JPH07323228A - Phosphoric acid based composition and catalyst for reductive destructing nox using the same - Google Patents

Phosphoric acid based composition and catalyst for reductive destructing nox using the same

Info

Publication number
JPH07323228A
JPH07323228A JP6118413A JP11841394A JPH07323228A JP H07323228 A JPH07323228 A JP H07323228A JP 6118413 A JP6118413 A JP 6118413A JP 11841394 A JP11841394 A JP 11841394A JP H07323228 A JPH07323228 A JP H07323228A
Authority
JP
Japan
Prior art keywords
phosphoric acid
catalyst
nox
phosphorus
based composition
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
Application number
JP6118413A
Other languages
Japanese (ja)
Inventor
Kenji Nakano
賢二 中野
Masaharu Nonoguchi
正治 野々口
Masanobu Ishida
政信 石田
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.)
Kyocera Corp
Original Assignee
Kyocera Corp
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 Kyocera Corp filed Critical Kyocera Corp
Priority to JP6118413A priority Critical patent/JPH07323228A/en
Publication of JPH07323228A publication Critical patent/JPH07323228A/en
Pending legal-status Critical Current

Links

Classifications

    • 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

Abstract

PURPOSE:To enable to stably purify an exhaust gas from a future diesel engine by providing high NOx reduction and destruction action in a high oxygen concn. atmosphere and improving heat resistance. CONSTITUTION:A phosphoric acid based composition is composed of at least copper(Cu), zirconium(Zr), phosphorus(P) and oxygen(O) as the structural components, satisfies 0.70<=y/z<=1.0 and 0.08<=x/(x+y+z)<=0.15 when the atomic ratio of copper(Cu), zirconium(Zr) and phosphorus(P) is x:y:z and is used for the catalyst for reductive destruction NOx.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、新規なリン酸系組成物
であり、特にNOx還元分解用触媒に適した組成物およ
びその製造方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a novel phosphoric acid composition, and more particularly to a composition suitable for a catalyst for NOx reduction decomposition and a method for producing the same.

【0002】[0002]

【従来技術】近年、環境汚染が重要な問題となり、その
中でも自動車の排気ガス中のNOx、COx等の有害物
質を分解、除去する方法の開発が急務となっている。そ
こで、従来より用いられている自動車の排気ガス浄化用
触媒としては、一酸化炭素(COx)および炭化水素
(CxHy)の酸化と、窒素酸化物(NOx)の還元を
同時に行う三元触媒が汎用されている。このような触媒
としては、Pd,Pt,Rh等の貴金属のγ−Al2
3 との混合物が用いられ、この触媒をコージェライト等
の耐火性担体に担持したものが用いられている。
2. Description of the Related Art In recent years, environmental pollution has become an important issue, and among them, there is an urgent need to develop a method for decomposing and removing harmful substances such as NOx and COx in exhaust gas of automobiles. Thus, as a conventional exhaust gas purifying catalyst for automobiles, a three-way catalyst that simultaneously oxidizes carbon monoxide (COx) and hydrocarbons (CxHy) and reduces nitrogen oxides (NOx) is widely used. Has been done. As such a catalyst, γ-Al 2 O of a noble metal such as Pd, Pt, Rh is used.
A mixture with 3 is used, and this catalyst is supported on a refractory carrier such as cordierite.

【0003】[0003]

【発明が解決しようとする問題点】しかしながら、この
ような触媒は、およそ1%程度の酸素濃度においてのみ
排気ガスの浄化を効率よく行うことができ、排気ガスの
酸素濃度が上記最適値よりも高くなると有効に働かなく
なると言う問題がある。そこで、通常は排気ガス中の酸
素濃度を測定して常に最適な空燃比となるように制御す
ることが行われているが、これより高い酸素濃度の排気
ガス浄化はほとんどできていないのが現状である。
However, such a catalyst can efficiently purify the exhaust gas only at an oxygen concentration of about 1%, and the oxygen concentration of the exhaust gas is higher than the above optimum value. There is a problem that it cannot work effectively when it gets higher. Therefore, it is usual to measure the oxygen concentration in the exhaust gas and control it so that it always has the optimum air-fuel ratio.However, it is almost impossible to purify exhaust gas with a higher oxygen concentration than this. Is.

