JPS58137425A - Filter apparatus for exhaust gas - Google Patents

Filter apparatus for exhaust gas

Info

Publication number
JPS58137425A
JPS58137425A JP57019419A JP1941982A JPS58137425A JP S58137425 A JPS58137425 A JP S58137425A JP 57019419 A JP57019419 A JP 57019419A JP 1941982 A JP1941982 A JP 1941982A JP S58137425 A JPS58137425 A JP S58137425A
Authority
JP
Japan
Prior art keywords
filter
exhaust gas
end surface
peripheral surface
case
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP57019419A
Other languages
Japanese (ja)
Other versions
JPH0153082B2 (en
Inventor
Mitsuyoshi Kawamura
川村 光義
Shintaro Hirate
平手 信太郎
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.)
Nippon Tokushu Togyo KK
Niterra Co Ltd
Original Assignee
NGK Spark Plug Co Ltd
Nippon Tokushu Togyo KK
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 NGK Spark Plug Co Ltd, Nippon Tokushu Togyo KK filed Critical NGK Spark Plug Co Ltd
Priority to JP57019419A priority Critical patent/JPS58137425A/en
Publication of JPS58137425A publication Critical patent/JPS58137425A/en
Publication of JPH0153082B2 publication Critical patent/JPH0153082B2/ja
Granted legal-status Critical Current

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

Abstract

PURPOSE:To prevent an electric leak, by using a cylindrical ceramic porous body wherein the outer peripheral surface thereof is an earth potential electrode and the inner peripheral surface thereof is other electrode as a filter. CONSTITUTION:To one circular end surface of a filter 1, a non-porous insulating ceramic disc 5 having a diameter same to that of said filter is bonded in a closely contacted state. To the other end surface of the filter 1, a non-porous insulating ceramic disc 7 having a diameter same to that of said filter is also bonded in a closely contacted state. A case 9 has an end surface wall 19 in the upstream side of an exhaust gas and an appropriate number of inflow ports 9a are provided by drilling to the peripheral flange of siad end surfadce wall 19 while a hole part 9c is provided to the central part of the end surface wall 19 in a concentrically circular relation to the end surface wall 19. In addition, to the end surface wall 19 between the inflow ports 9a and the hole part 9c, a ring like ridge 12b is provided at right angles so as to fit the inner periphery thereof with the upstream side end part of the filter 1. The entire upstream end surface of the case 9 is bonded to a connecting lid body 8 in a gastight state.

Description

【発明の詳細な説明】 本発明はガス中に含まれる]燃性微粒1′、1′Iに自
動車の111ガス中IJ含5[れるカーボン等の111
燃竹微粒子を除去Jるためのフィル今装置に関するbの
であり、更に:;T L、 < lよフィルタ自体に通
電しく発熱させることにより、高濾過f1を保16シ、
 1.:まま、濾別し1c可燃1つ微粒子を効率的に燃
焼除去716ノイルタ装置に関するらのである。
DETAILED DESCRIPTION OF THE INVENTION The present invention is directed to combustible fine particles 1', 1'I contained in gas and 111 of carbon, etc. contained in 111 gas of automobiles.
This is related to a filter device for removing particulates from burning bamboo, and furthermore, by energizing the filter itself and generating heat, a high filtration f1 can be maintained.
1. : It is related to the 716 Noirta device which efficiently burns and removes the combustible particulates by filtering and separating them.

従来、例λば公害対策として自動車エンジンの排ガス中
に含まれるカーボン微粒子を除去するために、刊気糸8
したは1)1気運流系に、フィル//^用いることが提
案されているが、長期の使用(はh−ホンがJtt、 
M L T [l Fn’i ”) f起コシ、I−+
−)) 48 人ヲ′1するという欠点があった。この
欠点を解消りるbのとしてフィルタの微粒1捕12部位
にニク11ノ1線ヒータあるいは発熱金属層を組み合わ
せて通電1111熱したり、捕捉部イス?に燃料を噴)
1して燃filの燃焼熱で加熱したり、高圧電極を設(
Jて火花放電により加熱したり、又、フィルタをカーボ
ン11$11どし、イのカーボン微粒子に通N′?lる
ことにより加熱して、−2− カーボン微粒子を焼却し+ 「I L!jまりを防ぐ方
法がとられていた。
Conventionally, for example, in order to remove carbon particulates contained in the exhaust gas of automobile engines as a pollution control measure,
1) It has been proposed to use fill//^ in the air flow system, but for long-term use (H-phone is Jtt,
M L T [l Fn'i ”) f rise, I-+
-)) 48 It had the disadvantage of requiring 1 person. As a solution to this drawback, a single-wire heater or a heat-generating metal layer may be combined with the part of the filter that captures particulates to heat the part of the filter. )
1 and then heat it with the combustion heat of fuel fil or install a high voltage electrode (
The filter is heated by spark discharge, or the filter is heated with carbon 11$11, etc., and the carbon particles are passed through the filter. A method was used to prevent clumping by heating the carbon particles by heating and incinerating the carbon particles.

