JPH02169033A - Catalyst for combustion - Google Patents

Catalyst for combustion

Info

Publication number
JPH02169033A
JPH02169033A JP63320831A JP32083188A JPH02169033A JP H02169033 A JPH02169033 A JP H02169033A JP 63320831 A JP63320831 A JP 63320831A JP 32083188 A JP32083188 A JP 32083188A JP H02169033 A JPH02169033 A JP H02169033A
Authority
JP
Japan
Prior art keywords
catalyst
noble metal
particles
combustion
carrier
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
JP63320831A
Other languages
Japanese (ja)
Inventor
Masato Okada
真人 岡田
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.)
Tanaka Kikinzoku Kogyo KK
Original Assignee
Tanaka Kikinzoku Kogyo KK
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 Tanaka Kikinzoku Kogyo KK filed Critical Tanaka Kikinzoku Kogyo KK
Priority to JP63320831A priority Critical patent/JPH02169033A/en
Publication of JPH02169033A publication Critical patent/JPH02169033A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/50Fuel cells

Abstract

PURPOSE:To obtain a catalyst for combustion preventing the deterioration of activity and separation of noble metal particles from the carrier and having stable performance over a long period of of time of incorporating noble metal particles into the crystal lattice of a perovskite type multiple oxide and firmly fixing them. CONSTITUTION:A perovskite type multiple oxide is formed on an inorg. carrier such as silica or alumina with a first metal such as Ba, La or Sr, a second metal such as Co, Ni or Cr and a noble metal such as Pt or Pd. Since particles of the noble metal having catalytic activity are incorporated into the perovskite type multiple oxide as a constituent and fixed in the crystal lattice of the oxide, the separation of the particles from the carrier is prevented even under severe conditions including high temp. and the resulting catalyst maintains high catalytic activity over a long period of time.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、各種燃料の燃焼用触媒に関し、より詳細には
、本発明はメタンやプロパンのような気体燃料、又は液
化天然ガスや液化石油ガス、アルコール等の気化させた
液体燃料等を燃焼させるために使用する燃焼用触媒に関
する。
Detailed Description of the Invention (Field of Industrial Application) The present invention relates to a catalyst for combustion of various fuels, and more particularly, the present invention relates to a catalyst for combustion of various fuels. This invention relates to a combustion catalyst used to combust vaporized liquid fuel such as gas or alcohol.

(従来技術とその問題点) 従来から白金やパラジウム等の各種貴金属を無機質担体
上に担持させた貴金属触媒が燃料の燃料用触媒として広
く使用されている (例えば特開昭63−65951号
公報)。
(Prior art and its problems) Precious metal catalysts in which various noble metals such as platinum and palladium are supported on inorganic carriers have been widely used as fuel catalysts (for example, Japanese Patent Laid-Open No. 63-65951). .

従来の燃焼用触媒における触媒活性物質である貴金属粒
子は無機質担体上に単独で担持されている。通常白金、
パラジウム及びロジウム等の貴金属粒子は単独では耐熱
性に乏しく、該貴金属粒子を担持した燃焼用触媒上で酸
素の授受による燃焼反応が起こると、該酸素の吸着と脱
離の繰り返しにより前記貴金属粒子がシンタリングを起
こして劣化し、あるいは該貴金属粒子が高温に曝されて
揮発したり互いに凝集して活性が低下する。該貴金属粒
子を例えば他の粒子とともに合金等を形成して、前記担
体上で互いに弱い結合力で結合されている状態において
も同様に、前記貴金属粒子の劣化が生じ、触媒寿命の短
縮化つまり高価な貴金属の失活又は損失の原因となって
いる。
Noble metal particles, which are catalytically active substances in conventional combustion catalysts, are supported singly on an inorganic carrier. Usually platinum,
Particles of noble metals such as palladium and rhodium alone have poor heat resistance, and when a combustion reaction occurs on a combustion catalyst supporting the noble metal particles by supplying and receiving oxygen, the noble metal particles are repeatedly adsorbed and desorbed. Sintering occurs and deteriorates, or the noble metal particles are exposed to high temperatures and volatilize or aggregate with each other, resulting in a decrease in activity. Even when the noble metal particles are bonded to each other with a weak bonding force on the carrier by forming an alloy or the like with other particles, the noble metal particles similarly deteriorate, shortening the life of the catalyst and increasing the cost. This causes deactivation or loss of precious metals.

