JPS58177118A - Preparation of diesel particulate filter - Google Patents
Preparation of diesel particulate filterInfo
- Publication number
- JPS58177118A JPS58177118A JP57060483A JP6048382A JPS58177118A JP S58177118 A JPS58177118 A JP S58177118A JP 57060483 A JP57060483 A JP 57060483A JP 6048382 A JP6048382 A JP 6048382A JP S58177118 A JPS58177118 A JP S58177118A
- Authority
- JP
- Japan
- Prior art keywords
- filter
- catalyst
- filter carrier
- carrier
- masking material
- 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)
- Filtering Materials (AREA)
Abstract
Description
【発明の詳細な説明】
ゼルエンジン、からの排出ガス中に含まれるパティキエ
レー)(9粒子)の捕集用フィルタの製造方法に関する
ものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing a filter for collecting Patikiere (9 particles) contained in exhaust gas from a diesel engine.
上記微粒子は主としてカーボン、炭化水素および金属か
らなり、炭化水素燃料の不完全燃焼などによって発生す
る。この微粒子は大気中に放出されると、環境衛生上な
いし環境保全上好ましくないため、従来よりこの微粒子
を除去又は排出蓋を最少にするため種々の技術が提案さ
れており、その一つにフィルタによる処理がある。この
フィルタによる処理は、微粒子をアルミナ等からなる無
機質多孔体のフィルタの空孔内に捕捉することによって
行うが、使用するlこしたがって微粒子が過度にフィル
タ内に蓄積してしまい、フィルタが容易に飽和又は動作
不能になってしまっていた〇
そのため、微粒子が過度番こフィルタ内に蓄積しないよ
うに又は過度に蓄積した微粒子を除去するために、種々
の触媒又は燃焼手段を用いて微粒子を燃焼除去する提案
もなされている。しかしながら、この微粒子の燃焼除去
技術も未だ充分なものではなく、しばしば微粒子量不足
による層火不良などの問題が生じていた。The fine particles are mainly composed of carbon, hydrocarbons, and metals, and are generated due to incomplete combustion of hydrocarbon fuel. When these particulates are released into the atmosphere, they are undesirable in terms of environmental hygiene and conservation. Therefore, various techniques have been proposed to remove these particulates or minimize the need for discharge lids, one of which is the use of filters. There is processing by Treatment with this filter is carried out by trapping particulates in the pores of the filter, which is made of an inorganic porous material such as alumina. It has become saturated or inoperable. Therefore, in order to prevent or remove excessively accumulated particulates, various catalysts or combustion means are used to burn off the particulates. There have also been proposals to do so. However, this technology for removing fine particles by combustion is still not sufficient, and problems such as poor bed firing often occur due to insufficient amount of fine particles.
本発明の目的は、排出ガス中の微粒子の燃焼除去におけ
る上記間趙点を解決し、微粒子の看火・燃焼を容易にし
たディーゼルパティキーレート捕集用フィルタの製造方
法を提供することにある0
本発明の方法により製造されるディーゼル/くティキュ
レート捕集用フィルタは、その一部分のみ触媒作用を有
しないことを特徴とするO本発明の方法は、フィルタ担
体の一部分を適当な材料でマスキングしたのち触媒を担
持させるか、或いはフィルタ担体に触媒を担持させたの
ち一部分を適当な材料でマスキングすることからなる0
即ち、本発明の第1の方法は、触媒を担持させたくない
フィルタ担体の部分を、熱で溶融除去又は脱燐可能な物
質よりなるマスキング材、例えばワックス、樹脂、低融
点金属等、でマスキングした後、このフィルタ担体に触
媒を担持せしめ、次いで該マスキング材を除去すること
を特徴とする〇
本発明の第2の方法は、フィルタ担体全体に触媒を担持
せしめた後、触媒作用を持たせたくないフィルタ担体部
分を無機物質でマスキングすることを特徴とする。An object of the present invention is to provide a method for manufacturing a filter for collecting diesel particulate matter that solves the above-mentioned problems in the combustion removal of particulates in exhaust gas and facilitates the ignition and combustion of particulates. 0 The diesel/citrate collecting filter produced by the method of the present invention is characterized in that only a portion thereof does not have a catalytic action. In other words, the first method of the present invention consists of supporting a catalyst on the filter carrier, or masking a portion of the filter carrier with an appropriate material after supporting the catalyst on the filter carrier. After masking the part with a masking material made of a substance that can be melted away or dephosphorized with heat, such as wax, resin, low melting point metal, etc., the catalyst is supported on the filter carrier, and then the masking material is removed. A second method of the present invention is characterized in that after a catalyst is supported on the entire filter carrier, the portion of the filter carrier that is not desired to have a catalytic action is masked with an inorganic substance.