しかし、−り11ム線を使用Jる場合は発熱面積が少な
くて1ネルギ効率が恕り、又、フィルタへの取り付けも
手間のかかるものであり、発熱金属層を設(プる場合は
濾過の障害にならないにうに細く小面積に設置プなくて
はならず、やはりエネルギ効率が悪く、取りイζHJら
手間がかかるものであり、υ1ガスににり貯湯がうまく
ゆかない場合は]ンジンを止めてから、フrルタにたま
ったカーボン微粒子を燃焼させな番−Jれば(j−らな
いことも生じた。
However, when using a 11mm wire, the heat generating area is small and the energy efficiency is poor, and it is also time consuming to attach it to the filter, so it is necessary to install a heat generating metal layer. It has to be installed in a narrow and small area so that it does not become a hindrance to the water supply, and it is also inefficient in terms of energy efficiency and takes time and effort to remove. After stopping, there were cases where the carbon particles that had accumulated in the filter were not allowed to burn.

又、燃料噴制および高圧放電方法は格別に複雑な駅部を
必要とし、丁ネルギを大量に消費し、燃料ににる火災1
−の問題、放電によるフィルタの損傷を牛し、又、カー
ボン繊維を使用したものは繊維自体が燃焼により消失し
てしまう欠点を有していlこ 、。
In addition, fuel injection and high-pressure discharge methods require particularly complex station areas, consume large amounts of energy, and can cause fires caused by fuel leakage.
- Problems include damage to the filter due to discharge, and those using carbon fiber have the disadvantage that the fiber itself is destroyed by combustion.

方、同様な用途にセラミックのハニカム構造フィルタが
知られており、このものは一般のフィルタに比べ、目を
細かくしても圧力損失が少なく−3− てづみ、しか−し、1ンパクトであるので自動中の1)
1ガス中のカーボン除去用に好適なものであるが1」粘
りを生じた場合、i11′ijI面が広範■1にわたる
ので、フィルりを使用部位より取りはずして全体を加熱
処理し、カーボン微粒子を燃焼消滅させなくて(:Lな
らなかった。更に、目詰まり防止の方法どしては、スラ
ンレスウール、アルミナペレッ1−等の一ノイルタの目
の細かさを段階的に変化させ、カーボン微粒子を分散さ
Vて捕捉し、更に燃料噴的によりカーボン微粒子を加熱
燃焼させる方法も提案されているが、カーボン微粒子捕
捉が不1−分であり又、排ガスは低酸素状態であるので
温度り昇にも限界があり速やかな焼MJができないのど
、KMが複雑になる欠点を有していた。
On the other hand, ceramic honeycomb structure filters are known for similar applications, and compared to general filters, these filters have less pressure loss even when the mesh is finely divided, and have an impact of only 1. So automatic 1)
1.It is suitable for removing carbon from gas, but if it becomes sticky, the i11'ijI surface covers a wide area. Furthermore, as a method to prevent clogging, the fineness of the mesh of a filter such as slanless wool or alumina pellets can be changed in stages, and carbon fine particles can be A method has also been proposed in which the carbon particles are captured by dispersion and further heated and combusted by fuel injection, but this method takes only a few minutes to capture the carbon particles, and the temperature rises because the exhaust gas is in a low oxygen state. However, it has the disadvantage that it is not possible to perform quick MJ due to its limitations, and that KM becomes complicated.

以上の問題を解決するものとして上記のハニカム構造の
セラミックフィルタ自体を自己通電発熱体とづることも
考慮されており、その効率的イT発熱性、カーボン微粒
子捕捉性を有することにJ、l/)、特に自動車排ガス
用ノイルタどして有望視され(いるものである、。
As a solution to the above problems, it has been considered to use the honeycomb-structured ceramic filter itself as a self-energizing heating element. ), and is particularly promising as a noilter for automobile exhaust gas.

