JPH082408B2 - Diesel particulate collection filter - Google Patents
Diesel particulate collection filterInfo
- Publication number
- JPH082408B2 JPH082408B2 JP2256988A JP2256988A JPH082408B2 JP H082408 B2 JPH082408 B2 JP H082408B2 JP 2256988 A JP2256988 A JP 2256988A JP 2256988 A JP2256988 A JP 2256988A JP H082408 B2 JPH082408 B2 JP H082408B2
- Authority
- JP
- Japan
- Prior art keywords
- filter
- alumina
- spinel structure
- slurry
- diesel particulate
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 239000010949 copper Substances 0.000 claims description 19
- 229910052596 spinel Inorganic materials 0.000 claims description 17
- 239000011029 spinel Substances 0.000 claims description 17
- 229910052802 copper Inorganic materials 0.000 claims description 15
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 12
- 239000011247 coating layer Substances 0.000 claims description 12
- 239000010410 layer Substances 0.000 claims description 11
- 229910052751 metal Inorganic materials 0.000 claims description 10
- 239000002184 metal Substances 0.000 claims description 10
- 229910044991 metal oxide Inorganic materials 0.000 claims description 7
- 150000004706 metal oxides Chemical class 0.000 claims description 7
- 229910052782 aluminium Inorganic materials 0.000 claims description 4
- 239000005749 Copper compound Substances 0.000 claims description 3
- 150000001880 copper compounds Chemical class 0.000 claims description 3
- 229910052804 chromium Inorganic materials 0.000 claims description 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 18
- 239000003054 catalyst Substances 0.000 description 15
- 239000002002 slurry Substances 0.000 description 13
- 238000007747 plating Methods 0.000 description 10
- 239000000843 powder Substances 0.000 description 10
- BNGXYYYYKUGPPF-UHFFFAOYSA-M (3-methylphenyl)methyl-triphenylphosphanium;chloride Chemical compound [Cl-].CC1=CC=CC(C[P+](C=2C=CC=CC=2)(C=2C=CC=CC=2)C=2C=CC=CC=2)=C1 BNGXYYYYKUGPPF-UHFFFAOYSA-M 0.000 description 7
- 239000011248 coating agent Substances 0.000 description 7
- 238000000576 coating method Methods 0.000 description 7
- 230000000052 comparative effect Effects 0.000 description 7
- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 6
- 239000000463 material Substances 0.000 description 6
- 239000012153 distilled water Substances 0.000 description 5
- 238000010438 heat treatment Methods 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 4
- 238000010304 firing Methods 0.000 description 4
- 239000006104 solid solution Substances 0.000 description 4
- 238000002441 X-ray diffraction Methods 0.000 description 3
- 229910052878 cordierite Inorganic materials 0.000 description 3
- JSKIRARMQDRGJZ-UHFFFAOYSA-N dimagnesium dioxido-bis[(1-oxido-3-oxo-2,4,6,8,9-pentaoxa-1,3-disila-5,7-dialuminabicyclo[3.3.1]nonan-7-yl)oxy]silane Chemical compound [Mg++].[Mg++].[O-][Si]([O-])(O[Al]1O[Al]2O[Si](=O)O[Si]([O-])(O1)O2)O[Al]1O[Al]2O[Si](=O)O[Si]([O-])(O1)O2 JSKIRARMQDRGJZ-UHFFFAOYSA-N 0.000 description 3
- 239000000395 magnesium oxide Substances 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- 229910018565 CuAl Inorganic materials 0.000 description 2
- 230000003197 catalytic effect Effects 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- XTVVROIMIGLXTD-UHFFFAOYSA-N copper(II) nitrate Chemical compound [Cu+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O XTVVROIMIGLXTD-UHFFFAOYSA-N 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 229910052748 manganese Inorganic materials 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000000465 moulding Methods 0.000 description 2
- 239000013618 particulate matter Substances 0.000 description 2
- 230000000717 retained effect Effects 0.000 description 2
- 229910052712 strontium Inorganic materials 0.000 description 2
- 238000011144 upstream manufacturing Methods 0.000 description 2