【0004】一方、ガソリンエンジンにおいては、低燃
費化を図るために希薄燃焼方式の研究開発が行われてい
るが、この場合、排気ガス中の酸素濃度が数%となり、
貴金属の酸素被毒により排気ガスの浄化ができなくなる
という欠点がある。またディーゼルエンジンにおいて
も、現状の燃焼方式では排気ガス中の酸素濃度が高いた
めに、排気ガスの浄化が全くなされていないのが現状で
ある。
On the other hand, in a gasoline engine, research and development of a lean burn system has been carried out in order to reduce fuel consumption. In this case, the oxygen concentration in the exhaust gas becomes several%,
There is a drawback that exhaust gas cannot be purified due to oxygen poisoning of precious metals. Even in the diesel engine, the exhaust gas is not purified at all under the current combustion system because the oxygen concentration in the exhaust gas is high.

【0005】また、工場等の固定式の燃焼装置において
は、排気ガス中にアンモニア等の還元剤を混入すること
により酸素濃度の高い排気ガス中のNOxの還元が行わ
れているが、この方法を自動車等の移動式燃焼装置に取
り付けることは安全性の面で問題があった。
Further, in a fixed combustion apparatus such as a factory, NOx in exhaust gas having a high oxygen concentration is reduced by mixing a reducing agent such as ammonia into the exhaust gas. There was a problem in terms of safety in mounting the vehicle on a mobile combustion device such as an automobile.

【0006】そこで、本出願人は、先にCu、Zr、P
(リン)およびO(酸素)からなるリン酸系組成物が比
較的高い酸素濃度下でもNOxを還元分解でき、これを
触媒として使用できることを提案したが、上記リン酸系
組成物では、自動車用触媒の耐熱温度と考えられる10
00℃付近に長時間保持された後に触媒活性が著しく低
下するという問題を有することが判明した。
[0006] Therefore, the present applicant has previously proposed that Cu, Zr, P
It has been proposed that a phosphoric acid-based composition composed of (phosphorus) and O (oxygen) can reductively decompose NOx even under a relatively high oxygen concentration and can be used as a catalyst. It is considered to be the heat resistant temperature of the catalyst 10
It has been found that there is a problem that the catalytic activity is significantly reduced after being kept at around 00 ° C for a long time.

【0007】[0007]

【問題点を解決するための手段】本発明者らは、上記リ
ン酸系組成物に対して、高濃度の酸素中でのNOx還元
分解性について組成の点から詳細に検討を重ねた結果、
リン酸系組成物の1つであるCuZr4 (PO4 6
成において、Zr含有量を定比組成より多く存在させる
ことにより、酸素濃度5%程度でも高いNOx還元性を
有するとともに、高い耐熱性を有し高温での処理後の触
媒性能の劣化が小さくなることを見いだし、本発明に至
った。
[Means for Solving the Problems] The inventors of the present invention have studied the above phosphoric acid-based composition in detail in terms of NOx reductive decomposability in high-concentration oxygen.
In CuZr 4 (PO 4 ) 6 composition, which is one of the phosphoric acid-based compositions, by making the Zr content more than the stoichiometric composition, it has a high NOx reducing property even at an oxygen concentration of about 5% and a high heat resistance. The present invention has been accomplished by finding that the deterioration of catalytic performance after treatment at high temperature is small.

【0008】即ち、本発明のリン酸系組成物は、少なく
とも銅(Cu)、ジルコニウム(Zr)、リン(P)お
よび酸素(O)を構成元素としてなるリン酸系組成物で
あり、前記銅(Cu)、ジルコニウム(Zr)およびリ
ン(P)の原子比をx:y:zとした時、0.70≦y
/z≦1、0.08≦x/(x+y+z)≦0.16を
満足することを特徴とするものであり、かかる組成物は
さらに、700〜1000℃においてCuZr4 (PO
4 6 相を主結晶相とすることを特徴とするものであ
り、本発明によれば、上記リン酸系組成物をNOx還元
分解用触媒として用いることを特徴とするものである。
That is, the phosphoric acid composition of the present invention is a phosphoric acid composition containing at least copper (Cu), zirconium (Zr), phosphorus (P) and oxygen (O) as constituent elements. When the atomic ratio of (Cu), zirconium (Zr) and phosphorus (P) is x: y: z, 0.70 ≦ y
/ Z ≦ 1, 0.08 ≦ x / (x + y + z) ≦ 0.16, wherein the composition further comprises CuZr 4 (PO) at 700 to 1000 ° C.
4 ) It is characterized in that the 6th phase is the main crystal phase, and according to the present invention, the phosphoric acid-based composition is used as a catalyst for NOx reduction decomposition.

