JP3336345B2 - Palladium-lanthanum composite oxide catalyst and supported catalyst - Google Patents

Palladium-lanthanum composite oxide catalyst and supported catalyst

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Publication number
JP3336345B2
JP3336345B2 JP08476791A JP8476791A JP3336345B2 JP 3336345 B2 JP3336345 B2 JP 3336345B2 JP 08476791 A JP08476791 A JP 08476791A JP 8476791 A JP8476791 A JP 8476791A JP 3336345 B2 JP3336345 B2 JP 3336345B2
Authority
JP
Japan
Prior art keywords
palladium
catalyst
lanthanum
composite oxide
supported
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
JP08476791A
Other languages
Japanese (ja)
Other versions
JPH04341343A (en
Inventor
雅宏 佐々木
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.)
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 JP08476791A priority Critical patent/JP3336345B2/en
Publication of JPH04341343A publication Critical patent/JPH04341343A/en
Application granted granted Critical
Publication of JP3336345B2 publication Critical patent/JP3336345B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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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、燃焼触媒等に使用され
るパラジウム酸化物系の触媒に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a palladium oxide catalyst used for a combustion catalyst or the like.

【0002】[0002]

【従来の技術とその問題点】従来、酸化触媒としては、
アルミナ等の高表面積担体をコージライトハニカムに5
0〜100g/lウオシュコートしたものに、含浸法、
イオン交換法等を用い、担体のアルミナに対しパラジウ
ムを5〜20wt%担持したものが主に触媒として使用
されていた。しかし、担持したパラジウムは酸化パラジ
ウムとなって初めて酸化触媒としての活性を示すことは
すでに知られているが、酸化パラジウムは800℃以上
では分解して金属パラジウムとなり酸素を放出し、酸化
触媒としての活性を失ってしまうため、800℃以上の
酸化触媒としては適用することができなかった。
2. Description of the Related Art Conventional oxidation catalysts include:
A high surface area carrier such as alumina is used for cordierite honeycomb.
0-100 g / l washcoat, impregnation method,
What carried out 5-20 wt% of palladium with respect to the support | carrier alumina using the ion exchange method etc. was mainly used as a catalyst. However, it is already known that the supported palladium exhibits the activity as an oxidation catalyst only after it becomes palladium oxide. Since the catalyst loses its activity, it cannot be used as an oxidation catalyst at 800 ° C. or higher.

【0003】[0003]

【発明の目的】本発明は、従来の酸化パラジウム触媒の
欠点を解決するために成されたもので、酸化触媒として
極めて活性をしめす酸化パラジウムを改良して800℃
以上の酸化触媒として使用に耐える酸化触媒を提供する
ことを目的とする。
SUMMARY OF THE INVENTION The present invention has been made to solve the drawbacks of the conventional palladium oxide catalysts.
An object of the present invention is to provide an oxidation catalyst that can be used as the above oxidation catalyst.

【0004】[0004]

【課題を解決するための手段】本発明は、酸化パラジウ
ムと酸化ランタンの割合が1:2〜2:1のmol比で
成るパラジウム−ランタン系複合酸化物触媒であり、担
体に予め、アルミナ又はアルミナに1種以上の希土類金
属及びアルカリ土類金属を含有するもの、あるいはジル
コニア又はジルコニアに1種以上の希土類金属及びアル
カリ土類金属を含有するものでウオシュコートしてお
き、それに前記パラジウム−ランタン系複合酸化物触媒
を担持した担持触媒である。
The present invention relates to a palladium-lanthanum-based composite oxide catalyst in which the ratio of palladium oxide to lanthanum oxide is 1: 2 to 2: 1 by mole, wherein alumina or Alumina containing one or more rare earth metals and alkaline earth metals, or zirconia or zirconia containing one or more rare earth metals and alkaline earth metals, is wash-coated, and the palladium-lanthanum-based This is a supported catalyst supporting a composite oxide catalyst.

【0005】酸化パラジウムと酸化ランタンの割合が
1:2〜2:1のmol比とするのは、酸化パラジウム
の酸化触媒としての活性を低下させずしかも燃焼触媒と
してメタン等の燃焼温度でも耐えることのできる触媒と
するためである。該割合のパラジウム−ランタン系複合
酸化物触媒は、1100〜1200℃の温度に耐えて活
性を維持させることができる。
The reason that the molar ratio of palladium oxide to lanthanum oxide is 1: 2 to 2: 1 is that the activity of palladium oxide as an oxidation catalyst is not reduced and the palladium oxide can withstand a combustion temperature of methane or the like as a combustion catalyst. This is because the catalyst can be used. The palladium-lanthanum-based composite oxide catalyst in this ratio can withstand temperatures of 1100 to 1200 ° C. and maintain its activity.

