JPH07293223A - Exhaust emission control device for diesel engine - Google Patents

Exhaust emission control device for diesel engine

Info

Publication number
JPH07293223A
JPH07293223A JP6114132A JP11413294A JPH07293223A JP H07293223 A JPH07293223 A JP H07293223A JP 6114132 A JP6114132 A JP 6114132A JP 11413294 A JP11413294 A JP 11413294A JP H07293223 A JPH07293223 A JP H07293223A
Authority
JP
Japan
Prior art keywords
exhaust
particulate filter
diesel engine
main
fine particle
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
Application number
JP6114132A
Other languages
Japanese (ja)
Inventor
Hideo Kawamura
英男 河村
Shogo Suzuki
省伍 鈴木
Toshiaki Sakaguchi
敏章 坂口
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.)
Isuzu Ceramics Research Institute Co Ltd
Original Assignee
Isuzu Ceramics Research Institute Co Ltd
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 Isuzu Ceramics Research Institute Co Ltd filed Critical Isuzu Ceramics Research Institute Co Ltd
Priority to JP6114132A priority Critical patent/JPH07293223A/en
Publication of JPH07293223A publication Critical patent/JPH07293223A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02BINTERNAL-COMBUSTION PISTON ENGINES; COMBUSTION ENGINES IN GENERAL
    • F02B3/00Engines characterised by air compression and subsequent fuel addition
    • F02B3/06Engines characterised by air compression and subsequent fuel addition with compression ignition

Landscapes

  • Processes For Solid Components From Exhaust (AREA)
  • Filtering Of Dispersed Particles In Gases (AREA)

Abstract

PURPOSE:To efficiently collect exhausted fine particles by means of two kinds exhausted fine particle filters according to the amount of exhaustion so as not to damage the exhausted fine particle filters. CONSTITUTION:The exhaust passage of a diesel engine is divided into main and sub exhaust routes A and B, a route switching valve 16 whose opening and closing are controlled according to the amount of exhaust gas is provided in the vicinity of a branching part, a felt-like main exhaust fine particle filter 22 made of inorganic fiber whose pore diameter is small and having a electrification heating wire netting on both surfaces is provided in the main exhaust route A and a sub exhaust fine particle filter 16 whose pore diameter is larger than that of the main exhaust fine particle filter 22 is provided on the sub- exhaust route B.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は排気流量に対応して2種
の排気微粒子フイルタを用い、排気微粒子を効率的に捕
集するようにした、デイーゼル機関の排気浄化装置に関
するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an exhaust gas purifying apparatus for a diesel engine, which uses two kinds of exhaust particle filters corresponding to exhaust gas flow rates to efficiently collect exhaust particles.

【0002】[0002]

【従来の技術】デイーゼル機関の排気中のパテイキユレ
ートと称する黒鉛などの排気微粒子を捕集する排気微粒
子フイルタとして、コーデイエライト・セラミツクスや
炭化珪素からなる多孔質ハニカム体を用いたもの、セラ
ミツクスからなる泡状気孔体を用いたもの、無機質繊維
からなる織布を用いたものなどが知られている。
2. Description of the Related Art As an exhaust particulate filter for collecting particulates such as graphite called particulates in the exhaust of a diesel engine, a cordierite ceramic or a porous honeycomb body made of silicon carbide is used. Known are ones that use foam-like pores, ones that use a woven fabric made of inorganic fibers, and the like.

【0003】セラミツクスからなる排気微粒子フイルタ
の再生方法としては、表面に捕集された排気微粒子を、
バーナの火炎で着火燃焼させるもの、燃焼伝播を利用す
るもの、電熱により着火燃焼させるものなどがある。ま
た、排気微粒子フイルタに排気流と逆方向に空気を流
し、排気微粒子フイルタの表面に捕集された排気微粒子
を落してから燃焼させるものがある。
As a method of regenerating the exhaust particulate filter made of ceramics, the exhaust particulates collected on the surface are
There are those that ignite and burn with the flame of a burner, those that utilize combustion propagation, and those that ignite and burn with electric heat. Further, there is one in which air is caused to flow in the exhaust particulate filter in the direction opposite to the exhaust flow, and the exhaust particulates collected on the surface of the exhaust particulate filter are dropped and then burned.

【0004】上述のセラミツクスからなる排気微粒子フ
イルタは、排気微粒子を捕集する表面の気孔径が排気微
粒子よりも小さいので、デイーゼル機関の排気流量に対
応したかなり広い表面積を必要とする。また、上述の排
気微粒子フイルタでは、排気微粒子フイルタの表面に排
気微粒子が捕集されると、排気微粒子フイルタの気孔径
はますます小さくなり、排気微粒子が排気微粒子フイル
タの表面に堆積し、排気微粒子フイルタの流体抵抗によ
る圧力損失が急激に大きくなる。
The exhaust particulate filter made of the above-mentioned ceramic requires a considerably large surface area corresponding to the exhaust gas flow rate of the diesel engine since the pore diameter of the surface for collecting the exhaust particulate is smaller than that of the exhaust particulate. Further, in the above exhaust particulate filter, when the exhaust particulates are collected on the surface of the exhaust particulate filter, the pore size of the exhaust particulate filter becomes smaller and smaller, and the exhaust particulates are accumulated on the surface of the exhaust particulate filter, and the exhaust particulates The pressure loss due to the fluid resistance of the filter suddenly increases.