【0009】以下、本発明を詳述する。本発明における
リン酸系組成物は、構成元素としてCu、Zr、P(リ
ン)およびO(酸素)を含むものであり、ZrのPに対
する原子比(y/z)が0.70≦y/z≦1,特に
0.70≦y/z≦0.85の範囲にあり、Cu、Zr
およびPの全原子に対するCuの原子比(x/x+y+
z)が0.08≦x/(x+y+z)≦0.16、特に
0.08≦x/(x+y+z)≦0.15であることが
望ましい。
The present invention will be described in detail below. The phosphoric acid-based composition according to the present invention contains Cu, Zr, P (phosphorus) and O (oxygen) as constituent elements, and the atomic ratio (y / z) of Zr to P is 0.70 ≦ y /. z ≦ 1, particularly 0.70 ≦ y / z ≦ 0.85, and Cu, Zr
And atomic ratio of Cu to all atoms of P (x / x + y +
z) is preferably 0.08 ≦ x / (x + y + z) ≦ 0.16, and more preferably 0.08 ≦ x / (x + y + z) ≦ 0.15.

【0010】本発明の組成物において、各元素の組成を
前述の範囲に限定したのは、y/z比、x/x+y+z
比が前述した組成範囲を逸脱する組成では、いずれも前
記結晶相以外の結晶相が析出し、触媒作用が低下するた
めである。
In the composition of the present invention, the composition of each element is limited to the above range by the y / z ratio, x / x + y + z.
This is because in any composition where the ratio deviates from the above-mentioned composition range, a crystal phase other than the above-mentioned crystal phase is precipitated and the catalytic action is lowered.

【0011】なお、本発明における上記リン酸系組成物
は、触媒として使用する場合、800〜1000℃の温
度に保持されるが、本発明の組成物は、この温度範囲に
おいても結晶が変化したりすることなく、CuZr
4 (PO4 6 結晶相を主相として存在するものである
が、この主結晶相以外に、高酸素濃度下でのNOx転化
率を低下させない範囲で微量のリン酸ジルコニウムまた
はジルコニウムやアモルファス相を含んでいてもよい。
When the phosphoric acid-based composition of the present invention is used as a catalyst, it is maintained at a temperature of 800 to 1000 ° C., but the composition of the present invention changes its crystal even in this temperature range. Without CuZr
4 (PO 4 ) 6 crystal phase exists as a main phase, but in addition to this main crystal phase, a trace amount of zirconium phosphate or zirconium phosphate or an amorphous phase is included as long as the NOx conversion rate under a high oxygen concentration is not reduced. May be included.

【0012】次に、前記リン酸系組成物を製造するため
の1つの例として、ゾルゲル法に基づき説明する。まず
原料として、Cuを含有する水溶性化合物とZrを含有
する水溶性化合物をそれぞれ準備し、先にCu含有水溶
液とZr含有水溶液との混合溶液をを調製する。一方、
水溶性のP(リン)含有化合物溶液を調製し、これを先
のCuおよびZrを含有する水溶液に滴下混合する。こ
の時のCu、Zr、およびPは前述したような組成比に
なるように調製される。
Next, a sol-gel method will be described as an example for producing the phosphoric acid composition. First, a water-soluble compound containing Cu and a water-soluble compound containing Zr are prepared as raw materials, respectively, and a mixed solution of a Cu-containing aqueous solution and a Zr-containing aqueous solution is prepared first. on the other hand,
A water-soluble P (phosphorus) -containing compound solution is prepared, and this is added dropwise to the above aqueous solution containing Cu and Zr. At this time, Cu, Zr, and P are prepared so as to have the above composition ratio.

【0013】次に、上述のようにして得られた混合溶液
を6.0±0.5の範囲にpH調整する。調整にあたっ
ては、アンモニア水や尿素などを使用する。このように
pHを調整することにより、混合溶液はゾル化する。こ
れを濾過した後、その残さ分を650乃至1050℃、
特に700乃至1000℃の温度で10時間以上熱処理
することにより得ることができる。
Next, the pH of the mixed solution obtained as described above is adjusted to a range of 6.0 ± 0.5. Ammonia water or urea is used for adjustment. By adjusting the pH in this way, the mixed solution becomes a sol. After filtering this, the residue is 650 to 1050 ° C,
In particular, it can be obtained by heat treatment at a temperature of 700 to 1000 ° C. for 10 hours or more.