−4− L)かし、での場合、−フィルタ全体が通電v1を有す
るので、そのまま排気管あるいは、排気還流管中へ付設
部ることは付設部(f/の材質が一般に鋼鉄等の電導体
であるところから、そのままでは漏電を引き起こし、何
らかの絶縁処理若しくは絶縁体を介して付設する必要が
あり、そのため濾過作用とは本質的に関係のない加工、
組み立て1稈あるいは部品数が必要であった。
-4- In the case of L), since the whole filter has a current v1, it is not possible to attach the part to the exhaust pipe or exhaust recirculation pipe as it is. Since it is a conductor, it will cause electrical leakage if it is left as it is, and it must be installed through some kind of insulation treatment or insulator, so processing that is essentially unrelated to the filtration effect,
One culm or several parts were required for assembly.

そこで本発明者らは、鋭意研究の結果、外周面が接地電
位電極、内周面がもう一方の電極である導電性セラミッ
クの筒状多孔体をフィルタとして使用することににす、
フィルタ自体に特に絶縁処理をしたり、絶縁体を組み合
わせなくとも、漏電を防ぐことができるごどを見い出し
、本発明を完成したのである。
As a result of intensive research, the inventors of the present invention decided to use as a filter a cylindrical porous body made of conductive ceramic whose outer circumferential surface is a ground potential electrode and whose inner circumferential surface is the other electrode.
They discovered that it is possible to prevent electrical leakage without insulating the filter itself or combining it with an insulator, and completed the present invention.

即f5本発明の要旨とでるところは、排ガスの濾過作用
を有するII導電性′ラミック多孔体を導電性レラミッ
クで筒状形に形成し、その外周面と内周面とに通電加熱
用の電極手段を設け、該筒形状多孔体の外周面でケース
に支持せしめ、外周面重積−5− を接地電IQ/側としC排ガスを濾過することを1!t
1牧とする排ガス用フィルタ装岡にある。
The gist of the present invention is that a II conductive lamic porous body having an exhaust gas filtration action is formed into a cylindrical shape using conductive lamic, and electrodes for electrical heating are provided on the outer and inner circumferential surfaces of the II conductive lamic porous body. 1! A means is provided, the outer peripheral surface of the cylindrical porous body is supported by the case, and the outer peripheral surface is set as the grounding voltage IQ/ side to filter the exhaust gas. t
It is located in the exhaust gas filter mounting area.

次に、図を参照しつつ説明づる。Next, it will be explained with reference to the figures.

第1図(5L自動車排ガス用フイルタ装置に適用1〕た
本発明の第1実施例を示す。
FIG. 1 shows a first embodiment of the present invention (applied to a 5L automobile exhaust gas filter device).

ここにおいて、1は中空円筒体状の多孔質導電性セラミ
ックフィルタを表し、孔口の径の大ささは0.1〜1n
vのものが使用される。
Here, 1 represents a hollow cylindrical porous conductive ceramic filter, and the diameter of the pores is 0.1 to 1 nm.
v is used.

フィルタ1の外周面の全面または部分的に金属質電極が
メタライズm3として形成され、内周面の全面または部
分的に金属質電極がメタライズ層4として形成され(い
る。
A metallic electrode is formed as a metallized layer m3 on the entire or partially outer circumferential surface of the filter 1, and a metallic electrode is formed as a metallized layer 4 on the entire or partially inner circumferential surface.

上記メタライズ43.4には各々導線1ご3.14が溶
接その他の方法で接続され、各々碍子16.17を介し
て絶縁状態に外部へ導かれて、該導線13はスイッチ1
5を介して電源Eに接続されており、他の導線14は電
源Eの他の極へ直接接続されている。ここで導線13側
で接地がなされ、メタライズ層3の電極側が接地電荀と
11つている。1−1−記構成ににす、フィルタ1、メ
タライズ層3、=  6 − 4、導線13.1/1.スイツ115及び電源[全体で
通電加熱回路を形成しCいる。
Conductive wires 1 and 3.14 are respectively connected to the metallization 43.4 by welding or other methods, and are led to the outside through insulators 16.17 in an insulated state.
5 to the power supply E, and the other conductor 14 is connected directly to the other pole of the power supply E. Here, the conducting wire 13 side is grounded, and the electrode side of the metallized layer 3 is connected to a grounding conductor. According to the configuration described in 1-1-, filter 1, metallized layer 3, = 6-4, conductive wire 13.1/1. The switch 115 and the power source together form an energizing heating circuit.