【0005】さらに、燃焼による排気微粒子フイルタの
再生時、排気微粒子が異常に堆積した部分では、燃焼温
度が1400℃にもなり、排気微粒子フイルタが破損し
たり、溶損することがある。燃焼温度が1400℃以下
でも、燃焼伝播が均一に行われず、熱応力により排気微
粒子フイルタに亀裂が生じることがある。従来の無機質
繊維からなる排気微粒子フイルタも、表面だけで排気微
粒子を捕集するので、広い表面積のものが必要になる。
Further, when the exhaust particulate filter is regenerated by combustion, the combustion temperature may reach 1400 ° C. in the portion where the exhaust particulate is abnormally accumulated, and the exhaust particulate filter may be damaged or melted. Even if the combustion temperature is 1400 ° C. or lower, the combustion is not uniformly propagated, and cracks may occur in the exhaust particulate filter due to thermal stress. A conventional exhaust particle filter made of inorganic fibers also has a large surface area because it collects exhaust particles only on the surface.

【0006】[0006]

【発明が解決しようとする課題】本発明の目的は上述の
問題に鑑み、排気微粒子フイルタが破損しないように、
排気流量に対応して2種の排気微粒子フイルタにより排
気微粒子を効率的に捕集するようにした、デイーゼル機
関の排気浄化装置を提供することにある。
SUMMARY OF THE INVENTION In view of the above problems, it is an object of the present invention to prevent the exhaust particulate filter from being damaged.
An object of the present invention is to provide an exhaust emission control device for a diesel engine in which exhaust particulates are efficiently collected by two types of exhaust particulate filters corresponding to the exhaust flow rate.

【0007】[0007]

【課題を解決するための手段】上記目的を達成するため
に、本発明の構成はデイーゼル機関の排気流路を主排気
流路と副排気流路とに分岐し、該分岐部付近に排気流量
に対応して開閉制御される流路切換弁を設け、主排気流
路には両面に通電加熱用金網を有する気孔径の小さな無
機質繊維からなるフエルト状の主排気微粒子フイルタを
配設し、副排気流路には主排気微粒子フイルタよりも気
孔径の大きな副排気微粒子フイルタを配設したものであ
る。
In order to achieve the above object, the structure of the present invention divides the exhaust passage of a diesel engine into a main exhaust passage and a sub-exhaust passage, and an exhaust flow rate near the branch portion. Is equipped with a flow path switching valve that is controlled to open and close, and a main exhaust fine particle filter in the form of a felt made of inorganic fibers with a small pore size that has a wire mesh for electric heating on both sides is installed in the main exhaust flow path. An auxiliary exhaust particulate filter having a larger pore size than the main exhaust particulate filter is arranged in the exhaust passage.

【0008】[0008]

【作用】機関の排気流量が少ない時は、排気を気孔径が
小さい無機質繊維のフエルト状体からなる主排気微粒子
フイルタへ通して効率的に排気微粒子を捕集し、排気流
量が多い時は、気孔径が大きい金属多孔質体からなる副
排気微粒子フイルタへ通して排気微粒子を捕集し、圧力
損失を小さくする。
[Function] When the exhaust gas flow rate of the engine is low, the exhaust gas is efficiently collected by passing the exhaust gas through the main exhaust particle filter consisting of a felt-like body of inorganic fibers having a small pore diameter, and when the exhaust gas flow rate is high, The exhaust particulates are collected by passing through an auxiliary exhaust particulate filter made of a metal porous body having a large pore diameter, and the pressure loss is reduced.

【0009】無機質繊維の間に最適な気孔径を有するフ
エルト状体は、表面だけでなく、表面よりも内側の部分
でも、排気微粒子を効率的に捕集する。
The felt-like material having the optimum pore size between the inorganic fibers efficiently collects exhaust particulates not only on the surface but also on the inside of the surface.

【0010】フエルト状体の両面に重ね合された耐熱性
の金網は、金網へ通電することにより、捕集された排気
微粒子を燃焼させる。
The heat-resistant wire nets laminated on both sides of the felt-like body burn the collected exhaust fine particles by energizing the wire nets.

