JPH0629542B2 - Diesel particulate collection filter - Google Patents

Diesel particulate collection filter

Info

Publication number
JPH0629542B2
JPH0629542B2 JP30014787A JP30014787A JPH0629542B2 JP H0629542 B2 JPH0629542 B2 JP H0629542B2 JP 30014787 A JP30014787 A JP 30014787A JP 30014787 A JP30014787 A JP 30014787A JP H0629542 B2 JPH0629542 B2 JP H0629542B2
Authority
JP
Japan
Prior art keywords
filter
temperature
particulates
composite oxide
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
Application number
JP30014787A
Other languages
Japanese (ja)
Other versions
JPH01142208A (en
Inventor
義次 小倉
徹 須崎
希夫 木村
正 鈴木
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.)
Toyota Motor Corp
Toyota Central R&D Labs Inc
Original Assignee
Toyota Motor Corp
Toyota Central R&D Labs Inc
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 Toyota Motor Corp, Toyota Central R&D Labs Inc filed Critical Toyota Motor Corp
Priority to JP30014787A priority Critical patent/JPH0629542B2/en
Publication of JPH01142208A publication Critical patent/JPH01142208A/en
Publication of JPH0629542B2 publication Critical patent/JPH0629542B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01NGAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
    • F01N3/00Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
    • F01N3/02Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust
    • F01N3/021Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters
    • F01N3/033Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters in combination with other devices
    • F01N3/035Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters in combination with other devices with catalytic reactors, e.g. catalysed diesel particulate filters
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02BINTERNAL-COMBUSTION PISTON ENGINES; COMBUSTION ENGINES IN GENERAL
    • F02B3/00Engines characterised by air compression and subsequent fuel addition
    • F02B3/06Engines characterised by air compression and subsequent fuel addition with compression ignition

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Processes For Solid Components From Exhaust (AREA)
  • Exhaust Gas Treatment By Means Of Catalyst (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パティキュレート捕集用フィルター
に係る。
DETAILED DESCRIPTION OF THE INVENTION [Industrial application] The present invention relates to a filter for collecting diesel particulates.

〔従来の技術〕[Conventional technology]

ディーゼルパティキュレート捕集用フィルターに主とし
てカーボン微粒子からなるパティキュレートが閉塞して
フィルター機能が低下することを抑制、防止するために
フィルターに各種の触媒を担持してパティキュレートを
より低温で燃焼し、フィルターの再生性を向上させるこ
とは知られている。このフィルターの再生性の向上のた
めの触媒としては、白金族金属や卑金属等各種のものが
提案され、白金族金属では白金(Pt)、卑金属では銅
(Cu)が比較的良好な再生性を有するとされている。
In order to prevent the filter function from being deteriorated by blocking the particulates mainly composed of carbon fine particles in the filter for collecting diesel particulates, the filter is loaded with various catalysts to burn the particulates at a lower temperature, It is known to improve the reproducibility of filters. Various catalysts such as platinum group metals and base metals have been proposed as catalysts for improving the reproducibility of this filter. Platinum (Pt) is a platinum group metal, and copper (Cu) is a base metal, which has a relatively good reproducibility. It is said to have.

またパティキュレート燃焼用を主眼とはしていないが、
複合酸化物系触媒として特公昭54-38598号公報に見られ
るCr3CuNi1.4O10や特公昭56-52619号公報に見られるCo1
6Mn12CuO10等も提案されている。さらに、フィルタ
ーの再生手段として、ヒータ・バーナ等の外部着火手段
による方法や吸・排気絞り等により排ガス温度をパティ
キュレートの燃焼温度以上に上昇させる方法等も採用さ
れる。
Also, although the main purpose is not for particulate combustion,
Cr 3 CuNi 1.4 O 10 found in Japanese Patent Publication No. 54-38598 and Co 1 found in Japanese Patent Publication No. 56-52619 as complex oxide catalysts.
~ 6 Mn 1 ~ 2 CuO 10 etc. have also been proposed. Further, as a filter regenerating means, a method using an external ignition means such as a heater or a burner or a method of raising the exhaust gas temperature to a temperature higher than the combustion temperature of particulates by means of suction / exhaust throttling or the like is adopted.