上記フィルタ1の円形の端面の一方には、同径の:11
多孔質絶縁性ヒ“)ミック円形板5が密着状態に結合さ
れている。、一方、フィルタ1の他端部にも同径の非多
孔質絶縁4/1セラミツク円形板7が密着状態に結合さ
れているが、該円形板7はその中心に円形穴及び該穴(
、″適合された円筒管7aが設置1られ、フィルタの中
心穴部6どほぼ同形の流出ロア1)を形成している。
One of the circular end surfaces of the filter 1 has the same diameter as: 11
A porous insulating ceramic circular plate 5 is tightly coupled to the other end of the filter 1.A non-porous insulating 4/1 ceramic circular plate 7 of the same diameter is also tightly coupled to the other end of the filter 1. However, the circular plate 7 has a circular hole in its center and the hole (
, ``A fitted cylindrical tube 7a is installed 1, forming an outflow lower 1) of approximately the same shape as the central hole 6 of the filter.

5)はフィルタを収納Jるための排気管、す1気運wL
管等のケースであり、その排ガス上流側に端面壁19を
インし、その端部壁には流入1]9aが、端部ら!19
の周縁に適当な個数穿設され、端部壁19の中心部にも
端百号ン19と同心円状に穴部9(]が穿設されている
。ただし、穴部9Cは軽量化のために設けられ1こ士)
のであり、穿設しなくてもJ:い。
5) is the exhaust pipe for storing the filter,
It is a case such as a pipe, and an end wall 19 is inserted on the upstream side of the exhaust gas, and the inflow 1]9a is injected into the end wall from the end! 19
An appropriate number of holes are drilled around the periphery of the end wall 19, and a hole 9 (] is also drilled in the center of the end wall 19 concentrically with the end wall 19.However, the hole 9C is made in order to reduce weight. 1 person)
Therefore, there is no need to drill holes.

上記流入II 9 aど穴部9Gとの間の端面v19に
直角に、その内周が上記フ、Cルタ1の上流側端一  
7 一 部IJ適合するJ、うイ「環状突条12bが設けられ、
該環状突条121)とその内側の端部壁1≦)とでフィ
ルタ1の」流側端部(こ結合している円形板5を密着状
態に支持し、機密状態を保っている。
The inner periphery is perpendicular to the end face v19 between the inlet II 9a and the upstream end of the filter 1.
7 Partially compatible with IJ,
The annular protrusion 121) and the inner end wall 1≦) closely support the circular plate 5 connected to the stream side end of the filter 1, thereby maintaining the airtight state.

ケース9の上流端面全体は短円筒形の接続蓋体8により
、各々の周縁鍔部20.21が互いに結合して、気密状
態に覆われている。そし゛C該蓋体8の一部に排ガス導
入口8aを右する管体(I Gが付設され、該管体8C
は、イブジ−ストマニホールドに1&続され(いる。
The entire upstream end surface of the case 9 is hermetically covered by a short cylindrical connecting lid 8 with peripheral flanges 20 and 21 connected to each other. A pipe body (IG) is attached to a part of the lid body 8 to the right of the exhaust gas inlet 8a, and the pipe body 8C
is connected to the valve thrust manifold.

一=方、ノノース9の上流端面全体は、tliit利状
接続蓋状接続蓋体10各々の周縁の鍔部22.23が亙
いに結合し゛C1気密状態に覆われ゛ている9、匠して
該漏斗状蓋体10は、そのυIガス流入口の内周面に突
出しCいる係止突条11a及びイの内周面が上記フィル
タ1の下流側の端部及び外周面端部に適合Jるような環
状突条11bが設りられ−(おり、蓋体10をケース9
に取り付けた際、上記係[1突条11a及び環状突条1
1bがフィルタ1の下流側端部を密着状態に支持し、気
密状態を保持−8− づる1、勃体10の下流側には小径の初出1”、、11
0 dを右し、図示しない1)1気管に接続されている
On the other hand, the entire upstream end surface of the nonose 9 is covered in an airtight state by connecting the flanges 22 and 23 on the periphery of each of the connecting lids 10 in an airtight manner. The funnel-shaped lid body 10 has locking protrusions 11a and 11a protruding from the inner circumferential surface of the υI gas inlet, respectively, and the inner circumferential surface of the locking protrusions C and A fit the downstream end and the outer circumferential surface end of the filter 1, respectively. An annular protrusion 11b that looks like this is provided.
When attached to
1b tightly supports the downstream end of the filter 1 and maintains an airtight state.
0 d on the right and is connected to 1) 1 trachea (not shown).