該欠点の解消のために資金、萬粒子を金属単体の状態の
まま担体上に強固に吸着させる方法の開発が続けられて
いるが、貴金属−無機質担体間の結合強度の上昇には限
界があり触媒寿命のある程度の長期化は図れても、飛躍
的な上昇には結びついていないのが現状である。
In order to overcome this drawback, efforts are being made to develop methods for firmly adsorbing metal particles onto a carrier in the form of a single metal, but there is a limit to increasing the bond strength between noble metals and inorganic carriers. Even if it is possible to extend the catalyst life to some extent, the current situation is that this has not led to a dramatic increase in catalyst life.

(発明の目的) 本発明は、上記欠点を解消するために、貴金属粒子が担
体上に強固に接合されて容易に脱離せず長期間に亘って
高い触媒活性を維持することが可能な燃焼用触媒を提供
することを目的とする。
(Object of the Invention) In order to eliminate the above-mentioned drawbacks, the present invention provides a combustion device in which noble metal particles are firmly bonded onto a carrier and are not easily desorbed and can maintain high catalytic activity over a long period of time. The purpose is to provide a catalyst.

(問題点を解決するた袷の手段) 本発明は、無機質担体上に、触媒成分として貴金属触媒
粒子を分散担持した活性酸化物を被覆して成る燃焼用触
媒において、前記貴金属触媒粒子が、バリウム、ランタ
ン、ストロンチウム、ネオジム及びセリウムより成る群
から選択される少なくとも1種の第1金属と、コバルト
、ニッケル、鉄、クロム及びモリブデンから成る群から
選択される少なくとも1種の第2金属とによりペロブス
カイト型複合酸化物を形成していることを特徴とする燃
焼用触媒である。
(Means for Solving the Problems) The present invention provides a combustion catalyst comprising an inorganic carrier coated with an active oxide in which noble metal catalyst particles are dispersedly supported as a catalyst component, in which the noble metal catalyst particles include barium. , lanthanum, strontium, neodymium and cerium, and at least one second metal selected from the group consisting of cobalt, nickel, iron, chromium and molybdenum to form a perovskite. This is a combustion catalyst characterized by forming a type composite oxide.

以下本発明の詳細な説明する。The present invention will be explained in detail below.

本発明では、貴金属粒子自体を担体上に吸着させるとい
う従来の触媒製造に関する考え方から離れ、触媒活性を
有する前記貴金属粒子を複合酸化物つまりペロブスカイ
ト型複合酸化物中にその構成要素として取り込み、該複
合酸化物の結晶格子中に固定して高温等の過酷な条件下
でも前記担体から脱離することがないようにしたことを
特徴とし、このように構成することにより該触媒の寿命
を飛躍的に向上させることを可能にしている。更に前記
ペロブスカイト型複合酸化物には酸素貯蔵効果があり、
これにより前記貴金属粒子が直接酸素と接触する割合が
減少して、前記劣化をより効果的に抑制することが可能
になる。
In the present invention, departing from the conventional concept of catalyst production in which noble metal particles themselves are adsorbed onto a carrier, the noble metal particles having catalytic activity are incorporated into a composite oxide, that is, a perovskite type composite oxide, as a component thereof, and the composite It is characterized by being fixed in the crystal lattice of the oxide so that it will not be detached from the carrier even under harsh conditions such as high temperatures, and this structure dramatically extends the life of the catalyst. It allows you to improve. Furthermore, the perovskite-type composite oxide has an oxygen storage effect,
This reduces the proportion of the noble metal particles that come into direct contact with oxygen, making it possible to more effectively suppress the deterioration.

本発明に使用する貴金属は、後述する第1及び第2金属
とともにペロブスカイト型複合酸化物を形成できれば特
に限定されず、白金、パラジウム、ロジウム、ルテニウ
ム等の任意の白金放念、@を使用することができる。
The noble metal used in the present invention is not particularly limited as long as it can form a perovskite-type composite oxide together with the first and second metals described below, and any platinum metal such as platinum, palladium, rhodium, and ruthenium may be used. Can be done.