〔発明が解決しようとする問題点〕[Problems to be solved by the invention]

しかしながら、上記のいずれの触媒でも、まだ着火性や
パティキュレート燃焼性の面で満足できる効果は得られ
ていない。さらに、フィルター材は再生時にパティキュ
レートの燃焼熱により1000℃程度あるいはそれ以上の高
温に曝されるが、上記触媒のいづれもこの様な高温条件
下で著しく劣化するという問題もある。
However, none of the above catalysts has yet achieved satisfactory effects in terms of ignitability and particulate combustibility. Further, the filter material is exposed to a high temperature of about 1000 ° C. or higher due to the combustion heat of particulates during regeneration, but there is a problem that any of the above catalysts is significantly deteriorated under such a high temperature condition.

〔問題点を解決するための手段〕[Means for solving problems]

本発明は、上記問題点を解決するためには、一般式A
1-xA′1-yB′(式中、Aは希土類元素から
選ばれた一種以上の元素、A′はアルカリ土類元素から
選ばれた一種以上の元素、B,B′はCr,Mn,F
e,Co,Ni,Cuから選ばれ、0≦x≦1、0≦y
≦1である。)で表わされるペロブスカイト型複合酸化
物をフィルター機能を有する担体にコーティングして成
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
フィルターを提供する。
In order to solve the above problems, the present invention provides the general formula A
1-x A'x B 1-y B'y O 3 (wherein A is one or more elements selected from rare earth elements, A'is one or more elements selected from alkaline earth elements, B, B'is Cr, Mn, F
e, Co, Ni, Cu, 0 ≦ x ≦ 1, 0 ≦ y
≦ 1. The present invention provides a filter for collecting diesel particulates, characterized in that the carrier having a filter function is coated with a perovskite type complex oxide represented by the formula (1).

フィルター機能を有する担体は、慣用のパティキュレー
ト捕集用フィルターの担体のいずれでもよく、例えば、
コージエライト、アルミナ、ムライト、チタン酸アルミ
ニウムなどのハニカム構造体や多孔構造のほか、単に粒
子を詰めたフィルターではその粒子も担体である。
The carrier having a filter function may be any carrier of a conventional particulate collection filter, for example,
In addition to a honeycomb structure or a porous structure of cordierite, alumina, mullite, aluminum titanate, etc., in a filter simply packed with particles, the particles are also carriers.

一般式A1-xA′1-yB′Oで表わされるペロブス
カイト型複合酸化物は、A,A′,B,B′を所望の組
成で含む溶液、通常酸性溶液、代表的には硝酸溶液にア
ルカリを加えてA,A′,B,B′の水酸化物を共沈さ
せ、乾燥後、焼成して得ることができる。
Formula A 1-x A 'perovskite-type composite oxide represented by x B 1-y B'O 3 is, A, A', B, a solution containing B 'in a desired composition, usually an acidic solution, typically Can be obtained by adding an alkali to a nitric acid solution to coprecipitate the hydroxides of A, A ', B and B', drying and firing.

複合酸化物を担体に担持することは、複合酸化物を分散
したスラリーに担体を浸漬し、含浸させた後、乾燥し、
必要に応じて焼成して行なうことができる。また、A,
A′,B,B′を含む分散体又は溶液に担体を浸漬し、
これらを含浸し、乾燥後、焼成してペロブスカイト型の
複合酸化物を担持させることも可能である。
Supporting the composite oxide on the carrier is performed by immersing the carrier in a slurry in which the composite oxide is dispersed, impregnating the carrier, and then drying,
It can be fired as necessary. Also, A,
Immersing the carrier in a dispersion or solution containing A ', B, B',
It is also possible to impregnate them, dry them, and then calcinate them to support the perovskite-type composite oxide.