【0006】また、前記パラジウム−ランタン系複合酸
化物触媒を担持する担体にアルミナ又はアルミナに1種
以上の希土類金属及びアルカリ土類金属を含有するも
の、あるいはジルコニア又はジルコニアに1種以上の希
土類金属及びアルカリ土類金属を含有するものをウオシ
ュコートしておくとするのは、前記の1100〜120
0℃の温度に耐える担体であり、しかも触媒を有効に利
用させるための高表面積を得られるもので、さらにパラ
ジウム−ランタン系複合酸化物触媒を担持した際に強固
に担持させることができるためである。
Further, a carrier supporting the palladium-lanthanum composite oxide catalyst contains alumina or alumina containing at least one rare earth metal and an alkaline earth metal, or zirconia or zirconia contains one or more rare earth metals. And those containing an alkaline earth metal are wash-coated in the above-described range from 1100 to 120
It is a carrier that can withstand a temperature of 0 ° C., and can provide a high surface area for effectively utilizing the catalyst, and can be firmly supported when a palladium-lanthanum-based composite oxide catalyst is supported. is there.

【0007】以下、本発明をより詳しく説明するために
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。
Hereinafter, the present invention will be described in more detail with reference to Examples, but the Examples do not limit the present invention.

【0008】[0008]

【実施例1】ランタニウムアセテート1.3gと塩化パ
ラジウム2.6gを蒸留水に溶かし、それに予め長さ2
5mm×20mm径のコージェライトハニカム担体にア
ルミナを100g/lウオシュコートしておいた担体を
浸す。次いで、該担体を取り出し、100℃で30分間
乾燥させ、その後、750℃で3時間焼成して、パラジ
ウムとして0.16g、ランタンとして0.05gを担
持したパラジウム−ランタン系複合酸化物触媒を担持し
た担持触媒を得た。酸化触媒としてのテストはメタンの
燃焼によって行い、メタンの完全燃焼F/A比は10時
間以上継続させることができた、また、燃焼温度を測定
したところ1050℃であった。別に、前記担持触媒の
触媒活性の有効な温度を燃焼試験で確認したところ11
05℃まで酸化触媒として活性を示した。
EXAMPLE 1 1.3 g of lanthanum acetate and 2.6 g of palladium chloride were dissolved in distilled water, and a length of
A carrier coated with a 100 g / l alumina washcoat of alumina is immersed in a cordierite honeycomb carrier having a diameter of 5 mm × 20 mm. Next, the carrier was taken out, dried at 100 ° C. for 30 minutes, and then calcined at 750 ° C. for 3 hours to carry a palladium-lanthanum composite oxide catalyst supporting 0.16 g as palladium and 0.05 g as lanthanum. A supported catalyst was obtained. The test as an oxidation catalyst was carried out by combustion of methane. The complete combustion F / A ratio of methane could be maintained for 10 hours or more, and the combustion temperature was measured to be 1050 ° C. Separately, when the effective temperature of the catalytic activity of the supported catalyst was confirmed by a combustion test,
It showed activity as an oxidation catalyst up to 05 ° C.

【0009】[0009]

【実施例2】ランタニウムアセテート5.2gと塩化パ
ラジウム2.6gを蒸留水50mlに溶かし、それに予
め長さ25mm×20mm径のコージェライトハニカム
担体にアルミナを100g/lウオシュコートしておい
た担体を浸す。次いで、該担体を取り出し、100℃で
30分間乾燥させ、その後、750℃で3時間焼成し
て、パラジウムとして0.16g、ランタンとして0.
21gを担持したパラジウム−ランタン系複合酸化物触
媒を担持した担持触媒を得た。酸化触媒としてのテスト
はメタンの燃焼によって行い、メタンの完全燃焼は15
時間以上継続させることができた、また、燃焼温度を測
定したところ1150℃であった。別に、前記担持触媒
の触媒活性の有効な温度を燃焼試験で確認したところ1
190℃まで酸化触媒として活性を示した。
Example 2 5.2 g of lanthanum acetate and 2.6 g of palladium chloride were dissolved in 50 ml of distilled water, and a carrier coated with a cordierite honeycomb carrier having a length of 25 mm × 20 mm in advance and a wash coat of alumina at 100 g / l was used. Soak. Next, the carrier was taken out, dried at 100 ° C. for 30 minutes, and then calcined at 750 ° C. for 3 hours to obtain 0.16 g of palladium and 0.1 g of lanthanum.
A supported catalyst supporting a palladium-lanthanum-based composite oxide catalyst supporting 21 g was obtained. The test as an oxidation catalyst was carried out by combustion of methane.
It could be continued for more than an hour, and the combustion temperature was measured to be 1150 ° C. Separately, the effective temperature of the catalyst activity of the supported catalyst was confirmed by a combustion test.
It showed activity as an oxidation catalyst up to 190 ° C.