- ONDPHDOFVYQSGI-UHFFFAOYSA-N zinc nitrate Chemical compound [Zn+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O ONDPHDOFVYQSGI-UHFFFAOYSA-N 0.000 description 2
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 1
- 229910015372 FeAl Inorganic materials 0.000 description 1
- 229910020068 MgAl Inorganic materials 0.000 description 1
- 229910000943 NiAl Inorganic materials 0.000 description 1
- NPXOKRUENSOPAO-UHFFFAOYSA-N Raney nickel Chemical compound [Al].[Ni] NPXOKRUENSOPAO-UHFFFAOYSA-N 0.000 description 1
- 229910003668 SrAl Inorganic materials 0.000 description 1
- XLOMVQKBTHCTTD-UHFFFAOYSA-N Zinc monoxide Chemical compound [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 description 1
- QGZKDVFQNNGYKY-UHFFFAOYSA-N ammonia Natural products N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 229910017052 cobalt Inorganic materials 0.000 description 1
- 239000010941 cobalt Substances 0.000 description 1
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 1
- -1 copper aluminate Chemical class 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007598 dipping method Methods 0.000 description 1
- 238000006073 displacement reaction Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 229910052750 molybdenum Inorganic materials 0.000 description 1
- 229910000480 nickel oxide Inorganic materials 0.000 description 1
- GNRSAWUEBMWBQH-UHFFFAOYSA-N oxonickel Chemical compound [Ni]=O GNRSAWUEBMWBQH-UHFFFAOYSA-N 0.000 description 1
- 239000003002 pH adjusting agent Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical group [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 1
- 230000001902 propagating effect Effects 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 229910052709 silver Inorganic materials 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- CIOAGBVUUVVLOB-UHFFFAOYSA-N strontium atom Chemical compound [Sr] CIOAGBVUUVVLOB-UHFFFAOYSA-N 0.000 description 1
- 229910052720 vanadium Inorganic materials 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02B—INTERNAL-COMBUSTION PISTON ENGINES; COMBUSTION ENGINES IN GENERAL
- F02B3/00—Engines characterised by air compression and subsequent fuel addition
- F02B3/06—Engines characterised by air compression and subsequent fuel addition with compression ignition
Landscapes
- Processes For Solid Components From Exhaust (AREA)
- Filtering Materials (AREA)
- Catalysts (AREA)
Description
【発明の詳細な説明】 [産業上の利用分野] 本発明は、ディーゼルエンジンの排ガス中に含まれる
パティキュレートを捕集し、これを燃焼するために用い
られるディーゼルパティキュレート捕集装置のディーゼ
ルパティキュレート捕集用フィルタに関する。The present invention relates to a diesel particulate filter of a diesel particulate trapping device used for trapping particulate matter contained in exhaust gas of a diesel engine and burning the particulate particulate matter. The present invention relates to a filter for collecting curate.
[従来の技術及びその問題点] ディーゼルエンジンから排出されるパティキュレート
は、人体及び環境に有害であることが知られており、そ
の排出量を低減する努力がなされている。その一つとし
てパティキュレートをフィルタ内に捕集して燃焼させる
装置が多く検討されている。このパティキュレート捕集
装置は、セラミックフィルタまたはハニカムフィルタ等
のディーゼルパティキュレート捕集用フィルタと、その
上流側端面に近接して取付けられるヒータ、バーナ等の
着火装置からなり、ディーゼルエンジンの排気系に取付
けて用いられる。ディーゼルエンジンの排ガスが比較的
低温であるのに対し、パティキュレートの燃焼には600
℃以上の高温を要するので、ヒータ、バーナ等の外部着
火装置を用いて前記フィルター上のパティキュレートを
燃焼させることが必要である。[Prior Art and Problems Thereof] Particulates discharged from a diesel engine are known to be harmful to the human body and the environment, and efforts have been made to reduce the amount thereof. As one of them, many devices for collecting and burning particulates in a filter have been studied. This particulate collection device consists of a diesel particulate collection filter such as a ceramic filter or a honeycomb filter, and an ignition device such as a heater and a burner that is mounted in close proximity to the upstream end surface of the diesel particulate collection filter. Used by mounting. Exhaust gas from a diesel engine is relatively low temperature, while 600 to burn particulates.
