JPH06317140A - Filter for collecting particulate in exhaust gas - Google Patents
Filter for collecting particulate in exhaust gasInfo
- Publication number
- JPH06317140A JPH06317140A JP5136381A JP13638193A JPH06317140A JP H06317140 A JPH06317140 A JP H06317140A JP 5136381 A JP5136381 A JP 5136381A JP 13638193 A JP13638193 A JP 13638193A JP H06317140 A JPH06317140 A JP H06317140A
- Authority
- JP
- Japan
- Prior art keywords
- filter plate
- conductive
- conductive filter
- exhaust gas
- opening
- 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
Landscapes
- Processes For Solid Components From Exhaust (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】ディーゼル車等から排出されるガ
スはスス状の炭素質の微粒子(以下「微粒子」と略称)
を含んでおり、この低減が地球環境問題における早期に
解決すべき重大な課題の一つとなっている。本発明は、
これらディーゼルエンジン等の内燃機関から排出される
ガスに含まれる微粒子を除去するための方法及びフィル
ターに関する。[Industrial application] Gas emitted from diesel vehicles is soot-like carbonaceous fine particles (hereinafter abbreviated as "fine particles")
This reduction is one of the important issues to be solved at an early stage in global environmental problems. The present invention is
The present invention relates to a method and a filter for removing fine particles contained in a gas discharged from an internal combustion engine such as a diesel engine.
【0002】[0002]
【従来の技術】従来、ディーゼルエンジン車から排出さ
れるガス中の微粒子を捕集するフィルターとしては、セ
ラミックス製のハニカム構造体が主として検討されてい
る(特開昭57−7216)。ここでハニカム構造体と
は、隔壁により区分された複数の貫通孔を有し、単位容
積あたりに濾過面積を多くとることができる構造体であ
る。ディーゼル車排ガスの微粒子捕集用としては、セル
密度が10〜15セル/cm2、総セル数1500〜2
500、隔壁厚0.3〜0.5mm、濾過面積約1.5
cm2が例示されている。2. Description of the Related Art Conventionally, a ceramic honeycomb structure has been mainly studied as a filter for collecting fine particles in a gas discharged from a diesel engine vehicle (Japanese Patent Laid-Open No. 57-7216). Here, the honeycomb structure is a structure having a plurality of through holes divided by partition walls and capable of taking a large filtration area per unit volume. For collecting fine particles of diesel vehicle exhaust gas, the cell density is 10 to 15 cells / cm 2 , and the total number of cells is 1500 to 2
500, partition wall thickness 0.3-0.5 mm, filtration area about 1.5
cm 2 is illustrated.
【0003】微粒子を捕集したハニカム構造体を再生す
るには、ハニカム構造体の全体あるいは一部に600℃
以上の高熱を加えて微粒子を着火し、燃焼除去する方式
が主に検討されており、捕集・再生を繰り返すことによ
り継続的に排ガスが処理される。この方式では、上記の
ような隔壁の厚さが極めて薄く、セル数の多いハニカム
構造体が、微粒子が燃焼する時の高温度に耐える性質
と、繰り返しの温度の変動に耐える性質が必要である。To regenerate a honeycomb structure in which fine particles are collected, the whole or a part of the honeycomb structure is heated to 600 ° C.
A method of igniting fine particles by applying the above high heat and burning and removing them is mainly studied, and exhaust gas is continuously treated by repeating collection and regeneration. In this method, the honeycomb structure having extremely thin partition walls and a large number of cells as described above is required to have a property of withstanding a high temperature when fine particles burn and a property of withstanding repeated temperature fluctuations. .
【0004】しかしながら、上記のような隔壁が薄く、
濾過面積の大きいハニカム構造体をピンホールなどの欠
陥を含まずに製造することは極めて困難であり、しかも
微粒子を燃焼させる際あるいは繰り返される温度の変動
の過程でハニカム構造体の隔壁に割れが生じ、捕集効率
が著しく低下するという生産性や信頼性に問題があっ
た。またフィルターを再生するにおいて、排ガスを流通
させて微粒子を捕集しながら再生する方式では、排ガス
温度が約150〜350℃と微粒子の燃焼可能温度より
もかなり低いために着火したとしても微粒子が燃え尽き
るまで燃焼を継続することができず、途中で失火すると
いう問題がある。このためフィルターを二系列設け、再
生時には一方のフィルターで捕集するといった、交互に
捕集と再生を繰り返す方式を採用せざるを得ないという
問題があり、微粒子捕集装置は全体として重装備で高価
になってしまうといった大きな問題がある。更にまた、
微粒子が異常に蓄積してフィルターが閉塞し、排ガスの
流路が遮断されるという非常時の対策も設備の中に取り
入れておく必要もあった。However, since the partition wall as described above is thin,
It is extremely difficult to manufacture a honeycomb structure with a large filtration area without containing defects such as pinholes, and moreover cracks occur in the partition walls of the honeycomb structure when burning fine particles or in the course of repeated temperature fluctuations. However, there was a problem in productivity and reliability that the collection efficiency was significantly reduced. Further, in the case of regenerating the filter, in the system in which exhaust gas is circulated to collect fine particles and regenerate, since the exhaust gas temperature is about 150 to 350 ° C., which is considerably lower than the combustible temperature of the fine particles, the fine particles burn out even if ignited. There is a problem that combustion cannot be continued up to this point and a fire is lost on the way. For this reason, there is a problem that it is necessary to adopt a method in which two filters are provided in series and one filter is used during regeneration, so that collection and regeneration are repeated alternately. There is a big problem that it becomes expensive. Furthermore,
It was also necessary to incorporate an emergency measure in the equipment, in which fine particles abnormally accumulated, the filter was blocked, and the exhaust gas flow path was blocked.
