体化されてなるものである。この伝熱変換素子15にお
いて、下部多孔体15bの空隙率(メッシュ)は上部多孔
体15aの空隙率(メッシュ)よりも大きく設定されて
おり、当該伝熱変換素子15の空気通過量は上部よりも
下部の方が多くなるようになされている。従って、この
伝熱変換素子15に流入した排気ガスは矢印で示すよう
に、下部の通過量が上部の通過量に比べて多くなる。
FIG. 2 shows the structure of the heat transfer conversion element, and the heat transfer conversion element 15
Is a structure in which two semicircular ceramic porous bodies 15a and 15b having different mesh sizes are vertically combined and integrated. In this heat transfer conversion element 15, the porosity (mesh) of the lower porous body 15b is set to be larger than the porosity (mesh) of the upper porous body 15a, and the air passage amount of the heat transfer conversion element 15 is higher than that of the upper part. Also, the lower part has more. Therefore, as shown by the arrow, the amount of exhaust gas flowing into the heat transfer conversion element 15 is larger in the lower passage amount than in the upper passage amount.

以下に作用を説明する。The operation will be described below.

微粒子捕集浄化装置1′は、第3図に示す従来の微粒子
捕集浄化装置1と同様に2点鎖線で示すエンジンの排気
通路4の途中に配設される。微粒子捕集フィルタ12の
再生時には、前述したようにバイパスバルブが開かれ
て、排気ガスの大部分はバイパス通路を通って流れ、微
粒子捕集浄化装置1′にはごく僅かの排気ガスが流れ込
む。微粒子捕集浄化装置1′に流入した矢印Aで示す排
気ガスは先ず伝熱変換素子15を通過する。この伝熱変
換素子15は矢印Cで示す上部を通過する排気ガス量に
比べて矢印Bで示す下部を通過する排気ガス量の方が多
くなるようにされているので、当該伝熱変換素子15の
下流に配設されたヒータ13により加熱される排気ガス
量は上部より下部の方が多くなっている。
The particulate collection and purification device 1'is arranged in the middle of the exhaust passage 4 of the engine shown by the chain double-dashed line, like the conventional particulate collection and purification device 1 shown in FIG. During regeneration of the particulate collection filter 12, the bypass valve is opened as described above, most of the exhaust gas flows through the bypass passage, and a very small amount of exhaust gas flows into the particulate collection and purification device 1 '. The exhaust gas indicated by arrow A that has flowed into the particulate collection and purification device 1 ′ first passes through the heat transfer conversion element 15. Since the heat transfer conversion element 15 is designed so that the amount of exhaust gas passing through the lower portion indicated by the arrow C is larger than the amount of exhaust gas passing through the upper portion indicated by the arrow C, the heat transfer conversion element 15 is concerned. The amount of exhaust gas heated by the heater 13 disposed on the downstream side is higher in the lower portion than in the upper portion.

排気ガスはこの伝熱変換素子15を通過した後、ヒータ
13により加熱されて高温ガスとされ、当該高温ガスは
フィルタ12の上流側端面に到達するまでの間に、自然
対流により上昇する。上記したように、ヒータ13通過
後の高温ガス量は下部の方が多くなっているため、その
一部が矢印Dで示すように上昇することによりフィルタ
12に流入する高温ガス量は当該フィルタ12の入口側
の全面において略均一となる。従って、フィルタ12の各
通路12a、12a′(第4図)には略均一な温度の高
温ガスが略均一な通過量で通過することとなり、この結
果、当該フィルタ12に捕集されているパティキュレー
トの燃焼が均一に効率良く行われると共に、フィルタ1
2に熱応力が発生することが防止される。
After passing through the heat transfer conversion element 15, the exhaust gas is heated by the heater 13 to be a high temperature gas, and the high temperature gas rises by natural convection until it reaches the upstream end surface of the filter 12. As described above, the amount of high-temperature gas after passing through the heater 13 is larger in the lower part, so that the amount of high-temperature gas that flows into the filter 12 when part of it rises as indicated by arrow D is Is substantially uniform over the entire inlet side. Therefore, the high temperature gas having a substantially uniform temperature passes through the passages 12a, 12a '(FIG. 4) of the filter 12 in a substantially uniform passage amount, and as a result, the particulates collected in the filter 12 are collected. The burning of the curate is performed uniformly and efficiently, and the filter 1
The generation of thermal stress in 2 is prevented.

尚、上記実施例においては、伝熱変換素子として上下に
2分割されたセラミック多孔体を使用した場合について
記述したが、かかる2分割体に限るものではなく、下部
へいく程ガス通過量が増大するような構成のものであれ
ばよい。
In the above embodiment, the case where the ceramic porous body which is divided into the upper and lower parts is used as the heat transfer conversion element has been described, but the present invention is not limited to such a divided body, and the gas passage amount increases toward the lower part. Any configuration may be used.