【0010】[0010]

【従来例】ランタニウムアセテートを加えず、塩化パラ
ジウムの量を2.6gとした以外実施例1と同様に操作
して酸化パラジウム担持触媒を調製し、これを酸化触媒
としてのテストはメタンの燃焼によって行い、メタンの
完全燃焼は1時間ももたず止まり、温度が低下してから
再び燃焼するという変化が見られた。
Conventional Example A palladium oxide-supported catalyst was prepared in the same manner as in Example 1 except that lanthanum acetate was not added and the amount of palladium chloride was changed to 2.6 g. The complete combustion of methane was stopped in less than one hour, and the temperature was lowered and the fuel was burned again.

【0011】[0011]

【発明の効果】以上の説明から明らかのように、本発明
のパラジウム−ランタン系複合酸化物触媒及び担持触媒
によれば、従来酸化触媒として有効な酸化パラジウムの
みでは使用することのできなかった800℃以上の温度
に対しても活性を低下させることがほとんどなく、約1
200℃程度の高い温度にも耐えるもので、特にメタン
等の燃焼触媒として利用することが可能となり、その利
用範囲が拡大させることができる画期的なものと言え
る。
As is apparent from the above description, according to the palladium-lanthanum-based composite oxide catalyst and the supported catalyst of the present invention, 800 palladium oxide, which was conventionally effective only as an effective oxidation catalyst, could not be used. The activity hardly decreases even at a temperature of at least
It can withstand a high temperature of about 200 ° C., and can be used as a combustion catalyst particularly for methane and the like.

フロントページの続き (56)参考文献 特開 昭63−88041(JP,A) 特開 平4−27433(JP,A) 特開 昭62−216642(JP,A) 特開 昭62−149343(JP,A) 特開 昭63−296842(JP,A) 特開 昭61−209045(JP,A) 特開 昭62−282642(JP,A) (58)調査した分野(Int.Cl.7,DB名) B01J 21/00 - 38/74 Continuation of the front page (56) References JP-A-63-88041 (JP, A) JP-A-4-27433 (JP, A) JP-A-62-121642 (JP, A) JP-A-62-149343 (JP) JP-A-63-296842 (JP, A) JP-A-61-209045 (JP, A) JP-A-62-282642 (JP, A) (58) Fields studied (Int. Cl. 7 , DB Name) B01J 21/00-38/74

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 パラジウムとランタンの原子比が1:1
〜1:4であるパラジウム−ランタン含有複合酸化物
らなることを特徴とする燃焼触媒。
1. An atomic ratio of palladium to lanthanum of 1: 1.
To 1: Palladium is a 4 - or lanthanum-containing composite oxide
Combustion catalyst, characterized in that Ranaru.
【請求項2】 担体に予め、アルミナ又はアルミナに1
種以上の希土類金属及びアルカリ土類金属を含有するも
の、あるいはジルコニア又はジルコニアに1種以上の希
土類金属及びアルカリ土類金属を含有するものでウオシ
ュコートを施し、それにパラジウムとランタンの原子比
が1:1〜1:4であるパラジウム−ランタン含有複合
酸化物を担持したことを特徴とする燃焼触媒。
2. A method in which alumina or alumina is added to the carrier in advance.
A washcoat is applied with one or more rare earth metals and alkaline earth metals, or zirconia or zirconia containing one or more rare earth metals and alkaline earth metals, wherein the atomic ratio of palladium to lanthanum is 1: A combustion catalyst comprising a palladium-lanthanum-containing composite oxide of 1 to 1: 4 supported thereon.
JP08476791A 1991-03-25 1991-03-25 Palladium-lanthanum composite oxide catalyst and supported catalyst Expired - Lifetime JP3336345B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP08476791A JP3336345B2 (en) 1991-03-25 1991-03-25 Palladium-lanthanum composite oxide catalyst and supported catalyst

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP08476791A JP3336345B2 (en) 1991-03-25 1991-03-25 Palladium-lanthanum composite oxide catalyst and supported catalyst

Publications (2)

Publication Number Publication Date
JPH04341343A JPH04341343A (en) 1992-11-27
JP3336345B2 true JP3336345B2 (en) 2002-10-21

Family

ID=13839834

Family Applications (1)

Application Number Title Priority Date Filing Date
JP08476791A Expired - Lifetime JP3336345B2 (en) 1991-03-25 1991-03-25 Palladium-lanthanum composite oxide catalyst and supported catalyst

Country Status (1)

Country Link
JP (1) JP3336345B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3843090B2 (en) 2003-09-12 2006-11-08 本田技研工業株式会社 Exhaust gas purification catalyst, method for producing the same, and exhaust gas purification catalyst device for vehicles
CA2581339C (en) 2004-09-24 2010-11-02 Honda Motor Co., Ltd. Catalyst for exhaust gas purification and exhaust gas purification apparatus

Also Published As

Publication number Publication date
JPH04341343A (en) 1992-11-27

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