【0005】[0005]
【発明が解決しようとする課題】本発明はこれらの従来
技術の欠点を解決することを目的として、構造が簡単で
耐久性が高く、フィルターの再生に必要な電気容量も少
なくてすむ排ガス中の微粒子の捕集用フィルターを提供
するものである。SUMMARY OF THE INVENTION The present invention is intended to solve these drawbacks of the prior art, and has a simple structure, high durability, and low electric capacity required for filter regeneration. A filter for collecting fine particles is provided.
【0006】[0006]
【課題を解決するための手段】本発明は、外筒、該外筒
の中にあって開口部及び導電性濾過板の取り付け部を有
する積み重ね可能な複数の絶縁性支持体、該開口部の一
部を残して該絶縁性支持体に取り付けた導電性濾過板、
及び該導電性濾過板に取り付けた電極を含んで構成され
る排ガス中の微粒子捕集用フィルターであり、更に、絶
縁性支持体の導電性濾過板の取り付け部にて電極を導電
性濾過板に取り付けた微粒子捕集用フィルターである。SUMMARY OF THE INVENTION The present invention is directed to an outer cylinder, a plurality of stackable insulative supports having an opening in the outer cylinder and a mounting portion for a conductive filter plate, and a plurality of stackable insulating supports. A conductive filter plate attached to the insulating support, leaving a part
And a filter for collecting fine particles in exhaust gas, which is configured to include an electrode attached to the conductive filter plate, and further, the electrode is used as the conductive filter plate at the mounting portion of the conductive filter plate of the insulating support. It is an attached filter for collecting fine particles.
【0007】本発明においては、開口部及び導電性濾過
板の取り付け部を有する積み重ね可能な複数の絶縁性支
持体を使用する。絶縁性支持体の形状は特に限定する必
要はないが、例として示した図1のような角形の形状
や、図2のような円形の形状、楕円形の形状等が採用可
能である。ここで、絶縁性支持体の開口部(図中11、
21)とは、絶縁性支持体を外筒内に取り付けた状態で
排ガスの流れを遮蔽する絶縁性支持体材料が存在しない
排ガスが素通りできる部分を言い、好ましくは、図1、
2のように絶縁性支持体材料で囲まれた中に位置する。
この開口部に導電性濾過板をその開口部の一部を残して
遮蔽する状態で取り付ける。導電性濾過板の取り付け部
(図中12、22)とは、導電性濾過板と少なくとも3
mm以上の幅、好ましくは5〜30mmの幅で接触する
帯状の領域を意味し、好ましくは取り付け部に、導電性
濾過板の絶縁性支持体への固定手段としての、例えばボ
ルトとナットで導電性濾過板を絶縁性支持体に取り付け
るためのボルトを通す穴を有する。The present invention uses a plurality of stackable insulative supports having openings and attachments for conductive filter plates. The shape of the insulative support is not particularly limited, but a square shape as shown in FIG. 1, a circular shape as shown in FIG. Here, the opening of the insulating support (11 in the figure,
21) means a portion through which exhaust gas can pass without an insulating support material that blocks the flow of exhaust gas in a state where the insulating support is attached inside the outer cylinder, and preferably, FIG.
2 surrounded by an insulative support material.
A conductive filter plate is attached to this opening in a state of being shielded while leaving a part of the opening. The attachment part (12, 22 in the figure) of the conductive filter plate is at least 3 times the conductive filter plate.
It means a strip-shaped region in contact with a width of not less than mm, preferably a width of 5 to 30 mm, and is preferably electrically conductive by means of a bolt and a nut as means for fixing the electrically conductive filter plate to the insulative support at the mounting portion. It has a hole through which a bolt for attaching the filter plate to the insulating support is inserted.
【0008】また、積み重ね可能とは、二つ以上の絶縁
性支持体を構造的に積み重ねできることを意味し、絶縁
性支持体を外筒に固定する手段を特別に設けなくても二
つ以上の絶縁性支持体を外筒の中で積み重ねた状態が構
造体として安定であることを意味する。この意味におい
て、積み重ねる複数の絶縁性支持体は実質的に同じ形を
有し、積み重ねた状態で互いに接触する部分は出来るだ
け間隙がない状態で接触することが好ましく、接触する
部分は出来るだけ平坦であることが好ましい。絶縁性支
持体を排ガスの流れ方向から見た開口部を含む全体の面
積は特に限定する必要はないが、ディーゼル乗用車用で
は10〜2000cm2が適切であり、より適切には4
0〜700cm2である。排ガスの流れ方向から見た開
口部の面積はこの面積の50〜99%、好ましくは70
〜95%を占める。また、絶縁性支持体の高さは、特に
限定する必要はないが、5〜100mmが好ましく、よ
り好ましくは10〜50mmである。Stackable means that two or more insulative supports can be structurally stacked, and two or more insulative supports can be structurally stacked without special means for fixing the insulative supports to the outer cylinder. It means that the state in which the insulating supports are stacked in the outer cylinder is stable as a structure. In this sense, the plurality of insulating supports to be stacked have substantially the same shape, and it is preferable that the portions in contact with each other in the stacked state are in contact with each other with as little gap as possible, and the contact portions are as flat as possible. Is preferred. The total area including the opening of the insulating support as viewed from the flow direction of the exhaust gas is not particularly limited, but 10 to 2000 cm 2 is appropriate for diesel passenger cars, and more suitably 4
It is 0 to 700 cm 2 . The area of the opening viewed from the flow direction of the exhaust gas is 50 to 99% of this area, preferably 70
Occupy ~ 95%. The height of the insulating support is not particularly limited, but is preferably 5 to 100 mm, more preferably 10 to 50 mm.