以上の構成におい−(,1ニンジンからのカーボン微粒
子を含んだ1.11ガスは、イブジ−ストマニホールド
をイのまま通過して、点線でしめでように上流方向Fに
り接続蓋体8の導入口8aに流入りる。
In the above configuration, the 1.11 gas containing carbon particles from the carrot passes through the Ibjist manifold as it is, and moves in the upstream direction F as shown by the dotted line to the connecting lid 8. It flows into the inlet 8a.

更に、蓋体8中で分流して、ケース9の端面壁19に開
口している流入+198から、ケース9の内部へ流入)
る。次いで、排ガスは))−ス9内部に露出している円
筒形のフィルタ1の外周面よりメタライズ層3を通過し
てぞの多孔質の内部へ浸入する。ここにおいて、カーボ
ン微粒子が捕捉され、J′J+ガスは、bう一方のメタ
ライズ層4を通過して中心穴部6へ流出する1、この時
点でカーボン微粒子はフィルタコ全(1に分1攻して捕
1fi!されており、排ガス中にはほとんど認められな
い。
Furthermore, the flow is divided in the lid body 8 and flows into the inside of the case 9 from the inflow +198 opened in the end wall 19 of the case 9)
Ru. Next, the exhaust gas passes through the metallized layer 3 from the outer peripheral surface of the cylindrical filter 1 exposed inside the space 9 and enters into the porous interior thereof. Here, the carbon particles are captured, and the J'J+ gas passes through the other metallized layer 4 and flows out into the center hole 6. At this point, the carbon particles attack the entire filter (1 in 1). 1fi!, and is hardly recognized in exhaust gas.

次に排ガスは中心穴部6から非多孔質絶縁性セラミック
円形板7の流出ロアbよりケース9内部から漏斗状蓋体
10へ流出し、次いで該蓋体10の排出D10dより■
気管へ排出する。
Next, the exhaust gas flows from the center hole 6 to the funnel-shaped lid 10 from inside the case 9 through the outflow lower b of the non-porous insulating ceramic circular plate 7, and then from the exhaust D10d of the lid 10.
Excretes into the trachea.

−9− このとき、加熱回路のスイツf′15がインし7(いて
、金属質電極であるメタライズli′4:’I、71間
(J通電が行われていると、フィルタ1中に分11にし
−(捕捉されているカーボン微粒子がフィルタ1自捧の
発熱にJ、す、速やかに燃焼演滅づる。
-9- At this time, when the heating circuit switch f'15 is turned on and the metallized electrodes li'4:'I and 71 (J are energized), there is a 11 - (The captured carbon particles quickly burn and disappear due to the heat generated by the filter 1.

次に第2図は本発明の第2実施例を示づ。Next, FIG. 2 shows a second embodiment of the present invention.

ここにおいて、31は中空円1n体状の多孔ri ri
pミル電性セラミックフィルタし、孔[1の径は第1実
施例と同様な−しのが使用され、フィルタ31はその両
端面の形状は中快き円形平面をな11゜上記゛フィル′
I31の外周面及び内周面に各々金属質電極どしてのメ
タライズ層33.34が設けられ、内周面のメタライズ
層34に密rIシ、フィルタ31の中心穴35の上流側
を閉鎖するIこめの非多孔質耐熱ヤ1のr!111管4
7が中心穴35に挿入されている。
Here, 31 is a hollow circular 1n-shaped porous hole ri ri
A p-mil electric ceramic filter is used, and the diameter of the holes [1 is the same as in the first embodiment].
Metalized layers 33 and 34 as metallic electrodes are respectively provided on the outer peripheral surface and the inner peripheral surface of the filter I31, and the metallized layer 34 on the inner peripheral surface is densely coated to close the upstream side of the center hole 35 of the filter 31. I rice non-porous heat resistant Ya 1 r! 111 tube 4
7 is inserted into the center hole 35.

上記フィルタ31はイの外周面が排気管、排気還流管等
のケース38内周面に密着づるにうに、ケース38の中
に納められ、外筒38の内部に突出した係止突条388
により排ガス上流側で係11− 10 − され、更にケース38ど1liilミ1林接続管39が
各々の鍔部381+、39aにて結合し、漏斗状接続管
39の他の鍔部39 dにで上記フィルタ8胃はイの排
ガス下流側で1糸止されて、その位置を保持している。
The filter 31 is housed in the case 38 so that the outer circumferential surface of A is in close contact with the inner circumferential surface of the case 38 such as an exhaust pipe, an exhaust gas recirculation pipe, etc., and a locking protrusion 388 protrudes into the inside of the outer cylinder 38.
The exhaust gas is connected on the upstream side by the connecting pipe 11-10-, and the case 38 and the connecting pipe 39 are connected at the respective flanges 381+ and 39a, and connected to the other flanges 39d of the funnel-shaped connecting pipe 39. The stomach of the filter 8 is fixed by one thread on the downstream side of the exhaust gas in A to maintain its position.

