JPH0538448A - Catalyst composition - Google Patents
Catalyst compositionInfo
- Publication number
- JPH0538448A JPH0538448A JP3199111A JP19911191A JPH0538448A JP H0538448 A JPH0538448 A JP H0538448A JP 3199111 A JP3199111 A JP 3199111A JP 19911191 A JP19911191 A JP 19911191A JP H0538448 A JPH0538448 A JP H0538448A
- Authority
- JP
- Japan
- Prior art keywords
- oxide
- catalyst
- catalyst composition
- rare earth
- 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
Links
Landscapes
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
- Catalysts (AREA)
Abstract
(57)【要約】
【目的】 本発明は500℃以上の高温で還元性雰囲気
中においても触媒活性の低下しない耐久性の優れた触媒
組成物が得られることを目的とする。
【構成】 希土類元素を含有するペロブスカイト型複合
酸化物と希土類酸化物と酸化アルミニウムと酸化鉄、及
びカルシウムまたはバリウムのうち1種以上の酸化物、
さらに貴金属のうちの1種以上からなる組成物とするこ
とにより耐久性の優れた触媒組成物を得る。(57) [Summary] [Object] An object of the present invention is to obtain a catalyst composition having excellent durability, in which the catalytic activity does not decrease even in a reducing atmosphere at a high temperature of 500 ° C or higher. [Composition] A perovskite-type composite oxide containing a rare earth element, a rare earth oxide, aluminum oxide, iron oxide, and one or more oxides of calcium or barium,
Furthermore, a catalyst composition having excellent durability is obtained by using a composition comprising at least one kind of noble metal.
Description
【0001】[0001]
【産業上の利用分野】本発明は排ガス中に含まれる炭化
水素(HC)、一酸化炭素(CO)及び窒素酸化物(N
Ox )を酸化または還元反応により水、炭酸ガス及び窒
素に変換する排ガス浄化用触媒体等に用いられる触媒組
成物に関する。TECHNICAL FIELD The present invention relates to hydrocarbon (HC), carbon monoxide (CO) and nitrogen oxide (N) contained in exhaust gas.
The present invention relates to a catalyst composition used for an exhaust gas purifying catalyst or the like that converts O x ) into water, carbon dioxide gas and nitrogen by an oxidation or reduction reaction.
【0002】[0002]
【従来の技術】従来のこの種の触媒組成物としては希土
類元素の酸化物とペロブスカイト型複合酸化物とパラジ
ウムからなるもの(特開昭58−156349号公報)
や表面にペロブスカイト型複合酸化物とO2 ストレージ
性希土類酸化物を含む層を設けた触媒担体に、パラジウ
ムまたはパラジウムと他の貴金属を触媒成分として担持
せしめたもの(特開昭59−162948号公報)があ
った。2. Description of the Related Art A conventional catalyst composition of this type comprises an oxide of a rare earth element, a perovskite complex oxide and palladium (Japanese Patent Laid-Open No. 156349/1983).
And palladium or palladium and other noble metals supported as catalyst components on a catalyst carrier having a layer containing a perovskite type complex oxide and an O 2 storage rare earth oxide on its surface or the surface (JP-A-59-162948). )was there.
【0003】[0003]
【発明が解決しようとする課題】しかしながら上記従来
の触媒組成物は200℃以上の高温の還元性雰囲気中で
長時間使用するとパラジウムなどの貴金属が粒成長を起
こしたり、ペロブスカイト型複合酸化物中に拡散したり
して触媒活性が次第に低下するなど耐久性が劣るという
課題があった。However, when the above conventional catalyst composition is used for a long time in a reducing atmosphere at a temperature of 200 ° C. or higher, noble metal such as palladium causes grain growth, and the perovskite type complex oxide is contained in the noble metal. However, there is a problem that durability deteriorates because the catalyst activity gradually decreases due to diffusion.
【0004】本発明は上記課題を解決するもので、耐久
性の優れた触媒組成物の提供を目的とする。The present invention has been made to solve the above problems, and an object thereof is to provide a catalyst composition having excellent durability.
【0005】[0005]
【課題を解決するための手段】上記目的を達成するため
本発明の触媒組成物は希土類元素を含有するペロブスカ
イト型複合酸化物と希土類酸化物と酸化アルミニウム、
酸化鉄、及びカルシウムまたはバリウムのうちの1種以
上の酸化物さらに貴金属のうちの1種以上からなる。To achieve the above object, the catalyst composition of the present invention comprises a perovskite complex oxide containing a rare earth element, a rare earth oxide, and aluminum oxide.