【0009】また、絶縁性支持体の材質は特に限定する
必要はないが、アルミナ、ムライト、コージエライト、
石英、窒化ケイ素、窒化ホウ素、各種耐熱ガラス等より
広範囲に選択でき、これらの成型焼結体等が好適に使用
できる。The material of the insulating support is not particularly limited, but may be alumina, mullite, cordierite,
A wide range can be selected from quartz, silicon nitride, boron nitride, various heat resistant glasses, etc., and molded sintered bodies of these can be preferably used.
【0010】本発明に使用する導電性濾過板は、これを
通電することによって少なくとも550℃以上、好まし
くは650℃以上に加熱できる性質が必要である。ま
た、導電性濾過板の表裏面間に圧力差があれば、気体は
導電性濾過板を貫通して通過させるが微粒子は捕獲でき
る性質が必要である。このような性質を有する導電性濾
過板は、ニッケル、クロム、鉄、アルミニウム、コバル
トなどより製造される導電性耐熱合金の多孔体や、二ケ
イ化モリブデン、二ケイ化タングステン、ジルコニア、
炭化ケイ素、炭化ホウ素、ランタンクロマイトなどの導
電性セラミックスの多孔体より形成することができ、気
孔率は少なくとも20%以上、好ましくは30〜80
%、平均細孔径は少なくとも0.1μm以上、好ましく
は1〜100μm、更に好ましくは10〜60μmを有
する多孔体より形成される。導電性濾過板の形状は特に
限定する必要はないが、絶縁性支持体の形状に合わせて
四角状、円状、楕円状などの広い範囲より選定される。
導電性濾過板の大きさは処理する排ガスの量によっても
異なるが、上記の絶縁性支持体の開口部の面積の少なく
とも30%以上、好ましくは60〜98%を覆う面積の
大きさとする。即ち、絶縁性支持体の開口部の排ガスの
流れ方向から見た面積を少なくとも70%未満、好まし
くは2〜40%残す大きさとする。排ガスの流れ方向か
ら見た適切な片側面積は約10〜1500cm2、好ま
しくは約30〜600cm2である。また、導電性濾過
板の厚みは空隙率や強度により選定されるが、0.1〜
5mmが好ましい。The conductive filter plate used in the present invention is required to have the property of being heated to at least 550 ° C. or higher, preferably 650 ° C. or higher by energizing it. In addition, if there is a pressure difference between the front and back surfaces of the conductive filter plate, the gas must pass through the conductive filter plate and pass through, but must have the property of trapping fine particles. The conductive filter plate having such properties, nickel, chromium, iron, aluminum, a porous body of a conductive heat-resistant alloy produced from cobalt, molybdenum disilicide, tungsten disilicide, zirconia,
It can be formed from a porous body of a conductive ceramic such as silicon carbide, boron carbide or lanthanum chromite, and has a porosity of at least 20% or more, preferably 30 to 80.
%, The average pore diameter is at least 0.1 μm or more, preferably 1 to 100 μm, and more preferably 10 to 60 μm. The shape of the conductive filter plate is not particularly limited, but it is selected from a wide range such as a square shape, a circular shape, an elliptical shape or the like according to the shape of the insulating support.
Although the size of the conductive filter plate varies depending on the amount of exhaust gas to be treated, the size of the conductive filter plate is at least 30% or more, preferably 60 to 98% of the area of the opening of the insulating support. That is, the area of the opening of the insulating support viewed from the flow direction of the exhaust gas is at least less than 70%, preferably 2 to 40%. A suitable one-sided area viewed from the flow direction of the exhaust gas is about 10 to 1500 cm 2 , preferably about 30 to 600 cm 2 . The thickness of the conductive filter plate is selected depending on the porosity and strength,
5 mm is preferable.
【0011】絶縁性支持体の開口部に導電性濾過板を取
り付けた状態で一部として残す開口部(例、図中33、
53)の位置は、濾過板の中央部、縁部等の任意の位置
させてよいが、絶縁性支持体に導電性濾過板を取り付け
た状態で積み重ねるにおいては、開口部が排ガスの流れ
方向に重ならないように、例えば90度、180度等回
転して積み重ねることが、微粒子の捕集効率の面から好
ましい。An opening left as a part of the state where the conductive filter plate is attached to the opening of the insulating support (eg, 33 in the figure,
The position of 53) may be any position such as the central portion and the edge of the filter plate. However, when stacking with the conductive filter plate attached to the insulating support, the opening is in the exhaust gas flow direction. It is preferable from the viewpoint of the collection efficiency of fine particles that they are stacked by rotating, for example, 90 degrees or 180 degrees so that they do not overlap.
【0012】絶縁性支持体に取り付けた導電性濾過板の
枚数は、達成すべき捕集効率と排ガスの圧力損失を配慮
して選定されるが、通常3〜300枚、より適切には5
〜50枚である。The number of conductive filter plates attached to the insulating support is selected in consideration of the collection efficiency to be achieved and the pressure loss of exhaust gas, but is usually 3 to 300, and more suitably 5
~ 50 sheets.