又、フィルタ装置の内周面のメタライス層34の一端4
5に導線41が溶接等により接続され、方、フィルタ3
1の外周面のメタライズ廟33が直接接触して通電状態
にあるケース38の一部4/Iに導粍)40が溶接着に
より接続されている。
Also, one end 4 of the metal rice layer 34 on the inner peripheral surface of the filter device
A conducting wire 41 is connected to the filter 3 by welding or the like.
A conductive wire 40 is connected by welding to a part 4/I of the case 38 which is in direct contact with the metallized temple 33 on the outer circumferential surface of the case 38 and is in an energized state.

導線41は漏斗状1a続管39に設置ノられた碍子/I
3を介して外部l\導出され、スイッチ42を介して電
源Eに接続され、一方、導線/1.04;を電源Eの反
対の極に接続され、導線40側で接地されている1゜ 」1記のフィルり31、ケース38.1!1線40゜4
1、スイッチ42及び電源E全体で通電加熱回路を形成
し−Cいる。
The conductor 41 is connected to the insulator/I installed in the funnel-shaped 1a continuation pipe 39.
3 and connected to the power supply E through a switch 42, while the conductor /1.04; is connected to the opposite pole of the power supply E and is grounded on the conductor 40 side. ” 1 fill 31, case 38.1! 1 line 40°4
1. The switch 42 and the power source E together form an energizing heating circuit.

以上の構成において、エンジンからのカーボン微粒子を
含んだ1」1力゛スは、イグゾーストマニホー−11= ルドをイのまま通過して、々−ス38に〒す、重線で示
1如り1ノ1万スに流方向1:より、フィルタ31へ浸
入Jる。このとき、フィルタ31の中心穴35へは閉鎖
管47がふきいひいるので、排ガスがそのま21:排気
管側F3へ索通りJることはf、Tい、。
In the above configuration, the 1'1 force containing carbon particulates from the engine passes through the exhaust manifold 11 and 38 as shown by the heavy line. In the flow direction 1:1, the water enters the filter 31 at a rate of 10,000 times. At this time, since the closed pipe 47 is blown into the center hole 35 of the filter 31, the exhaust gas does not directly pass through to the exhaust pipe side F3.

排ガスがフrルタ31の孔へ浸入すると、IJIガス中
のカーボン微粒rがフィルタ31の全体1゛分散して捕
捉され、次いでカーボン微粒子を含:1.ない排ガスは
フィルタ31の下流側j5り浸出し、漏斗状接続管39
を通過して、下流側B方向の図示しない排気管よりIJ
I出される。
When the exhaust gas enters the holes of the filter 31, the carbon particles in the IJI gas are dispersed and captured throughout the filter 31, and then the carbon particles containing: 1. Exhaust gas that does not exist leaks out through the downstream side of the filter 31 and is passed through the funnel-shaped connecting pipe 39.
from the exhaust pipe (not shown) in the direction of downstream B.
I will be served.

このとき、加熱回路のスイッチ42がオンしていて金属
質電極であるメタライズ層33.34間に通電が行われ
ていると、フィルタ31中に分散して捕捉されているカ
ーボン微粒子がフィルタ31自体の発熱に3」、す、速
やかに燃焼消滅ηる1゜上記第1及び第2実施例にd3
いて、多孔質導電性セラミックフCルタとしては、連通
孔を分布状に有する海綿状4M 3t!i体であるらの
、フェル1−状、織布状成形体等0多数″)線状索体′
7)集合構造体等 へ−12− の導電性セラミックフィルタ等を採用Jることができる
At this time, if the switch 42 of the heating circuit is turned on and electricity is applied between the metallized layers 33 and 34, which are metal electrodes, the carbon particles dispersed and captured in the filter 31 will be transferred to the filter 31 itself. d3 in the above first and second embodiments
As a porous conductive ceramic filter, a spongy 4M 3t! with communicating pores distributed in a distributed manner is used. i-body, Fell-shaped, woven fabric-like molded bodies, etc.
7) Aggregate structure, etc. -12- A conductive ceramic filter, etc. can be employed.