【0014】上記の製法において、pH値が上記範囲か
ら逸脱するとZr/Cu/Pモル比モル比を正確に制御
することが困難となるためである。また熱処理温度が6
50℃よりも低いと結晶化が十分に行われないために前
記X線回折ピークを有する結晶相が析出せず、1050
℃を越えると他の結晶相が析出し、触媒特性が低下する
ためである。
This is because in the above production method, if the pH value deviates from the above range, it becomes difficult to control the Zr / Cu / P molar ratio molar ratio accurately. The heat treatment temperature is 6
If the temperature is lower than 50 ° C., the crystallization is not sufficiently performed, so that the crystal phase having the X-ray diffraction peak does not precipitate, and 1050
This is because when the temperature exceeds ° C, other crystal phases are precipitated and the catalytic properties are deteriorated.

【0015】本発明により得られた組成物を用いてNO
x還元分解用触媒を作製する場合には、上記のようにし
て得られた合成粉を適度に粉砕した後、触媒として用い
るが、1200〜1600℃で再度焼成し、粉砕を行っ
た粉末を用いても良い。なお、触媒としての粉末の比表
面積はBET値で10m2 /g以上となるように制御す
ることが望ましい。
NO using the composition obtained according to the invention
x When a catalyst for reductive decomposition is produced, the synthetic powder obtained as described above is appropriately crushed and then used as a catalyst, but the powder that is calcinated again at 1200 to 1600 ° C. and crushed is used. May be. The specific surface area of the powder as a catalyst is preferably controlled so that the BET value is 10 m 2 / g or more.

【0016】[0016]

【作用】本発明によれば、Cu、Zr、P(リン)およ
びO(酸素)からなるリン酸系化合物において、CuZ
4 (PO4 6 で表される定比系に対して、Zrを過
剰に存在させることにより、NOx転化率を向上させる
ことができると同時に耐熱性を高め、高温での安定した
特性の維持が可能となる。これは、Zr量が増えること
によって結晶化および相転移の進行が遅くなるためと考
えられる。
According to the present invention, in the phosphoric acid compound consisting of Cu, Zr, P (phosphorus) and O (oxygen), CuZ
By making Zr excessively present in the stoichiometric system represented by r 4 (PO 4 ) 6 , the NOx conversion rate can be improved and at the same time, the heat resistance can be improved and stable characteristics at high temperature can be obtained. It can be maintained. It is considered that this is because the increase of Zr amount slows down the progress of crystallization and phase transition.

【0017】[0017]

【実施例】【Example】

実施例 出発原料として、Cu(NO3 2 ・3H2 O、ZrO
(NO3 2 ・2H2O、NH4 2 PO4 を用いて、
Cu、ZrおよびPの原子比、y/x、x/x+y+z
が表1に示す比になるように、それぞれ秤量した、ま
ず、Cu(NO32 ・3H2 OとZrO(NO3 2
・2H2 Oを純水に溶解させ十分に攪拌する。その後、
攪拌しながら、この溶液にNH4 2 PO4 水溶液を徐
々に滴下し、その後アンモニア水でpH6に調整し1時
間攪拌する。その後、吸引濾過、水洗、凍結乾燥および
熱風乾燥後、700℃で80時間、空気中で焼成した。
Example As starting materials, Cu (NO 3 ) 2 .3H 2 O and ZrO
Using (NO 3 ) 2 · 2H 2 O and NH 4 H 2 PO 4 ,
Atomic ratio of Cu, Zr and P, y / x, x / x + y + z
Were weighed so that the ratios shown in Table 1 were obtained. First, Cu (NO 3 ) 2 .3H 2 O and ZrO (NO 3 ) 2
・ Dissolve 2H 2 O in pure water and stir it sufficiently. afterwards,
An NH 4 H 2 PO 4 aqueous solution is gradually added dropwise to this solution while stirring, and then the pH is adjusted to 6 with aqueous ammonia and the mixture is stirred for 1 hour. Then, after suction filtration, washing with water, freeze-drying and hot-air drying, the mixture was baked at 700 ° C. for 80 hours in the air.