【0013】各々の導電性濾過板には通電加熱用の電極
を少なくとも二箇所取り付ける必要があるが、ここで電
極を導電性濾過板に取り付けるにおいて、絶縁性支持体
の導電性濾過板取り付け部に電極を取り付ける方式、即
ち、導電性濾過板と電極とを絶縁性支持体の導電性濾過
板取り付け部にて重ねた伏態で、例えばボルトとナット
で絶縁性支持体に一体に取り付ける方式が、フィルター
の構造の安定性及び製作の容易性から好ましい。電極に
は電源からの通電用のリード線を接続する。このリード
線は、一例として、外筒に設けた各々の電極用の穴を通
過させて電源より電極に導く。It is necessary to attach at least two electrodes for electric heating to each conductive filter plate. Here, when attaching the electrodes to the conductive filter plate, the electrodes are attached to the conductive filter plate mounting portion of the insulating support. A method of attaching electrodes, that is, a method of integrally mounting the conductive filter plate and the electrode on the insulating support body with bolts and nuts in a state of being superposed at the conductive filter plate mounting portion of the insulating support body, It is preferable because of the stability of the structure of the filter and the ease of manufacturing. Lead wires for energization from a power source are connected to the electrodes. As an example, the lead wires pass through the respective electrode holes provided in the outer cylinder and are guided to the electrodes from the power supply.
【0014】本発明のフィルターの組立ては、例えば、
導電性濾過板と電極を取り付た絶縁性支持体を外筒内に
配置して電極にリード線を接続し、次に導電性濾過板と
電極を取り付た絶縁性支持体を積み重ねて電極にリード
線を接続する、といった手順を所定の枚数繰り返すこと
によって行なうことができる。The filter of the present invention can be assembled, for example, by
Place the insulating support with the conductive filter plate and the electrode inside the outer cylinder, connect the lead wire to the electrode, and then stack the insulating support with the conductive filter plate and the electrode on top of the electrode. It can be performed by repeating a predetermined number of steps such as connecting a lead wire to.
【0015】[0015]
【作用】本発明の微粒子捕集用フィルターは、一部を残
して導電性濾過板で遮断した流路を排ガスが流れる過程
で生じる濾過板の表裏面間の圧力差を利用して、一部の
排ガス中の微粒子を捕集する操作を連続して複数回繰り
返す方式によって高い捕集率を達成するに適切なフィル
ターであり、各々の導電性濾過板に電極を取り付けるこ
とによって各々の導電性濾過板を独立して加熱再生でき
るフィルターである。The filter for collecting fine particles of the present invention partially uses the pressure difference between the front and back surfaces of the filter plate generated in the process of the exhaust gas flowing through the flow path blocked by the conductive filter plate while leaving a part of the filter. It is a filter suitable for achieving a high collection rate by repeating the operation of collecting fine particles in the exhaust gas of a plurality of times continuously, and by attaching electrodes to each conductive filtration plate, each conductive filtration It is a filter that can heat and regenerate the plate independently.
【0016】従って、この方式において各々の導電性濾
過板は、他の導電性濾過板や外筒との間で実質的に電気
的な導通がない状態で配置される必要がある。更に、導
電性濾過板は、走行するディーゼル車に搭載された状態
で構造的に安定であるように外筒内に配置される必要が
ある。本発明はこの課題に対し、導電性濾過板の取り付
け部を設けた絶縁性支持体に導電性濾過板を取り付ける
ことによって、外筒や他の導電性濾過板との実質的な絶
縁を達成し、更に、この絶縁性支持体を積み重ね可能な
構造とすることにより構造的な安定性を達成するもので
ある。即ち、外筒内で積み重ね可能であり、したがって
外筒内で実質的に構造が安定である絶縁性支持体に各々
の導電性濾過板を取り付けて外筒内に配置することによ
り、導電性濾過板の外筒及び他の導電性濾過板との非接
触が保証され、絶縁性支持体が外筒内で実質的に構造が
安定であるために、絶縁性支持体、導電性濾過板及びそ
れに取り付ける電極を全体として安定な構造体とするこ
とができる。Therefore, in this system, each conductive filter plate needs to be arranged in a state where there is substantially no electrical connection with other conductive filter plates or outer cylinders. Further, the conductive filter plate needs to be arranged in the outer cylinder so as to be structurally stable when mounted on a traveling diesel vehicle. To solve this problem, the present invention achieves substantial insulation from the outer cylinder and other conductive filter plates by attaching the conductive filter plate to the insulating support provided with the mounting portion of the conductive filter plate. Furthermore, structural stability is achieved by making this insulating support a stackable structure. That is, by mounting each conductive filter plate on an insulative support that can be stacked in the outer cylinder and therefore has a substantially stable structure in the outer cylinder and dispose in the outer cylinder, conductive filtration is performed. The non-contact between the outer casing of the plate and the other conductive filter plate is ensured, and the insulating support is substantially structurally stable in the outer casing. The attached electrode can be a stable structure as a whole.
【0017】以下、実施例によって本発明を具体的に説
明する。The present invention will be specifically described below with reference to examples.