l−記の多孔質ンυ電1’lレジミックフィルタの製造
方法1よ組成を焼成時に多孔質となるように配合され1
=生のセラミックを焼成製造Jる以外に、例えば、次の
如くなされる。炭化珪素あるいは1珪化モリブデン等の
主成分の他に、アルミナ、シリカ等の原料微粉末、アル
ドン酸ソーダ、アルギン酸アンモン、ポリビニールアル
コール等の有機バインダー、水、]−デルアル]−ル等
の溶剤を加えて混練して泥ψ状調合物を作り、その中に
所定の目の細かさをbつ、目的とJる所定形状のポリウ
レタン等のプラスチフオームを浸漬し、乾燥後大気雰囲
気あるいは窒素雰囲気下1600℃前後で焼成°りるこ
とにJ:り得られる。
According to method 1 for producing a porous electric filter according to 1-1, the composition is blended so as to become porous upon firing.
= In addition to firing raw ceramics, the following steps can be taken, for example. In addition to the main components such as silicon carbide or molybdenum monosilicide, fine raw material powders such as alumina and silica, organic binders such as sodium aldonic acid, ammonium alginate, and polyvinyl alcohol, water, and solvents such as ]-delal]- are used. In addition, a slurry-like mixture is made by kneading, into which a plastiform such as polyurethane with a predetermined mesh size and a predetermined shape for the purpose is immersed, and after drying, it is dried under an air atmosphere or a nitrogen atmosphere. It can be obtained by firing at around 1600°C.

金属質電極手段は導電性レラミツクフィルタの両端面に
、例えば、白金等の金属粉末ペーストあるいはニッケル
、コバルト等と珪素との粉末ペース1へ混合物を焼き付
けることににり形成される。
The metallic electrode means are formed on both end faces of the conductive reramic filter by baking a mixture of metal powder paste such as platinum or powder paste 1 of nickel, cobalt, etc. and silicon into powder paste 1, for example.

この場合、端面全体に形成しなくても、格子状、−13
− 縞状等に形成しても良い。
In this case, even if it is not formed on the entire end face, a grid-like, -13
- It may be formed in a striped shape or the like.

以−1−の説明の如く本発明の排ガス用ノイルタ装置は
、>9電性レラミツクの筒形状多孔体フィルタの外周面
に接地電位電極が設けられ、内周面にはもう一方の電極
が設【プられている1、それ故、フィルタを納めている
ケース自体が外周面電極の導線の替わりになることから
れかるように、外周面電極からの漏電は何ら問題となら
ず、一方、内周面電極は、フィルタの構成部分ではl)
−スJ、す111も離れた状態にある口とにより漏電が
生ずる可能性が非常に少なくなる。以上の特徴をhJる
本発明の排ガス用フィルタ装置の使用により、フィルタ
自体を絶縁するという手段を考taiることなく、電気
コーネルギーを有効に利用Jることができるのである。
As explained in -1- below, the exhaust gas noirtater device of the present invention has a ground potential electrode provided on the outer peripheral surface of the cylindrical porous filter with >9 conductivity, and the other electrode provided on the inner peripheral surface. [1] Therefore, since the case housing the filter itself replaces the conductor of the outer electrode, leakage from the outer electrode is not a problem; The circumferential electrode is a component of the filter l)
- The possibility of electrical leakage occurring due to the openings of the terminals 111 and 111 being separated is greatly reduced. By using the exhaust gas filter device of the present invention which has the above-mentioned features, it is possible to effectively utilize electric energy without having to consider insulating the filter itself.

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

第1図は本発明の排ガス用゛ノイルタ装置の第1実施例
の断面図、第2図は本発明の第2実施例の断面図である
。 1.31・・・円筒形状導電性セラミック多孔体−1/
1.  −
FIG. 1 is a cross-sectional view of a first embodiment of the exhaust gas noilter device of the present invention, and FIG. 2 is a cross-sectional view of a second embodiment of the present invention. 1.31...Cylindrical conductive ceramic porous body-1/
1. −

Claims (1)