又無機質担体も特に限定されず、アルミナ、シリカ、ジ
ルコニア、チタニア、アルミナ−シリカ、アルミナ−ジ
ルコニア、ジルコニア−シリカ等従来使用されているも
のを制限なく使用することができる。
Further, the inorganic carrier is not particularly limited, and conventionally used inorganic carriers such as alumina, silica, zirconia, titania, alumina-silica, alumina-zirconia, and zirconia-silica can be used without restriction.

前記貴金属粒子とともにペロブスカイト型複合酸化物を
形成する第1及び第2の金属は、それぞれバリウム、ラ
ンタン、ストロンチウム、ネオジム及びセリウムより成
る群、及びコバルト、ニッケル、鉄、クロム及びモリブ
デンから成る群から適宜選択される。
The first and second metals that form the perovskite-type composite oxide together with the noble metal particles are appropriately selected from the group consisting of barium, lanthanum, strontium, neodymium, and cerium, and the group consisting of cobalt, nickel, iron, chromium, and molybdenum. selected.

前記ペロブスカイト型複合酸化物は、通常化学式RMX
、で表される結晶構造を有し、RとMは前記第1又は第
2金属、Xは酸素を表す。該ペロブスカイト型複合酸化
物を調製するには、例えば前記貴金属を含有する各金属
の硝酸塩の混合溶液を形成し、該溶液を担体上に被覆し
、該被覆担体を熱処理して前記硝酸塩をそれぞれの金属
酸化物に変換して前記担体上にペロブスカイト型複合酸
化物を形成して所望の燃焼用触媒とすればよい。
The perovskite type composite oxide usually has the chemical formula RMX
, R and M represent the first or second metal, and X represents oxygen. In order to prepare the perovskite-type composite oxide, for example, a mixed solution of nitrates of each metal containing the noble metal is formed, the solution is coated on a carrier, and the coated carrier is heat-treated to dissolve the nitrates of each metal. A desired combustion catalyst may be obtained by converting it into a metal oxide and forming a perovskite-type composite oxide on the carrier.

このように調製された燃焼用触媒は、その触媒活性金属
である前記貴金属粒子がペロブスカイト型結晶構造中に
強固に固定され、かなり過酷な条件においても脱離や劣
化を起こすことがなく、長期間に亘って高活性で燃料の
燃焼を行うことができる触媒を提供することが可能にな
る。
In the combustion catalyst prepared in this way, the noble metal particles, which are the catalytically active metal, are firmly fixed in the perovskite crystal structure, and do not desorb or deteriorate even under extremely harsh conditions, and can last for a long period of time. It becomes possible to provide a catalyst that can burn fuel with high activity over a period of time.

(実施例) 以下本発明の実施例を記載するが、該実施例は本発明を
限定するものではない。
(Examples) Examples of the present invention will be described below, but these examples do not limit the present invention.

実施例1 ムライト担体上に5重単%の酸化ランタン及び5重工%
の酸化バリウムを含む活性アルミナを被覆し、次いで該
活性アルミナを硝酸ネオジム、硝酸ストロンチウム、硝
酸コバルト、硝酸パラジウムの混合溶液(モル比1 :
 1 : 1 : 1)に浸漬し、その後乾燥して80
0℃で熱処理して前記活性アルミナ上にパラジウムのペ
ロブスカイト型複合酸化物を形成して燃焼用触媒とした
Example 1 5% lanthanum oxide and 5% lanthanum oxide on mullite carrier
The activated alumina is then coated with a mixed solution of neodymium nitrate, strontium nitrate, cobalt nitrate, and palladium nitrate (molar ratio 1:
1:1:1) and then dried for 80 minutes.
A perovskite-type composite oxide of palladium was formed on the activated alumina by heat treatment at 0° C., and a combustion catalyst was obtained.

該触媒40gを用いてメタンの触媒燃焼反応を常圧下、
空気量801/分、触媒入ロガス流速10m/秒、燃焼
温度1300℃の条件で行ったところ、本実施例の触媒
は200時間にて清浄な1300℃の燃焼ガスを与えた
A catalytic combustion reaction of methane was carried out using 40 g of the catalyst under normal pressure.
When the test was carried out under the conditions of an air flow rate of 801/min, a flow rate of log gas entering the catalyst of 10 m/sec, and a combustion temperature of 1300°C, the catalyst of this example gave clean combustion gas of 1300°C in 200 hours.