【0011】[0011]

【実施例】図1は本発明によるデイーゼル機関の排気浄
化装置の概略構成を示す側面図、図2は同排気浄化装置
の側面断面図である。図2に示すように、排気浄化装置
は筒形の容器5の内周面に断熱材6を張り付け、容器5
の内部に隔壁筒23を同心に配置して、容器5と隔壁筒
23の間に主排気通路Aを、隔壁筒23の内部に副排気
流路Bをそれぞれ区画される。
DESCRIPTION OF THE PREFERRED EMBODIMENTS FIG. 1 is a side view showing a schematic structure of an exhaust gas purification apparatus for a diesel engine according to the present invention, and FIG. 2 is a side sectional view of the same exhaust gas purification apparatus. As shown in FIG. 2, in the exhaust gas purification device, a heat insulating material 6 is attached to the inner peripheral surface of a cylindrical container 5,
A partition cylinder 23 is concentrically arranged inside the partition wall, a main exhaust passage A is defined between the container 5 and the partition cylinder 23, and a sub exhaust passage B is defined inside the partition cylinder 23.

【0012】容器5と隔壁筒23の間の環状の主排気通
路Aに、両面に通電加熱用金網を備えた気孔径の小さな
無機質繊維のフイルタ状体からなる二重筒形の主排気微
粒子フイルタ22が配設される。しかし、主排気微粒子
フイルタ22は複数の細長いカツプ状のものを、容器5
と隔壁筒23の間の環状空間に周方向等間隔に配設して
もよい。右端壁25が閉鎖される二重筒形の主排気微粒
子フイルタ22は、排気入口側の表面にFe-Cr-Al-Y合金
などの通電加熱用金網を、排気出口側の表面に触媒作用
をする白金などの金網をそれぞれ重合せ結合される。主
排気微粒子フイルタ22は左端を環状板21に支持さ
れ、環状板21は主排気微粒子フイルタ22の左端入口
24に連通する多数の開口を周方向等間隔に設けられ
る。
A double-cylinder-shaped main exhaust particulate filter made of a filter-like body of inorganic fiber having a small pore size and provided with a wire mesh for electric heating on both sides in an annular main exhaust passage A between the container 5 and the partition tube 23. 22 is provided. However, the main exhaust particulate filter 22 is composed of a plurality of elongated cup-shaped ones.
You may arrange | position in the annular space between the partition tube 23 at equal intervals in the circumferential direction. The main exhaust fine particle filter 22 having a double cylindrical shape with the right end wall 25 closed is provided with a wire mesh for electrically heating Fe-Cr-Al-Y alloy or the like on the surface on the exhaust inlet side and a catalytic action on the surface on the exhaust outlet side. Wire meshes such as platinum are polymerized and bonded. The left end of the main exhaust particulate filter 22 is supported by the annular plate 21, and the annular plate 21 is provided with a large number of openings communicating with the left end inlet 24 of the main exhaust particulate filter 22 at equal intervals in the circumferential direction.

【0013】隔壁筒23の内部の副排気流路Bに、主排
気微粒子フイルタ22よりも気孔径の大きな無機質繊維
のフイルタ状体または表面にアルミニウム、アルミナ、
コーデイライトなどをコーテイングした金属多孔質体
(メタルホーム)からなる筒形の副排気微粒子フイルタ
16が配設される。筒形の副排気微粒子フイルタ16
も、内周面にFe-Cr-Al-Y合金などの通電加熱用金網を、
外周面に触媒作用をする白金などの金網をそれぞれ重合
せ結合される。副排気微粒子フイルタ16と隔壁筒23
も、容器5の入口端部(左端部)に配した環状板21に
支持される。
In the sub-exhaust passage B inside the partition tube 23, a filter-like body of inorganic fibers having a pore size larger than that of the main exhaust fine particle filter 22 or aluminum, alumina on the surface thereof,
A cylindrical auxiliary exhaust particulate filter 16 made of a metal porous body coated with cordierite or the like is provided. Cylindrical auxiliary exhaust particulate filter 16
Also, wire mesh for electric heating such as Fe-Cr-Al-Y alloy on the inner peripheral surface,
Wire meshes such as platinum that act as a catalyst are polymerized and bonded to the outer peripheral surface. Secondary exhaust particulate filter 16 and partition tube 23
Is also supported by the annular plate 21 arranged at the inlet end (left end) of the container 5.

【0014】主排気流路Aと副排気流路Bとの分岐部付
近に、排気流量に対応して開閉制御される流路切換弁1
4が配設される。このため、副排気微粒子フイルタ16
の左端に筒12が結合され、筒12の内部に支軸15に
より蝶形の流路切換弁14が回動可能に支持される。支
軸15は容器5の外部へ突出され、かつレバー51を結
合される。図1に示すように、レバー51は電磁アクチ
ユエータ53のプランジヤ52と連結される。副排気微
粒子フイルタ16の右端部に筒17が結合され、筒17
の端部を開閉する円板からなる逃し弁19が、ばね18
の力により引張られて筒17の端部へ当接される。
A flow passage switching valve 1 which is controlled to open and close in the vicinity of a branch portion between the main exhaust flow passage A and the sub exhaust flow passage B in accordance with the exhaust flow rate.
4 are provided. Therefore, the auxiliary exhaust particulate filter 16
A tube 12 is coupled to the left end of the, and a butterfly-shaped flow path switching valve 14 is rotatably supported inside the tube 12 by a support shaft 15. The support shaft 15 is projected to the outside of the container 5 and is connected with the lever 51. As shown in FIG. 1, the lever 51 is connected to the plunger 52 of the electromagnetic actuator 53. The cylinder 17 is connected to the right end portion of the auxiliary exhaust particulate filter 16,
The relief valve 19 made of a disc that opens and closes the end of the
Is pulled and brought into contact with the end of the cylinder 17.