It comprises iron oxide and one or more oxides of calcium or barium and one or more of noble metals.
【0006】[0006]
【作用】本発明は、上記構成によって500℃以上の高
温雰囲気中においても貴金属の粒成長やペロブスカイト
複合酸化物中への拡散を抑制する。According to the present invention, grain growth of noble metal and diffusion into the perovskite complex oxide are suppressed even in a high temperature atmosphere of 500 ° C. or higher.
【0007】[0007]
【実施例】以下本発明の実施例を説明する。EXAMPLES Examples of the present invention will be described below.
【0008】La0.9Ce0.1CoO3 の希土類元
素を含有するペロブスカイト型複合酸化物の粉末100
g、酸化セリウム(CeO2 )の粉末100g、アルミ
ナゾル(酢酸酸性、固形分1/10)50g、硝酸パラ
ジウム〔Pd(NO3 )2 〕0.9gと硝酸鉄〔Fe
(NO3 )2 〕4.5g、硝酸バリウム〔Ba(N
O3 )2 〕4.2g及び水150gを混合攪はんしてス
ラリーを調整した。上記スラリー中に断面が格子状の4
00セル/(インチ)2 のコーディエライト(2MgO
・5SiO2 ・2A12 O3 )製のハニカム担体を浸漬
し、引き上げたのち気流により余分なスラリーを吹き払
った。その後担体が200℃で1時間乾燥し、650℃
で1時間焼成して触媒組成物が約24重量%、担体が約
76重量%の触媒体を得た。ここで触媒組成物中のペロ
ブスカイト型複合酸化物は47.8重量%、酸化アルミ
ニウムは2.40重量%、パラジウムは0.27重量
%、酸化鉄は0.28重量%、酸化バリウムは0.56
重量%であった。Perovskite type complex oxide powder 100 containing a rare earth element of La0.9Ce0.1CoO 3 100
g, cerium oxide (CeO 2 ) powder 100 g, alumina sol (acetic acid acidity, solid content 1/10) 50 g, palladium nitrate [Pd (NO 3 ) 2 ] 0.9 g and iron nitrate [Fe
(NO 3 ) 2 ] 4.5 g, barium nitrate [Ba (N
O 3 ) 2 ] 4.2 g and 150 g of water were mixed and stirred to prepare a slurry. Cross section of the slurry is 4
00 cells / (inch) 2 cordierite (2MgO
A honeycomb carrier made of 5SiO 2 · 2A1 2 O 3 ) was dipped and pulled up, and then excess slurry was blown off by an air stream. The carrier is then dried at 200 ° C for 1 hour and 650 ° C.
After being calcined for 1 hour, a catalyst body having a catalyst composition of about 24 wt% and a carrier of about 76 wt% was obtained. Here, 47.8% by weight of the perovskite-type composite oxide, 2.40% by weight of aluminum oxide, 0.27% by weight of palladium, 0.28% by weight of iron oxide, and 0.20% by weight of barium oxide in the catalyst composition. 56
% By weight.
【0009】比較例としてペロブスカイト型複合酸化物
と酸化セリウムと酸化アルミニウムとパラジウムからな
る触媒組成物を担持した触媒体(比較例1)及びペロブ
スカイト型複合酸化物とパラジウムからなる触媒組成物
を担持した触媒体(比較例2)を作製した。As a comparative example, a catalyst body carrying a catalyst composition comprising perovskite type composite oxide, cerium oxide, aluminum oxide and palladium (Comparative Example 1) and a catalyst composition comprising perovskite type complex oxide and palladium were carried. A catalyst body (Comparative Example 2) was produced.
【0010】上記で作製した3種類の触媒体について触
媒性能の初期特性と耐久性を比較した。試験条件は次の
通りであり、試験結果を表1に示す。The initial characteristics of catalyst performance and durability of the three types of catalyst bodies produced above were compared. The test conditions are as follows, and the test results are shown in Table 1.