【特許請求の範囲】 1 排ガスの濾過作用を有する導電性セラミック多孔体
を導電性セラミックで筒形状に形成し、その外周面と内
周面とに通電加熱用の電極手段を設け、該筒形状多孔体
の外周面でケースに支持せしめ、外周面電極を接地電位
側として排カスを濾過することを特徴とする排ガス用フ
ィルタ装置。 2 濾過される排ガスが導電性セラミックの筒状多孔体
の外周面から浸入し、内周面へ排出されることを特徴と
する特許請求の範囲第1項記載の排ガス用フィルタ装置
。 3 導電性セラミックが二珪化モリブデンであることを
特徴とする特許請求の範囲第1項あるいは第2項記載の
排ガス用フィルタ装置。 4 導電性セラミックが炭化珪素であることを特徴とす
る特許請求の範囲第1項あるいは第2項記載の排ガス用
フィルタ装置。 −1−
[Scope of Claims] 1. A conductive ceramic porous body having an exhaust gas filtration action is formed into a cylindrical shape using conductive ceramic, and electrode means for energization heating is provided on the outer peripheral surface and inner peripheral surface of the conductive ceramic porous body, and the cylindrical shape is An exhaust gas filter device characterized in that the outer peripheral surface of a porous body is supported by a case, and the exhaust gas is filtered with an electrode on the outer peripheral surface set to the ground potential side. 2. The exhaust gas filter device according to claim 1, wherein the exhaust gas to be filtered enters from the outer peripheral surface of the conductive ceramic cylindrical porous body and is discharged to the inner peripheral surface. 3. The exhaust gas filter device according to claim 1 or 2, wherein the conductive ceramic is molybdenum disilicide. 4. The exhaust gas filter device according to claim 1 or 2, wherein the conductive ceramic is silicon carbide. -1-
JP57019419A 1982-02-09 1982-02-09 Filter apparatus for exhaust gas Granted JPS58137425A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57019419A JPS58137425A (en) 1982-02-09 1982-02-09 Filter apparatus for exhaust gas

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57019419A JPS58137425A (en) 1982-02-09 1982-02-09 Filter apparatus for exhaust gas

Publications (2)

Publication Number Publication Date
JPS58137425A true JPS58137425A (en) 1983-08-15
JPH0153082B2 JPH0153082B2 (en) 1989-11-13

Family

ID=11998734

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57019419A Granted JPS58137425A (en) 1982-02-09 1982-02-09 Filter apparatus for exhaust gas

Country Status (1)

Country Link
JP (1) JPS58137425A (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61118620U (en) * 1985-01-11 1986-07-26
JPS63105716U (en) * 1986-12-27 1988-07-08
JPH01281121A (en) * 1988-01-27 1989-11-13 Agency Of Ind Science & Technol Apparatus for removal of combustible fine particles
WO1993005862A1 (en) * 1991-09-20 1993-04-01 Nippondenso Co., Ltd. Self-heating filter
JPH0540200U (en) * 1991-10-29 1993-05-28 麒麟麦酒株式会社 Liquid pouring device
WO2002042615A1 (en) * 2000-11-21 2002-05-30 Siemens Aktiengesellschaft Method for reducing particle emissions containing carbon of diesel motors and a corresponding system
WO2002047796A3 (en) * 2000-12-13 2003-02-27 Ut Battelle Llc Device for separating co2 from fossil-fueled power plant emissions
WO2011114444A1 (en) * 2010-03-16 2011-09-22 イビデン株式会社 Sensor for exhaust purification use

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57190626A (en) * 1981-05-19 1982-11-24 Bridgestone Corp Material for collecting particulate in engine exhaust gas

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57190626A (en) * 1981-05-19 1982-11-24 Bridgestone Corp Material for collecting particulate in engine exhaust gas

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61118620U (en) * 1985-01-11 1986-07-26
JPS63105716U (en) * 1986-12-27 1988-07-08
JPH0521614Y2 (en) * 1986-12-27 1993-06-03
JPH01281121A (en) * 1988-01-27 1989-11-13 Agency Of Ind Science & Technol Apparatus for removal of combustible fine particles
WO1993005862A1 (en) * 1991-09-20 1993-04-01 Nippondenso Co., Ltd. Self-heating filter
US5405422A (en) * 1991-09-20 1995-04-11 Nippondenso Co., Ltd. Self-heating filter
JPH0540200U (en) * 1991-10-29 1993-05-28 麒麟麦酒株式会社 Liquid pouring device
WO2002042615A1 (en) * 2000-11-21 2002-05-30 Siemens Aktiengesellschaft Method for reducing particle emissions containing carbon of diesel motors and a corresponding system
WO2002047796A3 (en) * 2000-12-13 2003-02-27 Ut Battelle Llc Device for separating co2 from fossil-fueled power plant emissions
GB2389325A (en) * 2000-12-13 2003-12-10 Ut Battelle Llc Device for separating CO2 from fossil-fueled power plant emissions
GB2389325B (en) * 2000-12-13 2004-10-13 Ut Battelle Llc Device for separating CO2 from fossil-fueled power plant emissions
WO2011114444A1 (en) * 2010-03-16 2011-09-22 イビデン株式会社 Sensor for exhaust purification use

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