【0015】容器5の左端は円錐筒3を介して入口筒2
に接続され、入口筒2はフランジ2aを排気管の上流側
端部に結合される。容器5の右端は円錐筒7を介して出
口筒8に結合され、出口筒8はフランジ8aを排気マフ
ラに連通する排気管の下流側端部に接続される。
The left end of the container 5 is connected to the inlet cylinder 2 via the conical cylinder 3.
The inlet tube 2 has a flange 2a joined to the upstream end of the exhaust pipe. The right end of the container 5 is connected to the outlet cylinder 8 via the conical cylinder 7, and the outlet cylinder 8 is connected to the downstream end of the exhaust pipe that communicates the flange 8a with the exhaust muffler.

【0016】円錐筒3は絶縁物を介して電極41,4
2,43を支持され、同様に円錐筒7は電極44を支持
される。電極43,41は主排気微粒子フイルタ22の
内面に重ね合せた金網に通電し、電極42,44は副排
気微粒子フイルタ16の内面に重ね合せた金網に通電
し、各排気微粒子フイルタ16,22で捕集された排気
微粒子を燃焼させて排気微粒子フイルタ16,22を再
生する。
The conical cylinder 3 has electrodes 41, 4 via an insulator.
2 and 43 are supported, and similarly the conical cylinder 7 is supported by the electrode 44. The electrodes 43 and 41 are energized to the metal nets superposed on the inner surface of the main exhaust particulate filter 22, and the electrodes 42 and 44 are energized to the metal nets superposed on the inner surface of the auxiliary exhaust particulate filter 16, respectively. The collected exhaust particulates are burned to regenerate the exhaust particulate filters 16 and 22.

【0017】上述したデイーゼル機関の排気微粒子フイ
ルタにおいて、排気流量が中程度以下の場合は、流路切
換弁14は図2に示すように閉じられている。排気は入
口管2から円錐筒3を経て二重円筒状の主排気微粒子フ
イルタ22の内部へ入り、主排気微粒子フイルタ22を
径内方または径外方へ通過する時微粒子を濾過される。
濾過された排気は円錐筒7、出口筒8を経て排気マフラ
へ流れる。
In the exhaust particulate filter of the diesel engine described above, the flow path switching valve 14 is closed as shown in FIG. 2 when the flow rate of the exhaust gas is medium or less. Exhaust gas enters from the inlet pipe 2 through the conical cylinder 3 into the inside of the main exhaust fine particle filter 22 having a double cylindrical shape, and when passing through the main exhaust fine particle filter 22 inward or outward, the particles are filtered.
The filtered exhaust gas flows through the conical cylinder 7 and the outlet cylinder 8 to the exhaust muffler.

【0018】排気流量が中程度以上の場合は、排気流量
を検出するセンサ55の信号に基づく電子制御装置54
の出力により、電磁アクチユエータ53が励磁される。
磁アクチユエータ53のプランジヤ52が左方へ突出
し、流路切換弁14が支軸15を中心として時計方向へ
回動して開く。この時、排気流量の半部は前述のように
主排気微粒子フイルタ22を通過し、円錐筒7を経て出
口筒8へ流れる。排気流量の残部は副排気微粒子フイル
タ16を径外方へ通過する時微粒子を濾過される。濾過
された排気は隔壁筒23、円錐筒7を経て出口筒8へ流
れる。排気流量が中程度以下になれば、電磁アクチユエ
ータ53は消磁され、プランジヤ52が右方へ移動し、
流路切換弁14が閉じる。
When the exhaust flow rate is medium or more, the electronic control unit 54 based on the signal of the sensor 55 for detecting the exhaust flow rate.
The electromagnetic actuator 53 is excited by the output of.
The plunger 52 of the magnetic actuator 53 projects to the left, and the flow path switching valve 14 rotates clockwise about the support shaft 15 to open. At this time, half of the exhaust flow rate passes through the main exhaust particulate filter 22 and flows through the conical cylinder 7 to the outlet cylinder 8 as described above. The remaining part of the exhaust flow rate is filtered by the fine particles when passing through the auxiliary exhaust fine particle filter 16 radially outward. The filtered exhaust gas flows through the partition cylinder 23 and the conical cylinder 7 to the outlet cylinder 8. When the flow rate of exhaust gas becomes moderate or less, the electromagnetic actuator 53 is demagnetized, the plunger 52 moves to the right,
The flow path switching valve 14 is closed.