本発明の方法に使用し得るフィルタ担体は、微粒子捕集
用に使用されるものがそのまま使用できる。フィルタ担
体には、例えば連続気泡型のポリウレタンフォームなど
の発泡プラスチ・Iり体にアルミナスラ11−等を塗布
したのち、焼成することによって得られる多孔質スケル
トンが挙けられる。この他、アルミナの粒体からなる円
柱状、!・ニカム状の焼結体が使用できるO本発明の第
1の方法において使用し得るマスキング材は、熱で溶融
除去又は脱燐可能な物質であれば使用できるが、触媒担
持の際の熱処理温度又はフィルタ使用時の温度で熱溶融
ないしは消失するものがよい。このようなものとしては
ワヴクス;ポリエチレン等のポリオレフィン樹脂、ビニ
ル樹脂など線状ポリマー:および鉛、はんだ合金等の低
融点金属゛又は合金が例示できる。マスキングした後触
媒担持箪にフィルタ担1
体を浸漬した際に撥水性によってマスキングを充分なら
しめ、且つ低温溶融除去ないしは消失させることができ
ることから、ワックス、ポリオレフィン等が好ましい。As the filter carrier that can be used in the method of the present invention, those used for collecting particulates can be used as they are. Examples of the filter carrier include a porous skeleton obtained by applying alumina slurry 11- or the like to a foamed plastic body such as open-cell polyurethane foam and then firing it. In addition to this, there is also a cylindrical shape made of alumina particles!・Nicum-shaped sintered body can be used.O The masking material that can be used in the first method of the present invention can be any substance that can be melted away or dephosphorized with heat, but the heat treatment temperature when supporting the catalyst can be used. Alternatively, it is preferable to use one that thermally melts or disappears at the temperature at which the filter is used. Examples of such materials include Wavx, polyolefin resins such as polyethylene, linear polymers such as vinyl resins, and low melting point metals or alloys such as lead and solder alloys. Wax, polyolefin, etc. are preferable because when the filter carrier 1 is immersed in a catalyst-carrying chamber after masking, the masking becomes sufficient due to its water repellency, and it can be removed or disappeared by low-temperature melting.
これらの材料は炭素と水素以外の元素を含まないことか
ら、触媒毒となり得ないことからも好オしい。これらの
材料によってフィルタ担体をマスキングするには、溶融
させた材料中にフィルタ担体の一部を浸漬することによ
って行うのが有利であるが、ワックスやプラスチックの
懸濁液を塗布又は含浸させるようにしてもよい。These materials are preferable because they do not contain any elements other than carbon and hydrogen, and therefore cannot poison the catalyst. Masking of the filter carrier with these materials is advantageously carried out by immersing part of the filter carrier in the molten material, but it is also possible to apply or impregnate it with wax or plastic suspensions. It's okay.
本発明の第2の方法で使用される無機物質マスキング材
は、アルミナ、活性アルミナ、コー′シライト、スピネ
ル等の耐熱性無機物質材料のスラリーが使用できる。特
に多孔性皮膜が得られる点でアルばすが好ましい@マス
キングはマスキング材スラリー中にフィルタの一部を浸
漬し、乾燥し、そして焼成することによって得られる。As the inorganic masking material used in the second method of the present invention, a slurry of heat-resistant inorganic materials such as alumina, activated alumina, corsilite, spinel, etc. can be used. Albas is particularly preferred because it provides a porous film.@Masking is obtained by immersing a portion of the filter in a masking material slurry, drying, and firing.
触媒としては、白金などの貴金属単体またはアルカリ金
I!4塩、アルカリ土類金属塩、モリブデン酸塩もしく
は銀垣などの金属塩が使用される。これらの金属塩は、
通常水溶液として用いられ、これら触媒担持溶液に担体
を所要回数浸漬し乾燥したのち、または所要量溶液をス
プレーなどにより担体に塗布し乾燥させたのち、焼成す
ることtごよって担持させる。As a catalyst, a noble metal such as platinum or an alkali metal I! Metal salts such as 4 salts, alkaline earth metal salts, molybdates or silver fences are used. These metal salts are
Usually used as an aqueous solution, the carrier is immersed in these catalyst-supporting solutions a required number of times and dried, or a required amount of the solution is applied to the carrier by spraying, dried, and then baked to support the catalyst.
次に本発明を、実施例および比較例をもって更に詳しく
説明する。Next, the present invention will be explained in more detail with reference to Examples and Comparative Examples.