(考案の効果) 以上説明したように本考案によれば、排気通路に配設さ
れた円筒状容器と、該容器内に収納されると共に排気ガ
スが通過する多数の通路を有し当該排気ガス中の微粒子
を捕集する微粒子捕集フィルタと、該フィルタの上流に
配設され当該フィルタに捕集された微粒子を燃焼させる
ために前記排気ガスの温度を上昇させる着火・燃焼手段
とを備えた微粒子捕集浄化装置において、前記容器内且
つ前記着火・燃焼手段の上流側に、多数の排気ガス通路
が形成され、且つ下部の空隙率が上部の空隙率よりも大
きく設定された伝熱変換素子を配設したので、微粒子捕
集フィルタの再生時に、当該フィルタに流入する高温と
なった排気ガスの温度分布及びガス通過量が略均一とな
り、フィルタに捕集された微粒子の燃焼が均一に効率良
く行われると共に、当該フィルタに温度勾配に起因する
熱応力の発生が防止されるという効果を奏する。
(Effect of the Invention) As described above, according to the present invention, the exhaust gas has a cylindrical container arranged in the exhaust passage and a large number of passages through which the exhaust gas passes while being housed in the container. A fine particle collection filter for collecting fine particles therein, and an ignition / combustion means arranged upstream of the filter for raising the temperature of the exhaust gas for burning the fine particles collected by the filter are provided. In the particulate collection and purification device, a large number of exhaust gas passages are formed in the container and on the upstream side of the ignition / combustion means, and the lower void ratio is set higher than the upper void ratio. As a result, the temperature distribution and the gas passage amount of the hot exhaust gas flowing into the filter become substantially uniform during the regeneration of the particulate collection filter, and the combustion of the particulates collected by the filter becomes uniform. well As well as being performed, it is possible to prevent the generation of thermal stress due to the temperature gradient in the filter.

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

第1図は本考案の微粒子捕集浄化装置の一実施例を示す
断面図、第2図は第1図の伝熱変換素子の斜視図、第3
図は従来の微粒子捕集浄化装置をエンジンの排気通路に
配設した状態を示す構成図、第4図(a)は第3図の微粒
子捕集浄化装置の微粒子捕集フィルタの断面図、第4図
(b)は第4図(a)の端面図である。 1′…微粒子捕集浄化装置、4…排気通路、12…微粒子
捕集フィルタ、13…ヒータ、15…伝熱変換素子、15a、15
b…セラミック多孔体。
FIG. 1 is a sectional view showing an embodiment of the particulate collection and purification device of the present invention, FIG. 2 is a perspective view of the heat transfer conversion element of FIG. 1, and FIG.
FIG. 4 is a configuration diagram showing a state in which a conventional particulate collection and purification device is installed in an exhaust passage of an engine. FIG. 4 (a) is a sectional view of a particulate collection filter of the particulate collection and purification device in FIG. Figure 4
(b) is an end view of FIG. 4 (a). 1 '... Fine particle collection and purification device, 4 ... Exhaust passage, 12 ... Fine particle collection filter, 13 ... Heater, 15 ... Heat transfer conversion element, 15a, 15
b ... Ceramic porous body.

───────────────────────────────────────────────────── フロントページの続き (72)考案者 熊谷 保昭 東京都港区芝5丁目33番8号 三菱自動車 工業株式会社内 (56)参考文献 特開 昭59−520(JP,A) 実開 昭63−130611(JP,U) 実公 昭63−11293(JP,Y2) 実公 平1−15854(JP,Y2) ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Creator Yasuaki Kumagai 5-3-8 Shiba, Minato-ku, Tokyo Mitsubishi Motors Corporation (56) References JP-A-59-520 (JP, A) 63-130611 (JP, U) Actual public Sho 63-11293 (JP, Y2) Actual public 1-15854 (JP, Y2)

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 【請求項1】排気通路に配設された円筒状容器と、該容
器内に収納されると共に排気ガスが通過する多数の通路
を有し当該排気ガス中の微粒子を捕集する微粒子捕集フ
ィルタと、該フィルタの上流に配設され当該フィルタに
捕集された微粒子を燃焼させるために前記排気ガスの温
度を上昇させる着火・燃焼手段とを備えた微粒子捕集浄
化装置において、前記容器内且つ前記着火・燃焼手段の
上流側に、多数の排気ガス通路が形成され、且つ下部の
空隙率が上部の空隙率よりも大きく設定された伝熱変換
素子を配設したことを特徴とする微粒子捕集浄化装置。
1. A particulate collection filter having a cylindrical container arranged in an exhaust passage, and a large number of passages accommodated in the container and through which exhaust gas passes, for collecting fine particles in the exhaust gas. And a ignition / combustion unit arranged upstream of the filter for raising the temperature of the exhaust gas in order to burn the particles collected by the filter, in the container, A plurality of exhaust gas passages are formed on the upstream side of the ignition / combustion means, and a heat transfer conversion element having a lower void ratio set to be higher than the upper void ratio is arranged. Collective purifier.
JP15927287U 1987-07-20 1987-10-20 Particle collection and purification device Expired - Lifetime JPH068257Y2 (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
JP15927287U JPH068257Y2 (en) 1987-10-20 1987-10-20 Particle collection and purification device
KR1019880008638A KR930000473B1 (en) 1987-07-20 1988-07-12 Exhaust emission purifier for diesel engines
DE3824578A DE3824578A1 (en) 1987-07-20 1988-07-19 DEVICE FOR CLEANING THE EXHAUST EMISSION OF DIESEL ENGINES
US07/221,091 US4881959A (en) 1987-07-20 1988-07-19 Exhaust emission purifier for diesel engines

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15927287U JPH068257Y2 (en) 1987-10-20 1987-10-20 Particle collection and purification device

Publications (2)

Publication Number Publication Date
JPH0163719U JPH0163719U (en) 1989-04-24
JPH068257Y2 true JPH068257Y2 (en) 1994-03-02

Family

ID=31440338

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15927287U Expired - Lifetime JPH068257Y2 (en) 1987-07-20 1987-10-20 Particle collection and purification device

Country Status (1)

Country Link
JP (1) JPH068257Y2 (en)

Also Published As

Publication number Publication date
JPH0163719U (en) 1989-04-24

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