Since a high temperature of ℃ or more is required, it is necessary to burn the particulates on the filter using an external ignition device such as a heater or a burner.
この燃焼の際、着火性、燃焼伝播性を向上させるため
一時的に触媒を用いる。前記触媒の成分としては、Cu、
Agのような高熱伝導率を有するものが使用されている。
しかしながら、前記触媒は高温で使用されると触媒能が
下がり、再生性が悪くなる。これを防ぐためにアルミナ
等の高耐熱、高比表面積を有する触媒担体をフィルタ材
に被覆し、その上に金属触媒被膜を被覆する等の処置が
なされているが十分な結果は得られていない。例えばCu
は、新品時には良好な再生性を示すが、高温雰囲気にさ
らされると、アルミナ層に拡散して固溶し、銅アルミネ
ートを形成して再生性が低下するという問題がある。ま
た、担体被覆層がないと、フィルター表面上に保持され
なければならないCuが高温で容易にフィルタ材内に拡散
し、著しく性能の低下を招く原因となる。During this combustion, a catalyst is temporarily used in order to improve the ignitability and the combustion propagating property. As a component of the catalyst, Cu,
A material having a high thermal conductivity such as Ag is used.
However, when the catalyst is used at high temperature, the catalytic ability is lowered and the reproducibility is deteriorated. In order to prevent this, measures such as coating the filter material with a catalyst carrier having a high heat resistance and a high specific surface area such as alumina, and coating a metal catalyst coating on the filter material have not been obtained sufficiently. For example Cu
Shows good reproducibility when it is new, but when exposed to a high temperature atmosphere, it has a problem that it diffuses into the alumina layer and forms a solid solution to form copper aluminate, which lowers reproducibility. Further, without the carrier coating layer, Cu, which must be retained on the surface of the filter, easily diffuses into the filter material at high temperature, which causes a significant decrease in performance.
ディーゼルパティキュレート捕集用フィルタの再生性
を向上するための触媒成分として特開昭55−24597号公
報には白金族金属触媒、特開昭58−109139号公報にはC
u、Mn、V等の金属触媒成分が開示されており、また、
特開昭61−252821号公報にはCuとAgのメッキにより再生
性を向上する効果があることが開示されているが、いず
れも満足する結果は得られていない。As a catalyst component for improving the reproducibility of the diesel particulate filter, JP-A-55-24597 discloses a platinum group metal catalyst and JP-A-58-109139 discloses a C component.
Metal catalyst components such as u, Mn and V are disclosed, and
Japanese Unexamined Patent Publication (Kokai) No. 61-252821 discloses that there is an effect of improving the reproducibility by plating Cu and Ag, but no satisfactory result has been obtained.
本発明は上記従来技術の問題点に鑑みてなされたもの
で、担体被覆層と金属触媒被膜の固溶を防ぎ、再生性の
高いディーゼルパティキュレート捕集用フィルタを提供
することを目的とする。The present invention has been made in view of the above problems of the prior art, and an object of the present invention is to provide a filter for collecting diesel particulates having high reproducibility by preventing solid solution of a carrier coating layer and a metal catalyst coating.
[問題点を解決するための手段] 本発明は、前記パティキュレート補集用フィルタにお
いてフィルタ材表面に一般式AB2O4なるスピネル型構造
を有する金属酸化物の被覆層を形成し、その上層に銅ま
たは銅化合物からなる層(触媒層)を形成することを特
徴とする。[Means for Solving the Problems] The present invention is to form a coating layer of a metal oxide having a spinel structure represented by the general formula AB 2 O 4 on the surface of the filter material in the particulate collection filter, and the upper layer thereof. Is characterized in that a layer (catalyst layer) made of copper or a copper compound is formed.