フィルター担体への複合酸化物を担持する量は25〜150
g(フィルタ容積1あたり)、好ましくは75〜125g
程度が良い。
The amount of the complex oxide supported on the filter carrier is 25 to 150.
g (per filter volume), preferably 75 to 125 g
The degree is good.

また、複合酸化物中に白金族金属、特に白金を分散担持
すれば着火温度、ピーク温度が低下し、好ましい。白金
族金属はフィルター担体に複合酸化物を担持した後に複
合酸化物に含浸、乾燥、焼成して担持しても複合酸化物
に含浸、乾燥、焼成後複合酸化物と共にフィルタに担持
しても良い。
Further, it is preferable to disperse and support a platinum group metal, particularly platinum, in the composite oxide because the ignition temperature and the peak temperature are lowered. The platinum group metal may be supported by impregnating the composite oxide on the filter carrier, then impregnating the composite oxide, then drying and firing, or by impregnating the composite oxide, drying and firing, and then supporting it on the filter together with the complex oxide. .

〔作用〕[Action]

上記一般式で表される複合酸化物を担持したパティキュ
レート捕集用フィルターは再生性(着火温度、ピーク温
度)が向上し、かつ酸化物であることにより高温耐久性
が向上する。再生性の向上はこの複合酸化物の酸化活性
が高いことによると考えられる。
The particulate trapping filter carrying the complex oxide represented by the above general formula has improved reproducibility (ignition temperature, peak temperature), and its high temperature durability due to being an oxide. It is considered that the improvement in the reproducibility is due to the high oxidative activity of this composite oxide.

〔実施例〕〔Example〕

実施例1 A1-xA′1-yB′で示される複合酸化物を合
成するため、A元素としてLa,A′元素としてSr,
B,B′元素としてCo,Mn,Fe,Cr,Ni,C
uの硝酸塩を用意し、表1に示した目的とする組成とな
る様に濃度を調整した混合水溶液を調製した。次に、こ
の混合溶液を攪拌しながらNaCO3水溶液を徐々に滴下
し、これらの元素を水酸化物として共沈させた。得られ
た沈澱物は十分に水洗後濾別し、乾燥、粉砕、800℃大
気中で焼成を経て、第1表に示す組成のペロブスカイト
型複合酸化物粉末を得た。
Example 1 In order to synthesize a composite oxide represented by A 1-x A ′ x B 1-y B ′ y O 3 , an A element was La, an A ′ element was Sr,
Co, Mn, Fe, Cr, Ni, C as B and B'elements
A nitrate solution of u was prepared, and a mixed aqueous solution having a concentration adjusted so as to have a desired composition shown in Table 1 was prepared. Next, an aqueous NaCO 3 solution was gradually added dropwise to this mixed solution with stirring to coprecipitate these elements as hydroxides. The obtained precipitate was thoroughly washed with water, filtered off, dried, pulverized and calcined in the air at 800 ° C. to obtain a perovskite type complex oxide powder having the composition shown in Table 1.

生成物はX線回折を用いて同定し、それぞれペロブスカ
イト型の複合酸化物が形成されていることを確認した。
The product was identified by X-ray diffraction, and it was confirmed that a perovskite type complex oxide was formed in each product.

実施例2 実施例1で得られたLa0.8Sr0.2CoO3の組成を有する粉末
にPdCl2溶液を含浸し、乾燥後600℃大気中3時間焼成し
てPdを0.15wt%含有するPd/La0.8Sr0.2CoO3粉末を
得た。また同様の操作でHPtcl6溶液を用いてPt/L
a0.8Sr0.2CoO3粉末も得た。
Example 2 The powder having the composition of La 0.8 Sr 0.2 CoO 3 obtained in Example 1 was impregnated with a PdCl 2 solution, dried and baked at 600 ° C. in the atmosphere for 3 hours to obtain Pd / La containing 0.15 wt% of Pd. 0.8 Sr 0.2 CoO 3 powder was obtained. Also, in the same operation, using H 2 Ptcl 6 solution, Pt / L
A 0.8 Sr 0.2 CoO 3 powder was also obtained.