【0018】次に、得られた試料は、3ton/cm2
で冷間静水圧成形後、40メッシュパス、80メッシュ
オンの粉末に整粒した。ついで、この試料を用いて、N
O=C2 4 =1000ppm、O2 =5%、He=残
部、SV(空間速度)=4800/hの条件で200℃
から500℃の範囲でNOの還元分解活性をガスクロマ
トグラフを用いて測定した。結果を表1に示した。
Next, the obtained sample was 3 ton / cm 2.
After cold isostatic pressing, the powder was sized to powder of 40 mesh pass and 80 mesh on. Then, using this sample, N
200 ° C. under the conditions of O = C 2 H 4 = 1000 ppm, O 2 = 5%, He = the rest, SV (space velocity) = 4800 / h
The reductive decomposition activity of NO was measured in the range from 1 to 500 ° C. using a gas chromatograph. The results are shown in Table 1.

【0019】また、得られた試料に対して1000℃で
16時間空気中で熱処理し、その処理後のNOx転化率
も測定した。さらに、各試料に対してX線回折測定を行
い、検出される結晶相を同定し、試料を1000℃で1
6時間熱処理後も同様に測定を行い、結晶相の変化を調
べた。
Further, the obtained sample was heat-treated in air at 1000 ° C. for 16 hours, and the NOx conversion rate after the treatment was also measured. Further, X-ray diffraction measurement is performed on each sample to identify the crystal phase to be detected, and the sample is subjected to 1
After the heat treatment for 6 hours, the same measurement was performed to examine the change of the crystal phase.

【0020】[0020]

【表1】 [Table 1]

【0021】表1によれば、y/z、x/x+y+zの
比率が本発明の範囲を逸脱する試料No.1、6、7、
8、9、10、14はいずれもNOx転化率が低かった
り、熱処理後の特性の変化が大きいものであった。これ
に対して、本発明品は、いずれも高いNOx転化率を示
し、熱処理後の特性の劣化も小さいものであった。
According to Table 1, samples Nos. 1, 6, 7, in which the ratio of y / z and x / x + y + z deviates from the scope of the present invention.
Nos. 8, 9, 10, and 14 had low NOx conversion rates and large changes in characteristics after heat treatment. On the other hand, all the products of the present invention showed a high NOx conversion rate, and the deterioration of the characteristics after the heat treatment was small.

【0022】[0022]

【発明の効果】以上詳述した通り、本発明のリン酸系組
成物は、高酸素濃度の雰囲気中で高いNOx還元分解作
用を有するとともに、耐熱性に優れることから、今後の
ディーゼルエンジンなどの排気ガスの安定した浄化を行
うことができる。
As described in detail above, the phosphoric acid-based composition of the present invention has a high NOx reduction decomposition action in an atmosphere of high oxygen concentration and is excellent in heat resistance, and therefore, it is suitable for future diesel engines and the like. Exhaust gas can be stably purified.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 C01B 25/16 B01D 53/36 102 H ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Internal reference number FI technical display location C01B 25/16 B01D 53/36 102 H

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】少なくとも銅(Cu)、ジルコニウム(Z
r)、リン(P)および酸素(O)を構成元素としてな
るリン酸系組成物であり、前記銅(Cu)、ジルコニウ
ム(Zr)およびリン(P)の原子比をx:y:zとし
た時、0.70≦y/z≦1、0.08≦x/(x+y
+z)≦0.16を満足することを特徴とするリン酸系
組成物。
1. At least copper (Cu), zirconium (Z
r), phosphorus (P) and oxygen (O) as constituent elements, wherein the atomic ratio of copper (Cu), zirconium (Zr) and phosphorus (P) is x: y: z. , 0.70 ≦ y / z ≦ 1, 0.08 ≦ x / (x + y
+ Z) ≦ 0.16 is satisfied, the phosphoric acid composition.
【請求項2】700〜1000℃における主結晶相がC
uZr4 (PO4 6相である請求項1記載のリン酸系
組成物。
2. The main crystal phase at 700 to 1000 ° C. is C
The phosphoric acid composition according to claim 1, which has a uZr 4 (PO 4 ) 6 phase.
【請求項3】少なくとも銅(Cu)、ジルコニウム(Z
r)、リン(P)および酸素(O)を構成元素としてな
るリン酸系組成物であり、前記銅(Cu)、ジルコニウ
ム(Zr)およびリン(P)の原子比をx:y:zとし
た時、0.70≦y/z≦1、0.08≦x/(x+y
+z)≦0.16を満足するリン酸系組成物からなるこ
とを特徴とするNOx還元分解用触媒。
3. At least copper (Cu), zirconium (Z
r), phosphorus (P) and oxygen (O) as constituent elements, wherein the atomic ratio of copper (Cu), zirconium (Zr) and phosphorus (P) is x: y: z. , 0.70 ≦ y / z ≦ 1, 0.08 ≦ x / (x + y
+ Z) ≦ 0.16, which is a phosphoric acid-based composition, and is a catalyst for NOx reduction decomposition.
JP6118413A 1994-05-31 1994-05-31 Phosphoric acid based composition and catalyst for reductive destructing nox using the same Pending JPH07323228A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6118413A JPH07323228A (en) 1994-05-31 1994-05-31 Phosphoric acid based composition and catalyst for reductive destructing nox using the same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6118413A JPH07323228A (en) 1994-05-31 1994-05-31 Phosphoric acid based composition and catalyst for reductive destructing nox using the same