実施例1 絶縁性支持体として図1のような形状の角型のアルミナ
質焼結体、平板状の導電性濾過板、電極をフィルターの
部材として用い、これらを図3のように組み立てた。絶
縁性支持体31の寸法は11cm×11cm×高さ3c
mで、肉厚は3mmであった。絶縁性支持体の開口部は
排ガスの流れ方向から見た絶縁性支持体の中央に位置
し、寸法は10cm×10cmで、その周囲に7mmの
幅の導電性濾過板の取り付け部32を有した。またこの
導電性濾過板の取り付け部の幅の中央に直径2mmの取
り付け用の穴を8mmの間隔で設けた。アルミナ質焼結
体31の密度は3.85g/cm3で理論密度の97%
であった。Example 1 As an insulating support, a rectangular alumina sintered body having a shape as shown in FIG. 1, a flat conductive filter plate, and an electrode were used as a filter member, and these were assembled as shown in FIG. The size of the insulating support 31 is 11 cm × 11 cm × height 3 c
m, the wall thickness was 3 mm. The opening of the insulative support was located in the center of the insulative support as viewed from the direction of exhaust gas flow, had a size of 10 cm × 10 cm, and had a conductive filter plate mounting portion 32 with a width of 7 mm around it. . Further, mounting holes having a diameter of 2 mm were provided at intervals of 8 mm at the center of the width of the mounting portion of the conductive filter plate. The density of the alumina sintered body 31 is 3.85 g / cm 3, which is 97% of the theoretical density.
Met.
【0018】導電性濾過板34として10.6cm×8
cm×肉厚2mmの炭化ケイ素質多孔体を用いた。炭化
ケイ素質多孔体は密度が1.54g/cm3で気孔率は
52%であり、平均細孔径は28μmであった。この導
電性濾過板を図3に示した状態で絶縁性支持体に配置
し、絶縁性支持体の取り付け部32の取り付け用の穴の
位置に合わせて導電性濾過板34に穴を設け、この穴に
耐熱ステンレス合金製のボルトを通してボルトとナット
で一体に固定した。また電極35には幅3mm、長さ8
cm、肉厚1mmの耐熱ステンレス合金を用い、図3の
ように導電性濾過板に重ねた状態で2箇所に配置し、絶
縁性支持体と一体にボルトとナットで固定した。絶縁性
支持体に導電性濾過板と電極を取り付けた状態で、導電
性濾過板に遮蔽されない絶縁性支持体の開口部33は2
cm×10cmであった。10.6 cm × 8 as the conductive filter plate 34
A silicon carbide based porous material having a size of cm × 2 mm in thickness was used. The silicon carbide based porous material had a density of 1.54 g / cm 3 , a porosity of 52% and an average pore diameter of 28 μm. This conductive filter plate is arranged on the insulating support in the state shown in FIG. 3, and holes are provided in the conductive filter plate 34 in accordance with the positions of the mounting holes of the mounting portion 32 of the insulating support. A bolt made of heat-resistant stainless alloy was passed through the hole and fixed integrally with the bolt and nut. The electrode 35 has a width of 3 mm and a length of 8
A heat-resistant stainless alloy having a thickness of 1 cm and a thickness of 1 mm was placed on the conductive filter plate at two positions as shown in FIG. 3, and fixed with bolts and nuts integrally with the insulating support. With the conductive filter plate and the electrode attached to the insulating support, the opening 33 of the insulating support which is not shielded by the conductive filter plate is 2
It was cm × 10 cm.
【0019】このようにして絶縁性支持体に導電性濾過
板と電極を取り付けたものを15組用意し、内側寸法が
11.1cm×11.1cm、肉厚が2mm、長さが5
0cmの四角柱状のスチール管41の中に開口部が重な
らないように一つづつ180度回転させて図4のように
重ねて配置した。各々の電極にはスチール管を貫通して
通電用のリード線を取り付けた。スチール管の貫通孔の
周囲にはリード線とスチール管との導通を防ぐために絶
縁材を配置した。In this way, 15 sets of insulating supports to which conductive filter plates and electrodes were attached were prepared, and the inner dimensions were 11.1 cm × 11.1 cm, the wall thickness was 2 mm, and the length was 5 mm.
The steel tube 41 having a rectangular column shape of 0 cm was rotated by 180 degrees one by one so that the openings would not overlap with each other, and the tubes were stacked as shown in FIG. A lead wire for energization was attached to each electrode through the steel tube. An insulating material was placed around the through-hole of the steel tube to prevent conduction between the lead wire and the steel tube.
【0020】このようにして構成したフィルターを排気
量2500ccのディーゼルエンジンを搭載した自動車
に設置し、排ガスをフィルターに導いて100時間の実
走行条件下で微粒子捕集試験を行った。走行は約50k
m/hの速度とし、排ガスをフィルターに導きながら導
電性濾過板の一枚毎に順次1kwの電力を10分間供給
して間欠的にフィルターを加熱再生した。フィルターの
前及び後の両方には排ガス中の微粒子濃度を測定するス
モークメーター及び圧力計を設置し、連続的に測定し
た。結果として、フィルターによる微粒子の捕集率は8
3〜88%で、フィルターにおける圧力損失は0.53
〜0.57kg/cm2であり、引き続き微粒子の捕集
を継続するに障害となるような問題は観られなかった。The filter thus constructed was installed in an automobile equipped with a diesel engine having a displacement of 2500 cc, the exhaust gas was guided to the filter, and a particulate collection test was conducted under an actual running condition for 100 hours. Run about 50k
The speed was set to m / h, and an electric power of 1 kw was sequentially supplied to each of the conductive filter plates for 10 minutes while guiding the exhaust gas to the filter to intermittently heat and regenerate the filter. A smoke meter and a pressure gauge for measuring the concentration of fine particles in the exhaust gas were installed both before and after the filter, and continuous measurement was performed. As a result, the collection rate of fine particles by the filter is 8
3 to 88%, the pressure loss in the filter is 0.53
It was ˜0.57 kg / cm 2 , and no problem that hinders continuous collection of fine particles was observed.