【0019】副排気微粒子フイルタ16が目詰りした場
合に副排気微粒子フイルタ16の内部の排気圧が高くな
ると、ばね18の力に抗して逃し弁19が開き、各排気
微粒子フイルタ16,22の破損を防止する。この時、
排気の一部は副排気微粒子フイルタ16の内部から出口
筒8へ直接流れる。
When the exhaust gas pressure inside the auxiliary exhaust particle filter 16 becomes high when the auxiliary exhaust particle filter 16 is clogged, the relief valve 19 opens against the force of the spring 18 and the exhaust particle filters 16, 22 of each exhaust particle filter 16 and 22 are opened. Prevent damage. At this time,
A part of the exhaust gas flows directly from the inside of the auxiliary exhaust fine particle filter 16 to the outlet tube 8.

【0020】また、各排気微粒子フイルタ22,16の
内部の排気圧が高くなると、各排気微粒子フイルタ2
2,16の内部の排気圧を検出するセンサ56の信号に
基づく電子制御装置54の出力により、電極43,41
へ通電される。すなわち、電源から電極43、主排気微
粒子フイルタ22の金網、電極41、電源へ通電回路が
形成される。金網が熱せられると、主排気微粒子フイル
タ22の内面に捕集された黒鉛などの排気微粒子が燃焼
し、主排気微粒子フイルタ22が再生される。同時に、
電源から電極42、副排気微粒子フイルタ16の金網、
電極44、電源へ通電回路が形成される。金網が熱せら
れると、副排気微粒子フイルタ16の内面に捕集された
黒鉛などの排気微粒子が燃焼し、副排気微粒子フイルタ
16が再生される。各排気微粒子フイルタ22,16の
内部の排気圧が所定値以下になれば、逃し弁19はばね
18の力を受けて閉じ、各排気微粒子フイルタ22,1
6への通電も遮断される。
When the exhaust pressure inside the exhaust particulate filters 22 and 16 becomes high, the exhaust particulate filters 2 are exhausted.
The output of the electronic control unit 54 based on the signal of the sensor 56 that detects the exhaust pressure inside the electrodes 2, 16
Is energized to. That is, an energizing circuit is formed from the power source to the electrode 43, the wire mesh of the main exhaust particulate filter 22, the electrode 41, and the power source. When the wire net is heated, exhaust particulates such as graphite collected on the inner surface of the main exhaust particulate filter 22 are burned to regenerate the main exhaust particulate filter 22. at the same time,
From the power source to the electrode 42, the auxiliary exhaust particulate filter 16 wire mesh,
An energizing circuit is formed to the electrode 44 and the power source. When the wire net is heated, exhaust particulates such as graphite collected on the inner surface of the sub exhaust particulate filter 16 are burned, and the sub exhaust particulate filter 16 is regenerated. When the exhaust pressure inside each exhaust particulate filter 22, 16 falls below a predetermined value, the relief valve 19 is closed by the force of the spring 18, and each exhaust particulate filter 22, 1 is exhausted.
The power supply to 6 is also cut off.

【0021】図3に示すように、主排気微粒子フイルタ
22の排気微粒子の捕集効率を高めるために、主排気微
粒子フイルタ22は耐熱性の無機質繊維からなるフエル
ト状体32の両面に通電用金網31,31aを重ね合
せ、糸33により捕縛して構成される。無機質繊維には
Si-Ti-C-O 系セラミツクス、Si-C-O系セラミツクス、Si
-N系セラミツクス、Si-O系セラミツクスまたは金属から
なる繊維を用い、これらの無機質繊維の表面にアルミニ
ウム、アルミナまたはコーデイエライトをコーテイング
する。排気入口側の表面になる通電加熱用金網31には
Fe-Cr-Al-Y合金のものを、排気出口側の表面になる触媒
作用をする金網31aには白金のものをそれぞれ用い
る。
As shown in FIG. 3, in order to improve the efficiency of collecting the exhaust particulates of the main exhaust particulate filter 22, the main exhaust particulate filter 22 has a felt-like body 32 made of a heat-resistant inorganic fiber on both sides thereof for conducting electricity. It is configured by superposing 31, 31a and catching with a thread 33. For inorganic fibers
Si-Ti-CO ceramics, Si-CO ceramics, Si
-N-based ceramics, Si-O-based ceramics, or fibers made of metal are used, and the surface of these inorganic fibers is coated with aluminum, alumina, or cordierite. In the wire mesh 31 for electric heating which becomes the surface on the exhaust inlet side
An Fe-Cr-Al-Y alloy is used, and a platinum wire is used for the metal net 31a that acts as a catalyst on the exhaust outlet side surface.