Publications (1)

Publication Number Publication Date
JPH07323228A true JPH07323228A (en) 1995-12-12

Family

ID=14736037

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6118413A Pending JPH07323228A (en) 1994-05-31 1994-05-31 Phosphoric acid based composition and catalyst for reductive destructing nox using the same

Country Status (1)

Country Link
JP (1) JPH07323228A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000140642A (en) * 1998-11-11 2000-05-23 Toyota Central Res & Dev Lab Inc Catalyst for cleaning exhaust gas

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000140642A (en) * 1998-11-11 2000-05-23 Toyota Central Res & Dev Lab Inc Catalyst for cleaning exhaust gas

Similar Documents

Publication Publication Date Title
EP0320243B1 (en) Method of treating gaseous effluents with a catalyst containing cerium and copper oxides
JPH09173847A (en) Catalyst and its manufacture and use thereof
WO2008065819A1 (en) Composite oxide for exhaust gas clean-up catalyst, exhaust gas clean-up catalyst, and diesel exhaust gas clean-up filter
EP2269730B1 (en) Composite oxide for catalyst for exhaust gas purification, process for producing the same, catalyst for exhaust gas purification, and filter for diesel exhaust gas purification
JP2851773B2 (en) Oxide catalyst material for removing nitrogen oxides and method for removing nitrogen oxides
JPH07323228A (en) Phosphoric acid based composition and catalyst for reductive destructing nox using the same
JP3199562B2 (en) Oxide catalyst material for removing nitrogen oxides and method for removing nitrogen oxides
JPH0398644A (en) Preparation of catalyst for purifying exhaust gas
JP3152681B2 (en) Phosphoric acid composition and catalyst for NOx reductive decomposition using the same
JP3210748B2 (en) Phosphoric acid composition, method for producing the same, and catalyst for NOx reductive decomposition using the same
JP2922753B2 (en) Nitrogen oxide removal catalyst
JP3346653B2 (en) Oxide catalyst material for removing nitrogen oxides and method for removing nitrogen oxides
JP3532044B2 (en) Oxide catalyst material for removing nitrogen oxides and method for removing nitrogen oxides
JP3346665B2 (en) Oxide catalyst material for removing nitrogen oxides and method for removing nitrogen oxides
JP3152680B2 (en) Phosphoric acid composition and catalyst for NOx reductive decomposition using the same
JP2922759B2 (en) Oxide catalyst material for removing nitrogen oxides and method for removing nitrogen oxides
JPH08323204A (en) Oxide catalyst material and method for removing nitrogen oxide
JP3309024B2 (en) Oxide catalyst material for removing nitrogen oxides and method for removing nitrogen oxides
JP3199561B2 (en) Oxide catalyst material for removing nitrogen oxides and method for removing nitrogen oxides
JP2851769B2 (en) Oxide catalyst material for removing nitrogen oxides and method for removing nitrogen oxides
JPH09141102A (en) Oxide catalyst material for removing nitrogen oxide and removal of nitrogen oxide
JPH10180105A (en) Oxide catalyst material for removing nitrogen oxide and method for removing nitrogen oxide
JPH10180103A (en) Oxide catalyst material for removing nitrogen oxide and its preparation
JPH081002A (en) Oxide catalyst material for removing nitrogen oxide and removing method of nitrogen oxide
JPH09313941A (en) Oxide catalyst material for removing nitrogen oxide and removal of nitrogen oxide