比較例1 ムライト担体に活性アルミナを被覆し、次いで該活性ア
ルミナを硝酸パラジウム水溶液に浸漬し、乾燥し水素気
流中800℃で熱処理して燃焼用触媒を得た。この触媒
を実施例1と同様の条件下におけるメタン燃焼反応に使
用してところ、本比較例の触媒は20時間経過後に着火
不能となった。
Comparative Example 1 A mullite carrier was coated with activated alumina, and then the activated alumina was immersed in an aqueous palladium nitrate solution, dried, and heat-treated at 800° C. in a hydrogen stream to obtain a combustion catalyst. When this catalyst was used in a methane combustion reaction under the same conditions as in Example 1, the catalyst of this comparative example became unable to ignite after 20 hours.

実施例2 硝酸パラジウムに換えてジニトロジアンミン白金硝酸水
溶液を使用したこと以外は実施例1と同一条件で活性ア
ルミナ上に白金を含有するペロブスカイト型複合酸化物
を形成して燃焼用触媒とした。
Example 2 A perovskite-type composite oxide containing platinum was formed on activated alumina under the same conditions as in Example 1, except that a dinitrodiammine platinum nitric acid aqueous solution was used in place of palladium nitrate, and a combustion catalyst was prepared.

該触媒40gを用いてプロパンの触媒燃焼反応を実施例
1と同一条件で行ったところ、200時間に亘って清浄
な1300℃の燃焼ガスを与えた。
When a catalytic combustion reaction of propane was carried out using 40 g of the catalyst under the same conditions as in Example 1, clean combustion gas at 1300° C. was provided for 200 hours.

比較例2 硝酸パラジウム水溶液に換えてジニトロジアンミン白金
硝酸水溶液を使用しかつ水素気流中での処理に換えて大
気中の処理としたこと以外は比較例1と同一条件で白金
含有触媒を得、該触媒を比較例1と同一条件でプロパン
燃焼に使用したところ、本比較例の触媒は20時間経過
後に着火不能となった。
Comparative Example 2 A platinum-containing catalyst was obtained under the same conditions as Comparative Example 1, except that a dinitrodiammine platinum nitric acid aqueous solution was used instead of the palladium nitrate aqueous solution, and the treatment was performed in the atmosphere instead of in a hydrogen stream. When the catalyst was used for propane combustion under the same conditions as Comparative Example 1, the catalyst of this Comparative Example became unable to ignite after 20 hours.

実施例3 硝酸パラジウムに換えて硝酸ロジウムを使用したこと以
外は実施例1と同一条件で活性アルミナ上にロジウムを
含有するペロブスカイト型複合酸化物を形成して燃焼用
触媒とした。
Example 3 A perovskite-type composite oxide containing rhodium was formed on activated alumina under the same conditions as in Example 1, except that rhodium nitrate was used instead of palladium nitrate, and a combustion catalyst was prepared.

該触媒40gを用いてメタンの触媒燃焼反応を実施例1
と同一条件で行ったところ、200時間に亘って清浄な
1300℃の燃焼ガスを与えた。
Example 1: Catalytic combustion reaction of methane using 40 g of the catalyst
When conducted under the same conditions as above, clean combustion gas at 1300° C. was provided for 200 hours.

比較例3 硝酸パラジウム水溶液に換えて硝酸ロジウム水溶液を使
用したこと以外は比較例1と同一条件でロジウム含有触
媒を得、該触媒を比較例1と同一条件でメタン燃焼に使
用したところ、本比較例の触媒は20時間経過後に着火
不能となった。
Comparative Example 3 A rhodium-containing catalyst was obtained under the same conditions as Comparative Example 1 except that an aqueous rhodium nitrate solution was used instead of an aqueous palladium nitrate solution, and this catalyst was used for methane combustion under the same conditions as Comparative Example 1. The catalyst in the example failed to ignite after 20 hours.