比較例1 平均粒径約10μmの活性アルミナ粉末にCu(NO3)2
溶液を含浸し、乾燥、焼成工程を経てCuを5wt%含有
する活性アルミナ粉末を調製した。
Comparative Example 1 An activated alumina powder having an average particle size of about 10 μm was impregnated with a Cu (NO 3 ) 2 aqueous solution, dried and fired to prepare an activated alumina powder containing 5 wt% of Cu.

比較例2 平均粒径約10μmの活性アルミナ粉末にPdcl2水溶液
を含浸し、乾燥、焼成工程を経てPdを0.25wt%含有す
る活性アルミナ粉末を調製した。
Comparative Example 2 An activated alumina powder having an average particle size of about 10 μm was impregnated with an aqueous Pdcl 2 solution, dried and fired to prepare an activated alumina powder containing 0.25 wt% of Pd.

試験例1 実施例1,2で調製したペロブスカイト型複合酸化物粉
末(詳細は第1表参照)及び比較例1,2で調製した触
媒粉末を市販のカーボンブラック粉末と混合し、熱分析
装置によりカーボンブラックの着火温度を測定した。な
おこのときのカーボンブラックの混合量は10wt%、熱
分析装置の昇温速度は10℃/minであり、最も高性能
であったサンプルについては熱処理(1000℃,10時
間)により耐久後の着火温度も測定した。結果を第1表
に示す。
Test Example 1 The perovskite type complex oxide powder prepared in Examples 1 and 2 (see Table 1 for details) and the catalyst powder prepared in Comparative Examples 1 and 2 were mixed with a commercially available carbon black powder, and the mixture was analyzed by a thermal analyzer. The ignition temperature of carbon black was measured. At this time, the amount of carbon black mixed was 10 wt% and the temperature increase rate of the thermal analysis device was 10 ° C / min. The sample with the highest performance was subjected to heat treatment (1000 ° C, 10 hours) for ignition after endurance. The temperature was also measured. The results are shown in Table 1.

第1表より、本発明に於けるペロブスカイト型複合酸化
物はディーゼル排気中のパティキュレートの主成分であ
るカーボン微粒子の燃焼温度を著しく低下させることが
可能であること、B,B′位置にCo,Cu,Mn,F
e,Cr,Ni等のいずれの遷移金属を配しても従来の
構成であるCuO,PdO触媒に比べて良好な性能を有すこと
がわかる。またAとA′との割合を変えた例も一部紹介
しているが、従来触媒よりも良好な性能を有すること、
本ペロブスカイト型酸化物に白金族触媒、特にPdを共
存させることにより更に性能向上が可能であることがわ
かる。またこのペロブスカイト型酸化物は1000℃で熱処
理を行ってもほとんどカーボンブラツクの燃焼性が低下
しないことから耐久性にも優れるといえる。
From Table 1, it can be seen that the perovskite type complex oxide according to the present invention can remarkably lower the combustion temperature of the carbon fine particles which are the main component of the particulates in the diesel exhaust, and Co at the B and B'positions. , Cu, Mn, F
It can be seen that even if any transition metal such as e, Cr, or Ni is provided, it has better performance than the conventional CuO or PdO catalyst. Although some examples of changing the ratio of A and A'are also introduced, they have better performance than conventional catalysts,
It can be seen that the performance can be further improved by coexisting a platinum group catalyst, particularly Pd, with the present perovskite oxide. It can be said that this perovskite type oxide is also excellent in durability since the flammability of the carbon black hardly deteriorates even if it is heat-treated at 1000 ° C.