【0022】フエルト状体32を製作するには、カーデ
イング機械により無機質繊維を水平方向に不規則に配向
しつつ積層して互いに絡ませたうえ、針打ちして無機質
繊維を上下方向(厚さ方向)にも絡ませる。無機質繊維
は外径8〜15μm 、長さ30〜100mmのものが適当
であり、厚さ2〜10mmに積層したうえ、針打ち間隔約
4mm程度に針打ちすれば、空隙率が90〜99%の、無
機質繊維間に排気微粒子を捕捉するに十分な細長い複雑
な気孔が形成される。無機質繊維が所定寸法よりも短い
と絡みつきが悪く、長すぎると水平方向に不規則に配向
するのが厄介になる。針打ち間隔は4mm程度が適当であ
り、無機質繊維の積層厚さにより調整する。フエルト状
体32の厚さは2mm以下では排気微粒子が素通りし、厚
さが10mmを超えると、空隙率が高くなり、捕集効率が
低下し、再生時間が長くなる。
In order to manufacture the felt-like body 32, inorganic fibers are irregularly oriented in the horizontal direction by a carding machine, laminated and entangled with each other, and then needle-punched to make the inorganic fibers in the vertical direction (thickness direction). Also entwined with. An inorganic fiber having an outer diameter of 8 to 15 μm and a length of 30 to 100 mm is suitable, and if laminated with a thickness of 2 to 10 mm and needle punching at a needle punching interval of about 4 mm, the porosity is 90 to 99%. , Elongated elongated complex pores are formed between the inorganic fibers that are sufficient to trap the exhaust particulates. If the inorganic fibers are shorter than a predetermined size, the entanglement is poor, and if they are too long, it becomes difficult to orient them irregularly in the horizontal direction. It is appropriate that the needle spacing is about 4 mm, and it is adjusted by the laminated thickness of the inorganic fibers. If the thickness of the felt-like body 32 is 2 mm or less, the exhaust particulates pass through, and if the thickness exceeds 10 mm, the porosity increases, the collection efficiency decreases, and the regeneration time increases.

【0023】主排気微粒子フイルタ22の具体例を示せ
ば以下のとおりである。外径8.5μm の珪素、チタ
ン、炭素、酸素の元素からなる無機質繊維(商品名チラ
ノ繊維)を長さ50mmに切断し、切断した無機質繊維を
カーデイングの機械により水平方向に不規則に配向しつ
つ絡ませて均一な厚さに積層した。次いで、針打ち間隔
4mmに上下(厚さ)方向へ針を打ち、無機質繊維を裏面
や中間層から引き上げ、厚さ3mm、目付量200g/m
2 のフエルト状体32を形成した。無機質繊維からなる
フエルト状体32の片面にFe-Cr-Al-Y合金からなる35
メツシユの金網31を、フエルト状体32の他面に白金
からなる35メツシユの金網31aをそれぞれ重合せ結
合し、二重円筒状の排気微粒子フイルタ22を作製し
た。
A specific example of the main exhaust particulate filter 22 is as follows. An inorganic fiber (trade name: Tyranno fiber) having an outer diameter of 8.5 μm and made of elements of silicon, titanium, carbon, and oxygen is cut into a length of 50 mm, and the cut inorganic fiber is horizontally and irregularly oriented by a carding machine. They were entwined while being entwined and laminated to have a uniform thickness. Next, the needles are struck in the vertical (thickness) direction at a needle spacing of 4 mm to pull up the inorganic fibers from the back surface or the intermediate layer, and the thickness is 3 mm and the basis weight is 200 g / m
Two felt-like bodies 32 were formed. One side of the felt-like body 32 made of inorganic fiber is made of Fe-Cr-Al-Y alloy 35
The mesh metal mesh 31 was superposed on the other surface of the felt-like body 32 and the mesh metal mesh 31a made of platinum was polymerized and bonded to each other to form the double cylindrical exhaust particulate filter 22.

【0024】副排気微粒子フイルタ16は金属多孔質体
(Ni−Cr系メタルホーム)の気孔径が300〜50
0μm と大きく、排気微粒子の捕集効率が約20%と低
いので、捕集する粒径を調整しかつ耐腐食性を向上する
ために、アルミニウムのペーストを含浸塗布し、気孔径
を250〜300μm に調整した。
The auxiliary exhaust fine particle filter 16 has a porous metal body (Ni-Cr type metal home) having a pore diameter of 300 to 50.
Since it is as large as 0 μm and the collection efficiency of exhaust particulates is low at about 20%, aluminum paste is impregnated and applied to adjust the particle size to be collected and improve corrosion resistance, and the pore size is 250 to 300 μm. Adjusted to.