(発明の効果) 本発明に係わる燃焼用触媒は、従来の貴金属触媒粒子を
担体上にそのまま担持させるという着想から離れ、該貴
金属触媒粒子をペロブスカイト型複合酸化物の結晶格子
中に取り込み該格子中に強固に固定することにより、該
粒子の劣化や脱離を効果的に防止し、長期間に亘って安
定した触媒性能を有する燃焼用触媒を提供しようとする
ものであてる。
(Effects of the Invention) The combustion catalyst according to the present invention departs from the conventional idea of supporting noble metal catalyst particles on a carrier as they are, and incorporates the noble metal catalyst particles into the crystal lattice of a perovskite-type composite oxide. By firmly fixing the particles, deterioration and detachment of the particles can be effectively prevented, and a combustion catalyst having stable catalytic performance over a long period of time can be provided.

つまり通常の燃焼反応では担体表面での酸素の吸着及び
脱離が非常に頻繁に起こり、従来の燃焼用触媒では触媒
活性を有する貴金属触媒粒子が前記担体上に強固に固定
されていないため前記酸素の脱離とともに前記担体から
脱離したり、あるいは吸着酸素により損傷を受けて触媒
活性が低下したり又は前記貴金属粒子同志が凝集して活
性態下を招くといった事態が生じていたのである。
In other words, in normal combustion reactions, adsorption and desorption of oxygen on the carrier surface occur very frequently, and in conventional combustion catalysts, the noble metal catalyst particles with catalytic activity are not firmly fixed on the carrier, so the oxygen The noble metal particles may be detached from the support along with the detachment of the noble metal particles, or the catalyst may be damaged by adsorbed oxygen, resulting in a decrease in catalytic activity, or the noble metal particles may aggregate with each other, leading to an underactive state.

これに対し、本発明に係わる燃焼用触媒では、触媒活性
を有する貴金属触媒粒子がペロブスカイト複合酸化物の
結晶格子中に取り込まれているため、前記結晶格子が破
壊されない限り前記貴金属触媒粒子が担体から脱離する
ことがなく、しかも前記格子中で酸素等の隣接原子と強
固な結合を有しているため、吸着酸素による影響を受け
ることが殆どなく、更に安定性が向上し、該貴金属触媒
粒子自体が存する触媒活性を長期間に亘って維持するこ
とが可能になる。
On the other hand, in the combustion catalyst according to the present invention, since the noble metal catalyst particles having catalytic activity are incorporated into the crystal lattice of the perovskite composite oxide, the noble metal catalyst particles are removed from the carrier unless the crystal lattice is destroyed. Since it does not desorb and has strong bonds with adjacent atoms such as oxygen in the lattice, it is hardly affected by adsorbed oxygen, further improving the stability of the precious metal catalyst particles. It becomes possible to maintain the existing catalytic activity for a long period of time.

Claims (2)

【特許請求の範囲】[Claims] (1)無機質担体上に、触媒成分として貴金属触媒粒子
を分散担持した活性酸化物を被覆して成る燃焼用触媒に
おいて、前記貴金属触媒粒子が、バリウム、ランタン、
ストロンチウム、ネオジム及びセリウムより成る群から
選択される少なくとも1種の第1金属と、コバルト、ニ
ッケル、鉄、クロム及びモリブデンから成る群から選択
される少なくとも1種の第2金属とによりペロブスカイ
ト型複合酸化物を形成していることを特徴とする燃焼用
触媒。
(1) A combustion catalyst comprising an inorganic carrier coated with an active oxide having noble metal catalyst particles dispersed thereon as a catalyst component, wherein the noble metal catalyst particles include barium, lanthanum,
Perovskite-type complex oxidation with at least one first metal selected from the group consisting of strontium, neodymium, and cerium and at least one second metal selected from the group consisting of cobalt, nickel, iron, chromium, and molybdenum. A combustion catalyst characterized by forming a substance.
(2)貴金属触媒粒子が、パラジウム、白金及びロジウ
ムから選択される少なくとも1種である請求項1に記載
の燃焼用触媒。
(2) The combustion catalyst according to claim 1, wherein the noble metal catalyst particles are at least one selected from palladium, platinum, and rhodium.
JP63320831A 1988-12-20 1988-12-20 Catalyst for combustion Pending JPH02169033A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63320831A JPH02169033A (en) 1988-12-20 1988-12-20 Catalyst for combustion