なお、第1表の実施例1においてLa0.8Sr0.2CrO3及びLa
NiO3は、着火温度及びピーク温度が比較例1と同等の結
果となっている。しかしながら、第1表の比較例1のPd
OやCuOは調製時の焼成温度が600℃と低く、実質的に全
く劣化していない状態での性能を示している。PdO及びC
uOは1000℃程度の熱を受けると急激に着火性能が悪化す
る。これに対し、La0.8Sr0.2CrO3やLaNiO3は高温で安定
であり、高温耐久性の面で従来の触媒であるPdOやCuOよ
りも優れている。
In Example 1 of Table 1, La 0.8 Sr 0.2 CrO 3 and La
NiO 3 has the same ignition temperature and peak temperature as those of Comparative Example 1. However, Pd of Comparative Example 1 in Table 1
O and CuO have a low firing temperature of 600 ° C at the time of preparation, and show performance in a state where they are not substantially deteriorated. PdO and C
When uO receives heat of about 1000 ° C, its ignition performance deteriorates rapidly. On the other hand, La 0.8 Sr 0.2 CrO 3 and LaNiO 3 are stable at high temperatures and are superior to conventional catalysts PdO and CuO in terms of high temperature durability.

試験例2 本発明の効果をより実機に近い形で確認するため、以下
の実験を行った。具体的操作は次の通りである。
Test Example 2 The following experiment was conducted in order to confirm the effect of the present invention in a form closer to that of an actual machine. The specific operation is as follows.

(1)良好な性能を示したLa0.8Sr0.2CoO3粉末をエチルア
ルコール1ml中に1gの割合で分散させ、スラリー状に
した。
(1) La 0.8 Sr 0.2 CoO 3 powder showing good performance was dispersed in 1 ml of ethyl alcohol at a ratio of 1 g to form a slurry.

(2)調製したスラリーに市販のコージエライト製ハニカ
ムフィルター(直径30mm、長さ50mm、気孔率60
%)を浸漬し、フィルター材にスラリーを付着させた。
(2) A commercially available cordierite honeycomb filter (diameter 30 mm, length 50 mm, porosity 60) was added to the prepared slurry.
%) And the slurry was attached to the filter material.

(3)スラリー中よりこのフィルターを取り出し、圧縮空
気により余分のスラリーを吹き払った後乾燥する操作を
数回くり返し、800℃×3h焼成してLa0.8Sr0.2CoO3
フィルター容積1あたり約100gコーティングしたフ
ィルターAを得た。
(3) Take out this filter from the slurry, blow off excess slurry with compressed air, and then repeat drying several times, and bake at 800 ° C x 3h to make La 0.8 Sr 0.2 CoO 3 about 100g per filter volume. A coated filter A was obtained.

(4)市販のコージエライト製ハニカムフィルター(前述
と同じもの)を用意し、活性アルミナ粉末、硝酸アルミ
ニウム、アルミナゾル、蒸留水とから成るスラリーを用
いて、フィルター上に活性アルミナコート層を形成し
た。コート量はフィルター容積1あたり約75gであ
る。
(4) A commercially available cordierite honeycomb filter (the same as that described above) was prepared, and an active alumina coat layer was formed on the filter using a slurry composed of activated alumina powder, aluminum nitrate, alumina sol, and distilled water. The coating amount is about 75 g per filter volume.

(5)次にそのフィルターをPdCl2溶液に浸漬し、乾燥、焼
成工程を経てフィルター溶積1あたり1gのPdが担
持されたフィルターBを得た。
(5) Next, the filter was immersed in a PdCl 2 solution, dried and fired to obtain a filter B carrying 1 g of Pd per 1 of the filter melt.

(6)得られたフィルターA及びBを2.4渦流窒式ディー
ゼルエンジンの排気系に取り付け、2,000rpmトルク3kg
・mで2時間運転して、フィルター1ケあたり0.6〜0.6
5gのパティキュレートを捕集した。
(6) Install the obtained filters A and B in the exhaust system of a 2.4 vortex nitrogen diesel engine, 2,000 rpm torque 3 kg
・ Operating for 2 hours at m, 0.6 to 0.6 per filter
5 g of particulates were collected.