実施例
a)−7リカ(8i01)51重量%、 アルミナ(A
I、0. ) 55重量%およびマグネシア(MgO)
14重量%の化学組成となるように選ばれた滑石、水酸
化アルミニウム(またはアルミナ)および粘りからなる
配合物を水と混合して充分に攪拌し、あらかじめスラリ
ー化しておく。市販の発泡状ボ11ウレタンフオーム(
平均空孔径;0、5 wr )を100mφX 100
mの円柱状に切り出し、前記スラリー中に浸漬し、次い
でこのスラリーから引き上げ、余分なスラリーを吹き払
った後、乾燥固化した。その後、1400’Cの電気炉
で5時間焼成して三次元網目栴造をなすフィルタ担体を
得た。Example a)-7 Rica (8i01) 51% by weight, alumina (A
I, 0. ) 55% by weight and magnesia (MgO)
A compound consisting of talc, aluminum hydroxide (or alumina) and viscosity selected to have a chemical composition of 14% by weight is mixed with water and sufficiently stirred to form a slurry in advance. Commercially available foamed foam 11 urethane foam (
Average pore diameter; 0,5 wr) 100mφX 100
A cylindrical piece of m in size was cut out, immersed in the slurry, then taken out from the slurry, excess slurry was blown off, and then dried and solidified. Thereafter, the filter carrier was fired in an electric furnace at 1400'C for 5 hours to obtain a filter carrier having a three-dimensional mesh structure.
次に、フィルタ担体を活性アルミナ、アルミナゾルおよ
び水からなるスラリーに浸漬した後、取り出して余分な
スラリーを吹き払い、120℃で5時間乾燥し、その後
800℃で1時間焼成した。この操作により、フィルタ
担体の表面に全量に対して20重量%のアルミナコート
層を形成したO
b)このフィルタ担体の軸方向一端部(1〜2倒幅)を
、溶かしたワックス(融点42℃)中に浸漬した。次に
これを室温で冷やし固めた。Next, the filter carrier was immersed in a slurry consisting of activated alumina, alumina sol, and water, then taken out, excess slurry was blown off, dried at 120°C for 5 hours, and then calcined at 800°C for 1 hour. By this operation, an alumina coating layer of 20% by weight based on the total amount was formed on the surface of the filter carrier. ). This was then cooled and solidified at room temperature.
ワックスでマスキングしたフィルタ担体を十分な蒸留水
に50分間浸漬し、取り出して余分の水を吹き払った後
、塩化パラジ9ム(PdC1,)水溶液に浸漬し、該水
溶液を1時間攪拌した〇その後フィルタ担体を水溶液か
ら取り出して120℃で3時間乾燥してワックスを溶融
除去した後、500℃で1時間焼成して、一端部のみ触
媒化されないフィルタを得た〇
実施例2
実施例1 a)と同様の手順により得たアルミナコート
層を形成したフィルタ担体を、十分な蒸留水に30分間
浸漬し取り出して余分な水を吹き払った後、塩化パラジ
ウム(PdC1t )水溶液に浸漬し、該水溶液を1時
間攪拌した。その後、フィルタ担体を水溶液から取り出
して120℃で5時間乾燥した後、500℃で1時間焼
成した。このフィルタ担体の軸方向一端部(1〜2傭輪
)を、実施例1 a)に記載したアルミナスラリーlこ
浸漬し、余分なスラ11−を吹き払い、120℃で5時
間乾燥し、その後400’Cで1時間焼成し、軸方向一
端部の触媒活性を消したフィルタを得た。The filter carrier masked with wax was immersed in sufficient distilled water for 50 minutes, taken out and the excess water was blown off, then immersed in an aqueous palladium chloride (PdC1,) solution, and the aqueous solution was stirred for 1 hour. The filter carrier was taken out of the aqueous solution and dried at 120°C for 3 hours to melt and remove the wax, and then fired at 500°C for 1 hour to obtain a filter in which only one end was not catalyzed. Example 2 Example 1 a) A filter carrier with an alumina coat layer formed thereon obtained by the same procedure as above was immersed in sufficient distilled water for 30 minutes, taken out and the excess water was blown off, and then immersed in a palladium chloride (PdC1t) aqueous solution. Stirred for 1 hour. Thereafter, the filter carrier was taken out from the aqueous solution, dried at 120°C for 5 hours, and then fired at 500°C for 1 hour. One axial end (1 to 2 wheels) of this filter carrier was immersed in the alumina slurry described in Example 1a), the excess slurry was blown off, and the filter was dried at 120°C for 5 hours. The filter was fired at 400'C for 1 hour to obtain a filter in which the catalytic activity at one end in the axial direction was eliminated.
実施例1および2で得られたフィルタを添付図面に示す
。図中、1は触媒化しない或いは触媒活性を消した部分
、セして2は触媒活性を有する部分を承す。The filters obtained in Examples 1 and 2 are shown in the attached drawings. In the figure, 1 represents a portion that is not catalyzed or has no catalytic activity, and 2 represents a portion that has catalytic activity.