【0011】[0011]
【表1】 [Table 1]
【0012】触媒性能試験条件 ガス組成(容量基準) NO1%、CO1%、ヘリウム98%で構成される反応
ガスを用いた。 空間速度:12500/Hr 測定方法 固定床流通式により反応を行いガスクロマ
トグラフィーによりNOのN2 への転換率をもとめた。 反応温度は300℃である。同表より、触媒性能の耐久
性に対しては酸化鉄、及び酸化バリウムの存在が必須で
あることが明らかである。Catalyst Performance Test Conditions Gas composition (volume basis) A reaction gas composed of 1% NO, 1% CO and 98% helium was used. Space velocity: 12500 / Hr Measuring method The reaction was carried out by a fixed bed flow system, and the conversion rate of NO to N 2 was determined by gas chromatography. The reaction temperature is 300 ° C. From the table, it is clear that the presence of iron oxide and barium oxide is essential for the durability of the catalyst performance.
【0013】次に上記3種類の触媒体について触媒性能
の経時変化を測定すると図1に示す結果が得られた。同
図より、本実施例の触媒体は優れた耐久性を示した。Next, when the time-dependent changes in the catalyst performance of the above three types of catalyst bodies were measured, the results shown in FIG. 1 were obtained. From the figure, the catalyst body of this example showed excellent durability.
【0014】この時の試験条件は次の通りである。触媒
を900℃の電気炉で窒素雰囲気下処理し活性の変化を
調べた。 ガス組成(容量基準) NO1% CO1% ヘリウム98% 空間速度 12500/Hr 測定方法 固定床流通式により反応を行いガスクロマトグラフィー
によりNOのN2 への転換率を求めた。反応温度は30
0℃である。The test conditions at this time are as follows. The catalyst was treated in an electric furnace at 900 ° C. under a nitrogen atmosphere to examine the change in activity. Gas composition (volume basis) NO1% CO1% Helium 98% Space velocity 12,500 / Hr Measuring method The reaction was carried out by a fixed bed flow system, and the conversion rate of NO to N 2 was determined by gas chromatography. Reaction temperature is 30
It is 0 ° C.
【0015】なお、貴金属はパラジウムを用いた場合に
ついて説明したがパラジウムの他に一部または全部を白
金、ロジウムを用いても同様の効果が得られた。Although the case where palladium is used as the noble metal has been described, the same effect can be obtained by using platinum or rhodium in part or in whole in addition to palladium.
【0016】[0016]
【発明の効果】以上説明したように本発明の触媒組成物
は希土類元素を含有するペロブスカイト型複合酸化物と
希土類酸化物と酸化アルミニウム、酸化鉄、及びカルシ
ウムまたはバリウムのうち1種以上の酸化物さらに貴金
属のうちの1種以上からなり、500℃以上の高温の雰
囲気中においても貴金属の粒成長やペロブスカイト複合
酸化物中への拡散を抑制する耐久性の優れた触媒であ
る。As described above, the catalyst composition of the present invention comprises a perovskite complex oxide containing a rare earth element, a rare earth oxide, aluminum oxide, iron oxide, and at least one oxide of calcium or barium. Furthermore, it is a catalyst which is made of one or more of the noble metals and has excellent durability that suppresses the grain growth of the noble metals and their diffusion into the perovskite complex oxide even in a high temperature atmosphere of 500 ° C. or more.
【図1】本発明の一実施例と比較例の触媒性能の耐久性
を示す図FIG. 1 is a diagram showing durability of catalyst performance of an example of the present invention and a comparative example.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 平島 文明 静岡県浜松市高塚町300番地 スズキ株式 会社内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Fumiaki Hirashima 300, Takatsukacho, Hamamatsu City, Shizuoka Prefecture Suzuki Stock Company
Claims (1)
合酸化物と希土類酸化物と酸化アルミニウムと酸化鉄、
及びカルシウムまたはバリウムのうちの1種以上の酸化
物、さらに貴金属のうちの1種以上からなる触媒組成
物。1. A perovskite complex oxide containing a rare earth element, a rare earth oxide, aluminum oxide and iron oxide,
And a catalyst composition comprising one or more oxides of calcium or barium, and one or more of noble metals.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3199111A JPH0538448A (en) | 1991-08-08 | 1991-08-08 | Catalyst composition |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3199111A JPH0538448A (en) | 1991-08-08 | 1991-08-08 | Catalyst composition |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0538448A true JPH0538448A (en) | 1993-02-19 |
Family
ID=16402312
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP3199111A Pending JPH0538448A (en) | 1991-08-08 | 1991-08-08 | Catalyst composition |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0538448A (en) |
-
1991
- 1991-08-08 JP JP3199111A patent/JPH0538448A/en active Pending
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