(7)このフィルターを第1図に示す評価装置に取り付
け、ガス温(N−Oガス,O10vol%,流量;
10/min)を30℃/minで上昇させながら着火温度
を測定した。第1図中、1が反応管、2が排気管、3が
−Oガス導入管、4がフィルター、5が整流器、
6が電気炉である。着火温度の判定はフィルター内温度
の上昇曲線を用いて行い、フィルター再生操作終了後は
重量法によりパティキュレートの燃焼率も算出した。結
果を第2表に示す。
(7) This filter was attached to the evaluation device shown in FIG. 1, and the gas temperature (N 2 —O 2 gas, O 2 10 vol%, flow rate;
10 / min) was increased at 30 ° C./min to measure the ignition temperature. In FIG. 1, 1 is a reaction tube, 2 is an exhaust tube, 3 is a N 2 —O 2 gas introduction tube, 4 is a filter, 5 is a rectifier,
6 is an electric furnace. The ignition temperature was determined using the rise curve of the temperature inside the filter, and after the filter regeneration operation, the burning rate of particulates was also calculated by the gravimetric method. The results are shown in Table 2.

第2表から本発明によるペロブスカイト型複合酸化物
は、実際のフィルター材にコーティングされた場合でも
従来の触媒よりも低温でパティキュレートを燃焼させう
ることがわかった。なお、本実施例、試験例では、A,
A′としてそれぞれLa,Srを代表として紹介した
が、この様なパティキュレートの燃焼特性はA,A′元
素間に生ずる酸素欠陥とB,B′に配する遷移金属によ
り得られる酸化活性によるものと考えられ、従って、A
に配する元素としてCe,Pr,Nd,Y他の希土類元
素、A′に配する元素としてBa,Mg,Ca他のアル
カリ土類を用いても同様の効果が得られる。
Table 2 shows that the perovskite-type composite oxide according to the present invention can burn particulates at a lower temperature than conventional catalysts even when coated on an actual filter material. In the examples and test examples, A,
La and Sr have been introduced as representatives of A ', respectively. The combustion characteristics of such particulates are due to the oxygen deficiency generated between the A and A'elements and the oxidation activity obtained by the transition metal arranged in B and B'. And therefore A
The same effect can be obtained by using Ce, Pr, Nd, Y or other rare earth element as the element to be arranged in the above, and Ba, Mg, Ca or other alkaline earth element as the element in the arrangement to A '.

〔発明の効果〕〔The invention's effect〕

本発明の特定のペロブスカイト型複合酸化物を担持した
パティキュレート捕集用フィルターは、従来品と比べ
て、フィルターの再生性(パティキュレートの燃焼温度
等)が向上し、かつ耐久性がより優れている。
The particulate collection filter carrying the specific perovskite-type composite oxide of the present invention has improved filter reproducibility (combustion temperature of particulates, etc.) and is more durable than conventional products. There is.

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

第1図は実施例のフィルターの特性評価用装置の概略図
である。 1……反応管、2……排気管、 3……N−Oガス導入管、 4……フィルター、5……整流器、 6……電気炉。
FIG. 1 is a schematic diagram of an apparatus for evaluating characteristics of a filter according to an embodiment. 1 ...... reaction tube, 2 ...... exhaust pipe, 3 ...... N 2 -O 2 gas inlet, 4 ...... filter, 5 ...... rectifier, 6 ...... electric furnace.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 木村 希夫 愛知県愛知郡長久手町大字長湫字横道41番 地の1 株式会社豊田中央研究所内 (72)発明者 鈴木 正 愛知県愛知郡長久手町大字長湫字横道41番 地の1 株式会社豊田中央研究所内 (56)参考文献 特開 昭58−43214(JP,A) 特開 昭61−129030(JP,A) 特開 昭61−146314(JP,A) 特開 昭63−65927(JP,A) ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Norio Kimura Ai Prefecture Nagakute Town, Aichi Prefecture, Oita, Nagakage 1 No. 41 Yokomichi Toyota Central Research Institute Co., Ltd. (72) Inventor Masa Suzuki, Aichi Prefecture Nagakute Town, Aichi Prefecture 1 in 41, Yokomichi, Nagatoji (56) References JP-A-58-43214 (JP, A) JP-A-61-129030 (JP, A) JP-A-61-146314 (JP, JP-A) A) JP-A-63-65927 (JP, A)