【0021】実施例2 絶縁性支持体として図2のような形状の丸型のムライト
質焼結体51、切り欠き円板状の導電性濾過板54、電
極55をフィルターの部材として用い、これらを図5の
ように組み立てた。絶縁性支持体の寸法は直径12c
m、高さ3cmで、肉厚は2mmであった。絶縁性支持
体の開口部は排ガスの流れ方向から見た絶縁性支持体の
中央に位置し、寸法は直径10cmで、その周囲に8m
mの幅の導電性濾過板の取り付け部52を有した。また
この導電性濾過板の取り付け部52の幅の中央に直径2
mmの取り付け用の穴を8mmの間隔で設けた。ムライ
ト質焼結体51の密度は2.88g/cm3で理論密度
の95%であった。Example 2 A circular mullite sintered body 51 having a shape as shown in FIG. 2 as an insulating support, a notched disk-shaped conductive filter plate 54, and an electrode 55 were used as members of a filter. Was assembled as shown in FIG. The diameter of the insulating support is 12c
m, the height was 3 cm, and the wall thickness was 2 mm. The opening of the insulative support is located in the center of the insulative support as seen from the flow direction of the exhaust gas, and has a diameter of 10 cm and a circumference of 8 m.
It had a conductive filter plate mounting portion 52 of m width. In addition, a diameter of 2 mm is provided at the center of the width of the mounting portion 52 of the conductive filter plate.
mm mounting holes were provided at 8 mm intervals. The density of the mullite sintered body 51 was 2.88 g / cm 3 , which was 95% of the theoretical density.
【0022】導電性濾過板54として直径11.4c
m、最小幅6.4cm(図5のように幅2.5cmの切
り欠きが2か所ある)、肉厚1.5mmの二ケイ化モリ
ブデン質多孔体(気孔率46%、平均細孔径37μm)
を用いた。この導電性濾過板を図5に示した状態で絶縁
性支持体に配置し、実施例1と同様にして耐熱ステンレ
ス合金製のボルトとナットで一体に固定した。また電極
55には幅5mm、肉厚1mmの円弧状の耐熱ステンレ
ス合金を用い、図5のように導電性濾過板の取り付け部
で導電性濾過板に重ねた状態で2箇所に配置し、絶縁性
支持体と一体にボルトとナットで固定した。絶縁性支持
体に導電性濾過板と電極を取り付けた状態で、導電性濾
過板に遮蔽されない絶縁性支持体の開口部53は円の中
心方向の最大幅が1.8cmであった。Diameter 11.4c as the conductive filter plate 54
m, minimum width 6.4 cm (there are two notches with a width of 2.5 cm as shown in FIG. 5), and a thickness of 1.5 mm of molybdenum disilicide porous body (porosity 46%, average pore diameter 37 μm). )
Was used. This conductive filter plate was placed on the insulating support in the state shown in FIG. 5, and fixed in the same manner as in Example 1 by using bolts and nuts made of heat-resistant stainless alloy. Further, an arc-shaped heat-resistant stainless alloy having a width of 5 mm and a wall thickness of 1 mm is used for the electrode 55, and the electrodes are arranged at two positions in a state of being overlapped with the conductive filter plate at the mounting portion of the conductive filter plate as shown in FIG. It was fixed with bolts and nuts integrally with the flexible support. With the conductive filter plate and the electrodes attached to the insulating support, the maximum width in the center direction of the circle of the opening 53 of the insulating support not shielded by the conductive filter plate was 1.8 cm.
【0023】このようにして絶縁性支持体に導電性濾過
板と電極を取り付けたものを20組用意し、内径12.
2cm、肉厚2mm、長さが70cmの円筒状のスチー
ル管の中に開口部が重ならないように一つづつ90度回
転させて配置した。各々の電極にはスチール管を貫通し
て通電用のリード線を取り付けた。スチール管の貫通孔
の周囲にはリード線とスチール管との導通を防ぐために
絶縁材を配置した。このようにして構成したフィルター
を実施例1と同様にしてディーゼルエンジンを搭載した
自動車に設置し、100時間の実走行条件下で微粒子捕
集試験を行った。排ガスをフィルターに導きながら導電
性濾過板の一枚毎に順次1kwの電力を10分間供給し
て間欠的にフィルターを加熱再生した。フィルターの前
及び後の両方には排ガス中の微粒子濃度を測定するスモ
ークメーター及び圧力計を設置し、連続的に測定した。In this way, 20 sets of the electrically insulating supports to which the conductive filter plate and the electrodes are attached are prepared.
It was placed in a cylindrical steel tube having a length of 2 cm, a wall thickness of 2 mm, and a length of 70 cm, rotating 90 degrees one by one so that the openings would not overlap. A lead wire for energization was attached to each electrode through the steel tube. An insulating material was placed around the through-hole of the steel tube to prevent conduction between the lead wire and the steel tube. The filter thus constructed was installed in a vehicle equipped with a diesel engine in the same manner as in Example 1, and a particulate collection test was conducted under actual running conditions for 100 hours. While guiding the exhaust gas to the filter, electric power of 1 kw was sequentially supplied to each conductive filter plate for 10 minutes to intermittently heat and regenerate the filter. A smoke meter and a pressure gauge for measuring the concentration of fine particles in the exhaust gas were installed both before and after the filter, and continuous measurement was performed.