前記スピネル型構造を有する金属酸化物(AB2O4)に
おいて、BはAlまたはCrであり、特にAlが好ましい。ま
たAは2価の金属であり、Sr、Cu、Mo、Mn、Fe、Co、N
i、Znからなる群のうち少なくとも1つを用いることが
好ましい。In the metal oxide (AB 2 O 4 ) having the spinel structure, B is Al or Cr, and Al is particularly preferable. A is a divalent metal, Sr, Cu, Mo, Mn, Fe, Co, N
It is preferable to use at least one of the group consisting of i and Zn.
前記スピネル構造を有する金属酸化物の被覆層は、ス
ピネル構造を有する金属酸化物を粉砕し、これを主成分
とするスラリーを調製して前記フィルタ上に被覆した後
に焼成することによって形成させてもよいし、または、
焼成することによりスピネル構造を有する金属酸化物を
形成する金属Aの化合物(例えば、酸化物)と金属Bの
化合物(例えば酸化物)との混合物から主に成るスラリ
ーを、前記フィルタ上に被覆した後焼成して形成させて
もよい。The coating layer of the metal oxide having the spinel structure may be formed by pulverizing the metal oxide having the spinel structure, preparing a slurry containing the metal oxide as a main component, coating the slurry on the filter, and then firing the slurry. Good or
A slurry mainly composed of a mixture of a compound of metal A (for example, an oxide) and a compound of metal B (for example, an oxide) which forms a metal oxide having a spinel structure by firing is coated on the filter. You may form after baking.
前記銅化合物としては、CuO、CuCr2O4が好ましい。The copper compound is preferably CuO or CuCr 2 O 4 .
また、前記スラリー中に結合剤及びpH調整剤として硝
酸アルミニウム及びアルミナゾル等を加えてもよい。Further, aluminum nitrate, alumina sol or the like may be added to the slurry as a binder and a pH adjuster.
[実施例] 以下に本発明の実施例を示し本発明を具体的に説明す
る。[Examples] The present invention will be specifically described below by showing Examples of the present invention.
実施例1 マグネシア粉末、アルミナ粉末を主成分とし、硝酸ア
ルミニウム、アルミナゾル及び蒸溜水から成るスラリー
を調製し、直径30mm、長さ50mmの円筒状ハニカムフィル
タ(コーディエライト製)のフィルタ捕集表面上に、前
記スラリーをディップ法を用いて均一に被覆した。前記
スラリーにおいてマグネシア粉末とアルミナ粉末の混合
モル比は1:2とし、平均粒径は共に5μmであった。ま
た固形分割合は30重量%とした。次にスラリーで被覆し
たハニカムフィルタを1000℃で焼成してMgAl2O4スピネ
ル層を形成させた。この被覆層の形成量はハニカムフィ
ルタ容量1当り50gとした。前記焼成したフィルタに
おいてアルミナとマグネシアの約80%以上が反応してMg
Al2O4のスピネル構造を形成していることをX線回折に
よって確認した。その後スピネル層を形成したフィルタ
を市販の無電解銅メッキ液に浸漬し、銅メッキを行なっ
た。このとき銅メッキの量はフィルタ容量1に対し20
gとなるようにした。Example 1 On a filter collecting surface of a cylindrical honeycomb filter (made of cordierite) having a diameter of 30 mm and a length of 50 mm, a slurry containing magnesia powder and alumina powder as main components, aluminum nitrate, alumina sol and distilled water was prepared. Then, the slurry was uniformly coated by the dipping method. In the slurry, the mixing molar ratio of magnesia powder and alumina powder was 1: 2, and the average particle size was 5 μm. The solid content ratio was 30% by weight. Next, the honeycomb filter coated with the slurry was fired at 1000 ° C. to form a MgAl 2 O 4 spinel layer. The amount of the coating layer formed was 50 g per honeycomb filter capacity. About 80% or more of the magnesia and alumina react with each other in the calcined filter, and Mg
It was confirmed by X-ray diffraction that a spinel structure of Al 2 O 4 was formed. Then, the filter having the spinel layer formed thereon was dipped in a commercially available electroless copper plating solution to perform copper plating. At this time, the amount of copper plating is 20 for 1 filter capacity.
It became g.