比較例
実施例1 a)とIW1様□の手J1で表面にアルミナ
コート層を形成したフィルタ担体を作り、次にPdCl
、水溶液中に該フィルタ担体を、該液面上部に該担体
の115が出るように浸漬し、1時間液を攪拌した。そ
の後取り出して120℃で3時間乾燥した後、500℃
で1時間焼成してフィルタを得た。Comparative Example Example 1 A filter carrier with an alumina coat layer formed on the surface was made using a) and IW1's hands J1, and then PdCl
The filter carrier was immersed in an aqueous solution so that 115 of the carrier appeared above the liquid level, and the solution was stirred for 1 hour. After that, it was taken out and dried at 120℃ for 3 hours, and then heated to 500℃.
The filter was baked for 1 hour to obtain a filter.
本発明に従う実施例1および2の方法によると、それぞ
れワックス、γ−AI、03でマスキングすることによ
りフィルタの一部分のみ完全に触媒効果のないフィルタ
を製造することができた。According to the methods of Examples 1 and 2 according to the present invention, by masking with wax, γ-AI, and 03, respectively, it was possible to manufacture a filter in which only a portion of the filter had no catalytic effect.
しかし比較例の方法では、毛細管現象によりフィルタ全
体に触媒が担持されていた。However, in the method of the comparative example, the catalyst was supported on the entire filter due to capillarity.
以上の通り、本発明の方法によると、フィルタの所望の
部分のみが完全に触媒化されない或いは触媒作用が消さ
れたフィルタを得ることができる。フィルタの一部分、
例えば軸方向一端部(通常1〜2cslIりのみを触媒
不活性域とすることにより、該部分における微粒子蓄積
量を大きくすることができ、従って排出ガス中の微粒子
燃焼のための看火が格段に容易になり、触媒不活性域以
外の部分の微粒子蓄積量が少なくなることと相俟って、
微粒子の燃焼除去をより完全に且つ素早く行うことがで
きる。As described above, according to the method of the present invention, it is possible to obtain a filter in which only a desired portion of the filter is not completely catalyzed or the catalytic action is eliminated. part of the filter
For example, by making only one end in the axial direction (usually 1 to 2 cslI) the catalyst inactive region, it is possible to increase the amount of particulates accumulated in this part, and therefore the prevention of combustion of particulates in the exhaust gas is greatly improved. This combined with the fact that the amount of particulates accumulated in areas other than the catalyst inactive area is reduced.
The combustion removal of particulates can be performed more completely and quickly.
添付図面は、本発明の方法により得られるフィルタの一
例を示す斜視図である。
1・・・触媒活性を持たない部分
2・・・触媒化された部分
特許出願人 トヨタ自動車工業株式会社(はか1名
)
特開昭58−!77118(4)
1
ノ
80−The accompanying drawing is a perspective view showing an example of a filter obtained by the method of the present invention. 1... Portion that does not have catalytic activity 2... Catalyzed portion Patent applicant Toyota Motor Corporation (1 person) JP-A-1983-! 77118 (4) 1 no 80-
Claims (1)
な物質よりなるマスキング材でマスキングした後、該フ
ィルタ担体に触媒を担持せしめ、次いで骸マスキング材
を除去することを特做とする、ディーゼルパティキュレ
ートフィルタの製造方法。(11 Diesel patties characterized by masking a predetermined portion of the filter carrier with a masking material made of a substance that can be melted and removed or dephosphorized, then supporting the catalyst on the filter carrier, and then removing the masking material. Method of manufacturing a curate filter.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57060483A JPS58177118A (en) | 1982-04-12 | 1982-04-12 | Preparation of diesel particulate filter |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57060483A JPS58177118A (en) | 1982-04-12 | 1982-04-12 | Preparation of diesel particulate filter |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS58177118A true JPS58177118A (en) | 1983-10-17 |
Family
ID=13143566
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP57060483A Pending JPS58177118A (en) | 1982-04-12 | 1982-04-12 | Preparation of diesel particulate filter |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS58177118A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6288815U (en) * | 1985-11-25 | 1987-06-06 | ||
JPH04259618A (en) * | 1991-02-12 | 1992-09-16 | Matsushita Electric Ind Co Ltd | Regenerating device for filter of internal combustion engine |
-
1982
- 1982-04-12 JP JP57060483A patent/JPS58177118A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6288815U (en) * | 1985-11-25 | 1987-06-06 | ||
JPH0420970Y2 (en) * | 1985-11-25 | 1992-05-13 | ||
JPH04259618A (en) * | 1991-02-12 | 1992-09-16 | Matsushita Electric Ind Co Ltd | Regenerating device for filter of internal combustion engine |
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