【0024】結果として、フィルターによる微粒子の捕
集率は88〜91%で、フィルターにおける圧力損失は
0.57〜0.61kg/cm2であり、引き続き微粒
子の捕集を継続するに障害となるような問題は観られな
かった。As a result, the collection rate of fine particles by the filter is 88 to 91%, and the pressure loss in the filter is 0.57 to 0.61 kg / cm 2, which is an obstacle to continuing the collection of fine particles. No such problem was seen.
【0025】[0025]
【発明の効果】開口部及び導電性濾過板の取り付け部を
有する積み重ね可能な複数の絶縁性支持体を使用するこ
とにより、構造的に安定で、導電性濾過板の電気的な独
立性の信頼性が高いフィルターを提供できる。EFFECT OF THE INVENTION By using a plurality of stackable insulative supports having an opening and a mounting part of the conductive filter plate, structurally stable and reliable electrical independence of the conductive filter plate is obtained. A highly efficient filter can be provided.
【図1】絶縁性支持体の構造の一例を示す略図である。FIG. 1 is a schematic view showing an example of the structure of an insulating support.
【図2】絶縁性支持体の構造の一例を示す略図である。FIG. 2 is a schematic view showing an example of the structure of an insulating support.
【図3】絶縁性支持体に導電性濾過板と電極を取り付け
た状態を示す略図である。FIG. 3 is a schematic view showing a state in which a conductive filter plate and electrodes are attached to an insulating support.
【図4】排ガスの流れに平行な方向のフィルターの断面
の略図である。FIG. 4 is a schematic view of a cross section of a filter in a direction parallel to the flow of exhaust gas.
【図5】絶縁性支持体に導電性濾過板と電極を取り付け
た状態を示す略図である。FIG. 5 is a schematic view showing a state in which a conductive filter plate and electrodes are attached to an insulating support.
11…絶縁性支持体開口部 12…導電性濾過板の取り付け部 34…導電性濾過板 35…電極 41…スチール管 11 ... Insulating support opening 12 ... Attachment part of conductive filter plate 34 ... Conductive filter plate 35 ... Electrode 41 ... Steel tube
─────────────────────────────────────────────────────
─────────────────────────────────────────────────── ───
【手続補正書】[Procedure amendment]
【提出日】平成5年9月21日[Submission date] September 21, 1993
【手続補正1】[Procedure Amendment 1]
【補正対象書類名】明細書[Document name to be amended] Statement
【補正対象項目名】特許請求の範囲[Name of item to be amended] Claims
【補正方法】変更[Correction method] Change
【補正内容】[Correction content]
【特許請求の範囲】[Claims]
【手続補正2】[Procedure Amendment 2]
【補正対象書類名】明細書[Document name to be amended] Statement
【補正対象項目名】0001[Correction target item name] 0001
【補正方法】変更[Correction method] Change
【補正内容】[Correction content]
【0001】[0001]
【産業上の利用分野】ディーゼル車等から排出されるガ
スはスス状の炭素質の微粒子(以下「微粒子」と略称)
を含んでおり、この低減が地球環境問題における早期に
解決すべき重要な課題の1つとなっている。本発明は、
これらディーゼルエンジン等の内燃機関から排出される
ガスに含まれる微粒子を除去するためのフィルターに関
する。[Industrial application] Gas emitted from diesel vehicles is soot-like carbonaceous fine particles (hereinafter abbreviated as "fine particles")
This is one of the important issues to be solved at an early stage in global environmental problems. The present invention is
The present invention relates to a filter for removing fine particles contained in gas discharged from an internal combustion engine such as a diesel engine.
【手続補正3】[Procedure 3]
【補正対象書類名】明細書[Document name to be amended] Statement
【補正対象項目名】0002[Name of item to be corrected] 0002
【補正方法】変更[Correction method] Change
【補正内容】[Correction content]
【0002】[0002]
【従来の技術】従来、ディーゼルエンジン車から排出さ
れるガス中の微粒子を捕集するフィルターとしては、セ
ラミックス製のハニカム構造体が主として検討されてい
る(特開昭57−7216)。ここでハニカム構造体と
は、隔壁により区分され、一方の端部が交互の位置関係
において閉じた多数のセルを有し、単位容積あたりに濾
過面積を多くとることができる構造体である。ディーゼ
ル車排ガスの微粒子捕集用としては、セル密度が10〜
15セル/cm2、総セル数1500〜2500、隔壁
厚0.3〜0.5mm、濾過面積約1.5m2 が例示さ
れている。2. Description of the Related Art Conventionally, a ceramic honeycomb structure has been mainly studied as a filter for collecting fine particles in a gas discharged from a diesel engine vehicle (Japanese Patent Laid-Open No. 57-7216). Here, the honeycomb structure is divided by partition walls, and one end portion has an alternating positional relationship.
It is a structure that has a large number of closed cells and can have a large filtration area per unit volume. For collecting fine particles of exhaust gas from diesel vehicles, the cell density is 10
15 cells / cm 2 , total number of cells 1500 to 2500, partition wall thickness 0.3 to 0.5 mm, and filtration area of about 1.5 m 2 are exemplified.