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】一般式A1-xA′1-yB′(式
中、Aは希土類元素から選ばれた一種以上の元素、A′
はアルカリ土類元素から選ばれた一種以上の元素、B,
B′はCr,Mn,Fe,Co,Ni,Cuから選ば
れ、0≦x≦1,0≦y≦1である。)で表わされるペ
ロブスカイト型複合酸化物をフィルター機能を有する担
体にコーティングして成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ー。
1. A general formula A 1-x A ′ x B 1-y B ′ y O 3 (wherein A is one or more elements selected from rare earth elements, A ′
Is one or more elements selected from alkaline earth elements, B,
B ′ is selected from Cr, Mn, Fe, Co, Ni and Cu, and 0 ≦ x ≦ 1, 0 ≦ y ≦ 1. ) A diesel particulate filter for collecting diesel particulates, characterized by comprising a carrier having a filter function coated with a perovskite type complex oxide represented by the formula (1).
【請求項2】前記複合酸化物中に白金族金属を分散担持
した特許請求の範囲第1項記載のフィルター。
2. The filter according to claim 1, wherein a platinum group metal is dispersed and carried in the composite oxide.
JP30014787A 1987-11-30 1987-11-30 Diesel particulate collection filter Expired - Lifetime JPH0629542B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP30014787A JPH0629542B2 (en) 1987-11-30 1987-11-30 Diesel particulate collection filter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP30014787A JPH0629542B2 (en) 1987-11-30 1987-11-30 Diesel particulate collection filter

Publications (2)

Publication Number Publication Date
JPH01142208A JPH01142208A (en) 1989-06-05
JPH0629542B2 true JPH0629542B2 (en) 1994-04-20

Family

ID=17881307

Family Applications (1)

Application Number Title Priority Date Filing Date
JP30014787A Expired - Lifetime JPH0629542B2 (en) 1987-11-30 1987-11-30 Diesel particulate collection filter

Country Status (1)

Country Link
JP (1) JPH0629542B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1829609A1 (en) * 2004-12-24 2007-09-05 Dowa Mining Co., Ltd. Pm combustion catalyst and filter
US7923408B2 (en) 2006-02-21 2011-04-12 Mitsubishi Jidosha Kogyo Kabushiki Kaisha Diesel particulate filter and exhaust emission control system

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4904458B2 (en) * 2006-02-07 2012-03-28 Dowaエレクトロニクス株式会社 Composite oxide and filter for PM combustion catalyst
JP5233026B2 (en) * 2006-03-06 2013-07-10 Dowaエレクトロニクス株式会社 Manufacturing method of DPF
FR3087833B1 (en) * 2018-10-26 2021-02-19 Psa Automobiles Sa SELF-GENERATING PARTICULATE FILTER AND REDUCER PRODUCER FOR NOX REDUCTION
FR3103117A1 (en) * 2019-11-20 2021-05-21 Psa Automobiles Sa Process for treating NOx with ammonia produced in-situ in a motor vehicle particulate filter and device for implementing the process

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1829609A1 (en) * 2004-12-24 2007-09-05 Dowa Mining Co., Ltd. Pm combustion catalyst and filter
US7923408B2 (en) 2006-02-21 2011-04-12 Mitsubishi Jidosha Kogyo Kabushiki Kaisha Diesel particulate filter and exhaust emission control system

Also Published As

Publication number Publication date
JPH01142208A (en) 1989-06-05

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