実施例2 ZnAl2O4粉末を主成分とし、アルミナゾル、硝酸アル
ミニウム、硝酸亜鉛及び蒸溜水からなるスラリーをボー
ルミルを用いて十分粉砕した後、実施例1と同様にして
ハニカムフィルタ(コーディエライト製)のフィルタ捕
集表面に被覆した。次に700℃で焼成してZnAl2O4スピネ
ル層を形成させ、実施例1と同様に無電解銅メッキを行
なった。前記ZnAl2O4粉末は、アルミナ粉末に対し酸化
亜鉛粉末を1:2のモル比で混合し、マルメライザー(錠
剤成形機)により3mmの直径を有するペレットに成形
し、1000℃以上で加熱焼結してZnAl2O4スピネル構造を
形成させたものを粉砕して用いた。Example 2 A slurry consisting mainly of ZnAl 2 O 4 powder, alumina sol, aluminum nitrate, zinc nitrate and distilled water was sufficiently crushed using a ball mill, and then a honeycomb filter (made of cordierite) was processed in the same manner as in Example 1. ) Was coated on the filter collection surface. Next, it was baked at 700 ° C. to form a ZnAl 2 O 4 spinel layer, and electroless copper plating was performed in the same manner as in Example 1. The ZnAl 2 O 4 powder was prepared by mixing zinc oxide powder with alumina powder in a molar ratio of 1: 2, molding it into pellets having a diameter of 3 mm with a Marumerizer (tablet molding machine), and baking it at 1000 ° C or higher. It was pulverized and used after being bonded to form a ZnAl 2 O 4 spinel structure.
実施例3 酸化鉄ゾルとアルミナゾルを混合し、実施例1と同様
にしてハニカムフィルタに被覆した。次に前記フィルタ
を1100℃で焼成し、スピネル構造を有するFeAl2O4の被
覆層を形成させた後、実施例1と同様にして無電解銅メ
ッキを行なった。前記酸化鉄ゾルとアルミナゾルは含有
するFeとAlのモル比を1:1とした。Example 3 An iron oxide sol and an alumina sol were mixed, and a honeycomb filter was coated in the same manner as in Example 1. Next, the filter was fired at 1100 ° C. to form a coating layer of FeAl 2 O 4 having a spinel structure, and then electroless copper plating was performed in the same manner as in Example 1. The iron oxide sol and the alumina sol had a molar ratio of Fe and Al contained of 1: 1.
実施例4 硝酸銅と硝酸アルミニウム溶液をアンモニア水を用い
てpH5.5に調整し得られたゲルを静置、熟成させ、蒸溜
水で稀釈したものを実施例と同様にしてフィルタに被覆
した。次に前記フィルタを930℃で焼成しスピネル構造
を有するCuAl2O4層を形成させた後、実施例1と同様に
して無電解銅メッキを行なった。前記硝酸銅と硝酸アル
ミニウム溶液は焼成後のモル比Cu:Alが1:2となるように
調整した。Example 4 A solution of copper nitrate and aluminum nitrate was adjusted to pH 5.5 with aqueous ammonia, the resulting gel was allowed to stand, aged, and diluted with distilled water to coat the filter in the same manner as in Example. Next, the filter was fired at 930 ° C. to form a CuAl 2 O 4 layer having a spinel structure, and then electroless copper plating was performed in the same manner as in Example 1. The copper nitrate and aluminum nitrate solutions were adjusted so that the molar ratio Cu: Al after firing was 1: 2.