【手続補正4】[Procedure amendment 4]
【補正対象書類名】明細書[Document name to be amended] Statement
【補正対象項目名】0009[Correction target item name] 0009
【補正方法】変更[Correction method] Change
【補正内容】[Correction content]
【0009】また、絶縁性支持体の材質は特に限定する
必要はないが、アルミナ、ムライト、コージェライト、
石英、窒化ケイ素、窒化ホウ素、各種耐熱ガラス等より
広範囲に選択でき、これらの成形焼結体等が好適に使用
できる。また、金属に絶縁性セラミック材料等を溶射し
た材料とするか、或いは支持体と導電性濾過板との接触
部分に絶縁性のパッキン等を介在させて支持体の実質的
な絶縁性を確保した構造も採用可能である。 The material of the insulating support is not particularly limited, but may be alumina, mullite, cordierite,
A wide range of materials can be selected from quartz, silicon nitride, boron nitride, various heat resistant glasses, etc., and molded sintered bodies thereof can be preferably used. Also, spray an insulating ceramic material onto the metal.
Material, or contact between the support and the conductive filter plate
Insulating packing etc. is interposed in the part
It is also possible to adopt a structure that ensures sufficient insulation.
【手続補正5】[Procedure Amendment 5]
【補正対象書類名】明細書[Document name to be amended] Statement
【補正対象項目名】0011[Correction target item name] 0011
【補正方法】変更[Correction method] Change
【補正内容】[Correction content]
【0011】絶縁性支持体の開口部に導電性濾過板を取
り付けた状態で一部として残す開口部(例、図中33、
53)の位置は、濾過板の中央部、縁部等の任意の位置
であってよいが、絶縁性支持体に導電性濾過板を取り付
けた状態で積み重ねるにおいては、開口部が排ガスの流
れ方向に重ならないように、例えば90度、180度等
回転して積み重ねることが、微粒子の捕集効率の面から
好ましい。An opening left as a part of the state where the conductive filter plate is attached to the opening of the insulating support (eg, 33 in the figure,
The position of 53) is an arbitrary position such as the central part and the edge of the filter plate.
May be at, but in stacking in a state of mounting a conductive filtration plate insulating support, so that the opening does not overlap in the flow direction of the exhaust gas, for example 90 degrees, be stacked rotated 180 degrees such It is preferable from the viewpoint of the collection efficiency of fine particles.
Claims (2)
電性濾過板の取り付け部を有する積み重ね可能な複数の
絶縁性支持体、該間口部の一部を残して該絶縁性支持体
に取り付けた導電性濾過板、及び該導電性濾過板に取り
付けた電極を含んで構成される排ガス中の微粒子捕集用
フィルター。1. An outer cylinder, a plurality of stackable insulative supports having an opening and an attachment portion of a conductive filter plate in the outer cylinder, and the insulating property with a part of the front opening left. A filter for collecting fine particles in exhaust gas, comprising a conductive filter plate attached to a support and an electrode attached to the conductive filter plate.
部にて電極を導電性濾過板に取り付けた請求項1記載の
フィルター。2. The filter according to claim 1, wherein the electrode is attached to the conductive filter plate at a portion of the insulating support where the conductive filter plate is attached.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5136381A JPH06317140A (en) | 1993-04-30 | 1993-04-30 | Filter for collecting particulate in exhaust gas |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5136381A JPH06317140A (en) | 1993-04-30 | 1993-04-30 | Filter for collecting particulate in exhaust gas |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH06317140A true JPH06317140A (en) | 1994-11-15 |
Family
ID=15173829
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP5136381A Pending JPH06317140A (en) | 1993-04-30 | 1993-04-30 | Filter for collecting particulate in exhaust gas |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH06317140A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2020179223A1 (en) * | 2019-03-05 | 2020-09-10 | 株式会社デンソー | Electrode-equipped honeycomb substrate |
-
1993
- 1993-04-30 JP JP5136381A patent/JPH06317140A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2020179223A1 (en) * | 2019-03-05 | 2020-09-10 | 株式会社デンソー | Electrode-equipped honeycomb substrate |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP0559907B1 (en) | Self-heating filter | |
CN113825893B (en) | Vehicle exhaust gas purification device, corresponding production method, exhaust line and vehicle | |
EP0606071B1 (en) | Particulate trap | |
WO1995002117A1 (en) | Regenerable diesel exhaust filter and heater | |
US4054417A (en) | Regenerative-filter-incinerator device | |
KR20070087121A (en) | Exhaust gas purification apparatus | |
EP0879939B1 (en) | Exhaust gas purifier | |
JPH0211287B2 (en) | ||
JP2590943Y2 (en) | Exhaust gas purification device | |
EP0504422B1 (en) | Self-heating filter | |
JPH06317140A (en) | Filter for collecting particulate in exhaust gas | |
JPS6239247B2 (en) | ||
JPH08243333A (en) | Particulate trap for diesel engine | |
CN100419227C (en) | Composite filtering-regeneration device for particulates in exhaust gas from diesel vehicle | |
JPH0754631A (en) | Filter for collecting minute particle in exhaust gas | |
JPH06193430A (en) | Collecting method of particulate in exhaust gas and filter | |
JPH07136435A (en) | Filter for exhaust gas purifying apparatus and production thereof | |
JPH0610649A (en) | Filter for exhaust gas emission control | |
JPH05345110A (en) | Filter for purifying waste gas | |
JPH05312018A (en) | Filter for purifying exhaust gas | |
JPS60111014A (en) | Purifying device collecting fine particle | |
JPH06129228A (en) | Method and trapping micro particle in exhaust gas and filter therefor | |
JPH062526A (en) | Filter for purifying exhaust gas | |
JPH08100630A (en) | Spherical electric conductor charging type particulate collecting filter | |
JPH06193431A (en) | Collecting method of particulate in exhaust gas and filter |