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63320831A JPH02169033A (en) 1988-12-20 1988-12-20 Catalyst for combustion

Publications (1)

Publication Number Publication Date
JPH02169033A true JPH02169033A (en) 1990-06-29

Family

ID=18125724

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63320831A Pending JPH02169033A (en) 1988-12-20 1988-12-20 Catalyst for combustion

Country Status (1)

Country Link
JP (1) JPH02169033A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006090907A1 (en) * 2005-02-24 2006-08-31 Toyota Jidosha Kabushiki Kaisha Catalyst for fuel cell, membrane electrode assembly, and solid polymer electrolyte fuel cell
JP2010238546A (en) * 2009-03-31 2010-10-21 Equos Research Co Ltd Fine particle carrying metal oxide catalyst, its manufacturing method, and electrode for fuel cell
CN110327938A (en) * 2019-07-30 2019-10-15 苏州卡泰里环保能源有限公司 Catalytic combustion catalyst with core-shell structure and preparation method thereof
CN111644183A (en) * 2020-05-12 2020-09-11 五邑大学 IrO-containing2Preparation method and application of perovskite oxide

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006090907A1 (en) * 2005-02-24 2006-08-31 Toyota Jidosha Kabushiki Kaisha Catalyst for fuel cell, membrane electrode assembly, and solid polymer electrolyte fuel cell
US8815470B2 (en) 2005-02-24 2014-08-26 Toyota Jidosha Kabushiki Kaisha Fuel cell catalyst, membrane electrode assembly and solid polymer electrolyte fuel cell
JP2010238546A (en) * 2009-03-31 2010-10-21 Equos Research Co Ltd Fine particle carrying metal oxide catalyst, its manufacturing method, and electrode for fuel cell
CN110327938A (en) * 2019-07-30 2019-10-15 苏州卡泰里环保能源有限公司 Catalytic combustion catalyst with core-shell structure and preparation method thereof
CN110327938B (en) * 2019-07-30 2022-05-13 苏州卡泰里环保能源有限公司 Catalytic combustion catalyst with core-shell structure and preparation method thereof
CN111644183A (en) * 2020-05-12 2020-09-11 五邑大学 IrO-containing2Preparation method and application of perovskite oxide
CN111644183B (en) * 2020-05-12 2023-07-28 五邑大学 IrO-containing material 2 Preparation method and application of perovskite oxide

Similar Documents

Publication Publication Date Title
JP2979809B2 (en) Exhaust gas purification catalyst and method for producing the same
JP5226633B2 (en) Engine exhaust gas catalyst containing palladium-gold
KR101155847B1 (en) Exhaust gas purifying catalyst
EP1332787A1 (en) Catalyst for purifying exhaust gases
JP2773428B2 (en) Exhaust gas purification method
JPH0838897A (en) Production of exhaust gas purifying catalyst
JP2006055748A (en) Manufacturing method for catalyst
KR101524054B1 (en) A catalyst for purifying exhaust gas from combustions sytems using CNG as fuel
JP2008114153A (en) Catalyst for purification of exhaust gas and system and method for purification of exhaust gas
JP3216858B2 (en) Exhaust gas purification catalyst and method for producing the same
JP6107487B2 (en) N2O decomposition catalyst and N2O-containing gas decomposition method using the same
JPH02169033A (en) Catalyst for combustion
JPH03106446A (en) Catalyst for purifying exhaust gas and preparation thereof
JP3532979B2 (en) Exhaust gas purification catalyst
JP5094049B2 (en) Exhaust gas purification catalyst
JP6296412B2 (en) Exhaust gas purification system and exhaust gas purification method
JP3335755B2 (en) Exhaust gas purification catalyst
JP2006035043A (en) Catalyst for purifying exhaust gas
US20040156771A1 (en) Method of reducing carbon monoxide concentration
JPH04122447A (en) Catalyst for cleaning exhaust gas
JPH02166305A (en) Combustion method for fuel
JPH0398644A (en) Preparation of catalyst for purifying exhaust gas
KR100736703B1 (en) A catalyst with double-layers for improving oxidation activity for diesel exhaust gases
JP2531677B2 (en) Exhaust gas purification catalyst
JPH0356140A (en) Catalyst for purifying exhaust gas