【0025】上述の具体例では、副排気微粒子フイルタ
16の金属多孔質体を250〜300μm に調整した
が、100μm 程度にまで調整してもよい。また、金属
多孔質体の代りに、コーデイエライト・セラミツクスか
らなる多孔質体、または主排気微粒子フイルタ22のも
のと同様に、無機質繊維からなるフエルト状体の目付量
を制御して空隙率を大きくしたものを用いてもよい。
Although the metal porous body of the sub exhaust particulate filter 16 is adjusted to 250 to 300 μm in the above-mentioned specific example, it may be adjusted to about 100 μm. Further, instead of the porous metal body, as in the case of the porous body made of cordierite ceramics or the main exhaust fine particle filter 22, the felt-like body made of inorganic fibers is controlled to control the porosity. A larger one may be used.

【0026】本発明に係る主排気微粒子フイルタ22の
比較例として、排気微粒子フイルタ全体を金属多孔質体
にしたものを作製し、本発明に係る主排気微粒子フイル
タ22と比較例の各捕集効率を表1に示す。この試験結
果から明らかなように、本発明に係る主排気微粒子22
の捕集効率が非常に高く、圧力損失が小さい。
As a comparative example of the main exhaust fine particle filter 22 according to the present invention, one in which the entire exhaust fine particle filter is made of a metal porous body is produced, and the collection efficiency of each of the main exhaust fine particle filter 22 according to the present invention and the comparative example. Is shown in Table 1. As is clear from the test results, the main exhaust fine particles 22 according to the present invention
The collection efficiency is very high and the pressure loss is small.

【0027】 表1 排気微粒子 排気微粒子の 圧力損失(mmHg) 圧力損失(mmHg) フイルタ 捕集効率(%) 流量20m3/min. 流量20m3/min. 捕集量0 の時 捕集量45g/m2の時 本発明のもの 80 4 120 比較例 50 0 40 現状のデイーゼル機関で許容できる排気微粒子フイルタ
の圧力損失は150mmHg以下、排気微粒子の捕集効率は
50%以上が望まれるが、本発明に係る主排気微粒子フ
イルタ22のフエルト状体32は空隙率が高いので圧力
損失が小さく、排気微粒子の捕集効率が高く、主排気微
粒子フイルタ22の表面積を従来のハニカム型のものの
約1/3に狭くできる。この理由は無機質繊維からなる
フエルト状体32に繊維の密な部分と繊維の粗の部分が
混在し、表面近くの繊維の粗の部分で大きな排気微粒子
が捕集され、表面よりも内側の繊維の蜜の部分で小さい
排気微粒子が捕集されることによる。
Table 1 Exhaust particulates Exhaust particulates Pressure loss (mmHg) Pressure loss (mmHg) Filter collection efficiency (%) Flow rate 20 m3 / min. Flow rate 20 m3 / min. Collection rate 0 when collected 45 g / m2 At the time of the present invention 80 4 120 Comparative example 50 0 40 The pressure loss of the exhaust particulate filter acceptable in the current diesel engine is 150 mmHg or less, and the exhaust particulate collection efficiency is desired to be 50% or more. The felt-like body 32 of the main exhaust particulate filter 22 has a high porosity so that the pressure loss is small, the exhaust particulate collection efficiency is high, and the surface area of the main exhaust particulate filter 22 is narrowed to about 1/3 that of the conventional honeycomb type. it can. The reason for this is that the felt-like body 32 made of an inorganic fiber has a mixture of a dense portion of fibers and a coarse portion of fibers, and large exhaust fine particles are collected in the coarse portion of the fibers near the surface, so that the fibers inside the surface are covered. This is because small exhaust particles are collected in the honey part.

【0028】[0028]

【発明の効果】本発明は上述のように、デイーゼル機関
の排気流路を主排気流路と副排気流路とに分岐し、該分
岐部付近に排気流量に対応して開閉制御される流路切換
弁を設け、主排気流路には両面に通電加熱用金網を有す
る気孔径の小さな無機質繊維からなるフエルト状の主排
気微粒子フイルタを配設し、副排気流路には主排気微粒
子フイルタよりも気孔径の大きな副排気微粒子フイルタ
を配設したものであり、排気流量が少ない時は気孔径が
小さい無機質繊維のフエルト状体からなる主排気微粒子
フイルタにより排気微粒子を効率よく捕集でき、排気流
量が多い時は気孔径が大きい無機質繊維のフエルト状体
または金属多孔質体(メタルホーム)からなる副排気微
粒子フイルタを併用して排気微粒子を捕集し、圧力損失
を小さくできる。
As described above, according to the present invention, the exhaust passage of the diesel engine is branched into the main exhaust passage and the sub-exhaust passage, and the flow is controlled to be opened and closed in the vicinity of the branch portion according to the exhaust flow rate. A flow switching valve is provided, and a main exhaust particulate filter is provided in the main exhaust channel, which is made of inorganic fiber with a small pore size and has wire mesh for electric heating on both sides.The main exhaust particulate filter is provided in the auxiliary exhaust channel. A secondary exhaust fine particle filter having a larger pore diameter is arranged, and when the exhaust flow rate is small, the exhaust particulate can be efficiently collected by the main exhaust fine particle filter made of a felt-like body of inorganic fibers having a small pore diameter, When the flow rate of exhaust gas is large, the exhaust gas particles can be collected by using the auxiliary exhaust gas particle filter made of a felt-like body of inorganic fibers or a porous metal body (metal home) having a large pore diameter to reduce the pressure loss.