実施例5〜7 実施例1と同様にして、ストロンチウム、コバルト、
ニッケルの酸化物の粉末に、各々モル比が1:2のγ−ア
ルミナ粉末を混合したものを主成分とし、アルミナゾ
ル、硝酸アルミニウム及び蒸溜水を混合したスラリーを
調製し、フィルタに被覆した。次に前記フィルタを900
〜1200℃で焼成し、各々スピネル構造を持つSrAl2O4、C
oAl2O4、NiAl2O4を80%以上含む被覆層を形成させた
後、実施例1と同様にして無電解銅メッキを行ない、各
々実施例5、6、7とした。Examples 5 to 7 In the same manner as in Example 1, strontium, cobalt,
The main component was a mixture of γ-alumina powder with a molar ratio of 1: 2 to nickel oxide powder, and a slurry was prepared by mixing alumina sol, aluminum nitrate and distilled water, and the slurry was coated on the filter. Then filter 900
SrAl 2 O 4 , C with spinel structure after firing at ~ 1200 ℃
After forming a coating layer containing 80% or more of oAl 2 O 4 and NiAl 2 O 4 , electroless copper plating was performed in the same manner as in Example 1 to obtain Examples 5, 6, and 7, respectively.
比較例1 γ−アルミナ粉末、アルミナゾル、硝酸アルミニウ
ム、蒸溜水から成るスラリーを、ディップ法を用いて実
施例1と同様にしてフィルタに被覆した。前記フィルタ
を700℃で約3時間焼成し、フィルタ上にγ−アルミナ
層を形成させた。次に実施例1と同様にして無電解銅メ
ッキを行なった。Comparative Example 1 A filter was coated with a slurry composed of γ-alumina powder, alumina sol, aluminum nitrate, and distilled water in the same manner as in Example 1 using the dip method. The filter was fired at 700 ° C. for about 3 hours to form a γ-alumina layer on the filter. Next, electroless copper plating was performed in the same manner as in Example 1.
実施例2〜7および比較例1のアルミナ層のスピネル
構造の定性は実施例と同様のX線回折によって確認し
た。The qualitativeness of the spinel structure of the alumina layers of Examples 2 to 7 and Comparative Example 1 was confirmed by X-ray diffraction similar to that of Examples.
比較例2 実施例1と同様のハニカムフィルタに、実施例1と同
様にして無電解銅メッキを行なった。Comparative Example 2 The same honeycomb filter as in Example 1 was subjected to electroless copper plating in the same manner as in Example 1.
上記に示す実施例1〜7及び比較例1,2のフィルタを
排気量2400ccの過流室式のディーゼルエンジンの排気系
に取付け(同時に12本取付けることができる。)回転数
2000回転/分、トルク1Kg・mの条件で2時間15分運転
し、フィルタ1個当り0.6〜0.65gのパティキュレートを
付着させた。The filters of Examples 1 to 7 and Comparative Examples 1 and 2 shown above were attached to the exhaust system of a turbulent chamber type diesel engine with a displacement of 2400cc (12 can be attached at the same time).
It was operated for 2 hours and 15 minutes under the conditions of 2000 revolutions / minute and a torque of 1 kg · m, and 0.6 to 0.65 g of particulates was attached to each filter.
次に、フィードガス予熱部を有し、フィルタ位置の上
流側端面にパティキュレートに着火するためのヒータを
設置したパティキュレート捕集用実験装置に前記フィル
タを組入れ、N24.5/分、O20.5/分のガス流量下で
ヒーターに通電してパティキュレートの燃焼率を測定し
た。なお、燃焼率の測定はヒータに接近したフィルタ側
端部の温度をヒータ通電量によって3段階に変化させ各
々の燃焼率を測定した。測定は、まずフィルタが新品時
のパティキュレートの燃焼率を測定した後、電気炉内で
1000℃で3時間加熱処理し前述の方法と同様にして燃焼
率を測定した。その結果を第1表に示す。Next, the filter was incorporated into an experimental device for collecting particulates, which had a feed gas preheating section and a heater for igniting particulates on the upstream end surface of the filter position, and the filter was incorporated into the device, and N 2 4.5 / min, O 2 The heater was energized at a gas flow rate of 0.5 / min to measure the burning rate of particulates. The burning rate was measured by changing the temperature of the filter-side end portion close to the heater in three stages depending on the heater energization amount. For the measurement, first measure the burning rate of particulates when the filter is new, and then in the electric furnace.
The heat treatment was carried out at 1000 ° C. for 3 hours, and the burning rate was measured by the same method as described above. The results are shown in Table 1.