【0029】特に、主排気微粒子フイルタが無機質繊維
からなるフエルト状体の表面だけでなく、内部でも捕集
されるので、排気微粒子の高い捕集効率が得られる。
In particular, since the main exhaust particulate filter is collected not only on the surface of the felt-like body made of inorganic fibers but also inside, a high exhaust particulate collection efficiency can be obtained.

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

【図1】本発明に係るデイーゼル機関の排気浄化装置の
概略構成を示す側面図である。
FIG. 1 is a side view showing a schematic configuration of an exhaust emission control device for a diesel engine according to the present invention.

【図2】同排気浄化装置の側面断面図である。FIG. 2 is a side sectional view of the exhaust emission control device.

【図3】同排気浄化装置における主排気微粒子フイルタ
の側面断面図である。
FIG. 3 is a side sectional view of a main exhaust particulate filter in the exhaust emission control device.

【符号の説明】[Explanation of symbols]

A:主排気流路 B:副排気流路 16:副排気微粒子
フイルタ 22:主排気微粒子フイルタ 31,31
a:金網 32:フエルト状体 33:糸
A: Main exhaust flow passage B: Sub exhaust flow passage 16: Sub exhaust particulate filter 22: Main exhaust particulate filter 31, 31
a: wire mesh 32: felt-like body 33: thread

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 B01D 46/30 B 7446−4D ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Internal reference number FI technical display location B01D 46/30 B 7446-4D

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】デイーゼル機関の排気流路を主排気流路と
副排気流路とに分岐し、該分岐部付近に排気流量に対応
して開閉制御される流路切換弁を設け、主排気流路には
両面に通電加熱用金網を有する気孔径の小さな無機質繊
維からなるフエルト状の主排気微粒子フイルタを配設
し、副排気流路には主排気微粒子フイルタよりも気孔径
の大きな副排気微粒子フイルタを配設したことを特徴と
する、デイーゼル機関の排気浄化装置。
An exhaust passage of a diesel engine is branched into a main exhaust passage and a sub-exhaust passage, and a passage switching valve that is controlled to open and close according to an exhaust flow rate is provided near the branch portion, and a main exhaust passage is provided. A felt-like main exhaust particulate filter made of inorganic fiber with a small pore size, which has wire mesh for electric heating on both sides, is installed in the flow passage, and a sub-exhaust passage has a larger pore diameter than the main exhaust particulate filter. An exhaust emission control device for a diesel engine, which is provided with a fine particle filter.
【請求項2】前記副排気微粒子フイルタは空隙率が98
%以下の無機質繊維からなる、請求項1に記載のデイー
ゼル機関の排気浄化装置。
2. The secondary exhaust particulate filter has a porosity of 98.
The exhaust gas purification device for a diesel engine according to claim 1, wherein the exhaust gas purification device is made of an inorganic fiber of not more than%.
【請求項3】前記副排気微粒子フイルタは導電性金属多
孔質体からなる、請求項1に記載のデイーゼル機関の排
気浄化装置。
3. The exhaust purification system for a diesel engine according to claim 1, wherein the auxiliary exhaust particulate filter is made of a conductive metal porous body.
【請求項4】前記副排気微粒子フイルタは導電性金属多
孔質体にアルミニウムのペーストを含浸塗布してなる、
請求項1に記載のデイーゼル機関の排気浄化装置。
4. The auxiliary exhaust fine particle filter is formed by impregnating and coating aluminum porous paste on a conductive metal porous body.
An exhaust emission control device for a diesel engine according to claim 1.
JP6114132A 1994-04-28 1994-04-28 Exhaust emission control device for diesel engine Pending JPH07293223A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6114132A JPH07293223A (en) 1994-04-28 1994-04-28 Exhaust emission control device for diesel engine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6114132A JPH07293223A (en) 1994-04-28 1994-04-28 Exhaust emission control device for diesel engine

Publications (1)

Publication Number Publication Date
JPH07293223A true JPH07293223A (en) 1995-11-07

Family

ID=14629946

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6114132A Pending JPH07293223A (en) 1994-04-28 1994-04-28 Exhaust emission control device for diesel engine

Country Status (1)

Country Link
JP (1) JPH07293223A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7354558B2 (en) 2003-09-24 2008-04-08 Toyota Jidosha Kabushiki Kaisha Exhaust gas purification system

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7354558B2 (en) 2003-09-24 2008-04-08 Toyota Jidosha Kabushiki Kaisha Exhaust gas purification system
DE102004044731B4 (en) * 2003-09-24 2013-10-02 Toyota Jidosha Kabushiki Kaisha emission Control system

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