各フィルタとも新品時はほぼ同等のパティキュレート
燃焼率を示したが、1000℃、3時間の加熱処理後では、
比較例1,2に比べ実施例1〜7が非常に優れていること
が確認された。 Each filter exhibited almost the same particulate burning rate when new, but after heat treatment at 1000 ° C for 3 hours,
It was confirmed that Examples 1 to 7 were extremely superior to Comparative Examples 1 and 2.
加熱処理後の各フィルタのX線回折図から、比較例1
では触媒成分であるCuがアルミナと固溶してCuAl2O4を
形成していることが確認され、一方実施例1〜7ではフ
ィルタ上の銅がCuOとしてスピネル構造を持つ被覆層上
部に保持されていることが明らかになった。また、比較
例2ではCuが加熱によってコーディエライト質のフィル
タ材内に拡散し、フィルタ捕集表面上にはほとんど確認
されなかった。From the X-ray diffraction diagram of each filter after the heat treatment, Comparative Example 1
It was confirmed that Cu as a catalyst component formed a solid solution with alumina to form CuAl 2 O 4 , while in Examples 1 to 7, copper on the filter was retained as CuO on the upper part of the coating layer having a spinel structure. It became clear that it is being done. Further, in Comparative Example 2, Cu was diffused into the cordierite filter material by heating and was hardly confirmed on the filter collection surface.
[発明の効果] 本発明のデイーゼルパティキュレート捕集用フィルタ
は、フィルタ捕集表面に、スピネル構造を有する触媒担
体被覆層を形成させた上に触媒金属被膜を被覆すること
により、触媒担体被覆層と触媒金属被覆の固溶を防ぎ、
加熱による触媒の劣化を防止している。したがって、本
発明のディーゼルパティキュレート捕集用フィルタは、
従来のフィルタに比べて再生性が高いものである。[Advantages of the Invention] In the filter for collecting diesel particulates of the present invention, the catalyst carrier coating layer is formed by forming a catalyst carrier coating layer having a spinel structure on the filter collection surface, and then coating the catalyst metal coating layer. And prevent solid solution of catalytic metal coating,
Prevents catalyst deterioration due to heating. Therefore, the filter for collecting diesel particulate according to the present invention,
The reproducibility is higher than that of the conventional filter.
Claims (1)
2O4(Aは2価の金属、BはAlまたはCr)で表されるス
ピネル構造を有する金属酸化物の被覆層を形成し、さら
に、その上層に銅または銅化合物層を形成してなること
を特徴とするディーゼルパティキュレート捕集用フィル
タ。1. An AB on the collecting surface of the particulate filter.
A coating layer of a metal oxide having a spinel structure represented by 2 O 4 (A is a divalent metal, B is Al or Cr), and a copper or copper compound layer is further formed thereon A filter for collecting diesel particulates, which is characterized in that
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2256988A JPH082408B2 (en) | 1988-02-02 | 1988-02-02 | Diesel particulate collection filter |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2256988A JPH082408B2 (en) | 1988-02-02 | 1988-02-02 | Diesel particulate collection filter |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH01199613A JPH01199613A (en) | 1989-08-11 |
JPH082408B2 true JPH082408B2 (en) | 1996-01-17 |
Family
ID=12086507
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2256988A Expired - Lifetime JPH082408B2 (en) | 1988-02-02 | 1988-02-02 | Diesel particulate collection filter |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH082408B2 (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1998042963A1 (en) * | 1997-03-25 | 1998-10-01 | Nippon Oil Co., Ltd. | Exhaust emission control catalyst, exhaust emission control catalyst manufacturing method, exhaust emission control filter, exhaust emission control filter manufacturing method, and exhaust emission control apparatus |
KR100469066B1 (en) | 2003-04-14 | 2005-02-02 | 에스케이 주식회사 | A catalytic filter for the removal of soot particulates from diesel engine and method of making the same |
JP4853495B2 (en) * | 2008-05-30 | 2012-01-11 | マツダ株式会社 | Exhaust gas purification catalyst |
-
1988
- 1988-02-02 JP JP2256988A patent/JPH082408B2/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
JPH01199613A (en) | 1989-08-11 |
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